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		<title>Urquhart Repowering Project, Beach Island, South Carolina</title>
		<link>http://powergen.wordpress.com/2008/06/24/urquhart-repowering-project-beach-island-south-carolina/</link>
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		<pubDate>Tue, 24 Jun 2008 07:16:47 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Combined Cycle]]></category>
		<category><![CDATA[Gas Turbine]]></category>
		<category><![CDATA[Power Plant]]></category>
		<category><![CDATA[Repowering]]></category>
		<category><![CDATA[Beach Island]]></category>
		<category><![CDATA[GE]]></category>
		<category><![CDATA[Mark IV]]></category>
		<category><![CDATA[Retrofit]]></category>
		<category><![CDATA[South Carolina]]></category>
		<category><![CDATA[Urquhart Repowering Project]]></category>

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		<description><![CDATA[Owned and operated by South Carolina Electric &#38; Gas Co. For many utilities, repowering a 50-year-old coal-fired plant has become an attractive alternative to making expensive environmental upgrades to such a plant reaching the end of its useful life. Repowering is especially attractive if the plant&#8217;s existing water and air permits can be &#8220;recycled.&#8221; South [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=114&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span style="font-size:12pt;font-family:Times New Roman;">Owned and operated by South Carolina Electric &amp; Gas Co.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">For many utilities, repowering a 50-year-old coal-fired plant has become an attractive alternative to making expensive environmental upgrades to such a plant reaching the end of its useful life. Repowering is especially attractive if the plant&#8217;s existing water and air permits can be &#8220;recycled.&#8221; South Carolina Electric &amp; Gas Co. was able to do just that at its Urquhart Station a few years ago. By repowering the plant&#8217;s older two units and cross-connecting them with Unit 3, the utility boosted Urquhart&#8217;s overall efficiency and operating flexibility. Creative engineers found a way to squeeze every dollar of savings from this plant.</span></p>
<p><span id="more-114"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">By Skip Smith, Project Manager<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">South Carolina Electric &amp; Gas Co. (SCE&amp;G), a subsidiary of Scana Corp. (Columbia, S.C.), built the Urquhart Station&#8217;s original three coal-fired units—two 75-MW GE steam turbines and another rated at 100 MW—in the early 1950s. The plant (Figure 1) is located in Beach Island, S.C., on the Savannah River near Aiken City.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>1. Urquhart Station.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">South Carolina Electric &amp; Gas Co.&#8217;s 1950s-vintage Urquhart Station was repowered with two GE 7FA gas turbines using the two existing 75-MW steam turbines. Plant output increased from 250 MW to 550 MW.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: South Carolina Electric &amp; Gas Co.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">By 1999, environmental pressures, rapidly escalating maintenance costs, and service territory load growth were straining SCE&amp;G&#8217;s generating resources. The solution: Invest $228 million and repower the older two units to create a modern, combined-cycle facility based on GE 7FA gas turbines (GTs). The other GTs at the site are three 15-MW peakers installed in the 1960s and a 42-MW GE LM6000 simple-cycle peaker installed in 1999.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The repowered plant is an intermediate service plant, operated during times of high load demand. During the summer and winter months, the plant is generally operated 10 to 16 hours per day. For the first full year of operation, GT-1 produced 541,000 MWh and GT-2 produced 520,000 MWh. The plants operated 4,668 and 4,544 hours, respectively.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Beyond the addition of a badly needed 300 MW, the repowering project promised other benefits:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">It would allow SCE&amp;G to retain Urquhart&#8217;s well-trained workforce.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">It would allow retention of the plant&#8217;s water discharge permit.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">By effecting a significant drop in NOx, SO2, and particulate emissions from Urquhart, the project would delay the need for SCE&amp;G to install a selective catalytic reduction system on one of its other coal-fired plants (Figure 2).<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>2. Repowering benefits.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The repowering project enabled Urquhart Station to retain its existing water discharge permit. But perhaps more important, the reduction in emissions that resulted from removing the old coal-fired Units 1 and 2 from service enabled SCE&amp;G to delay the installation of a selective catalytic reduction system on one of its other coal-fired plants.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: South Carolina Electric &amp; Gas Co.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Upon commissioning of the new combined-cycle plant, Units 1 and 2 were taken out of service. Unit 3—rated at 100 MW—was kept on-line. As a result, the new plant has an output of 550 MW.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Duke/Fluor Daniel was selected as the EPC contractor for the repowering project in April 2000. Site preparation began that spring, and construction began in September 2000 immediately following receipt of an air permit for the plant. First fire was in March 2002, and the plant was declared commercial on June 1, 2002—ahead of schedule.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Greater operating flexibility<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The new Urquhart Station has a 1 x 1 combined-cycle configuration. Each GE 7FA exhausts into a Nooter/Eriksen (St. Louis, Mo.) heat-recovery steam generator (HRSG). Steam conditions are 1,440 psig/1,000F superheat and 1,000F/366 psig reheat. The HRSGs are single-pressure units configured as follows: reheater-HP superheat 2-HP superheat 1-HP evaporator-HP economizer-Unit 3 feedwater heating.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">One of the plant&#8217;s unique features is the cross-connection of the steam turbines for improved operational flexibility. In fact, both 75-MW steam turbines can be operated with a single gas turbine under steady-state conditions (Figure 3). These cross ties include hot and cold reheat connections for the reheat steam turbines. The reheat cross connection was predicated on an innovative design by Duke/Fluor Daniel and GE. The flexibility of this &#8220;semi-plant&#8221; mode of operation provides for more timely and economic dispatch of the facility.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>3. Flexibility.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Plant main steam is cross-connected to the two 75-MW steam turbines for improved operating flexibility. Both steam turbines can be operated with a single combustion turbine.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: South Carolina Electric &amp; Gas Co.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">The design also allows the cold start of both steam turbines by one gas turbine. A cascading steam bypass from the HRSG to the condenser using the cold and hot reheat lines allows each GT to continue operating when both steam turbines are out of service. As part of the project, the steam turbines and generators of Units 1 and 2 were refurbished and upgraded to make them compatible with combined-cycle operation.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Another unique feature of the facility design is the use of steam generated by the HRSGs of repowered Units 1 and 2 to heat HP feedwater for the existing Unit 3 steam turbine (Figure 4). This not only increases the operational efficiency of Unit 3 but also the operational flexibility of the overall plant.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>4. Steam use.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Steam generated by the HRSGs of the repowered Units 1 and 2 is used to heat the HP feedwater of the existing Unit 3 steam turbine. The net effect is an improvement in the overall plant&#8217;s efficiency and operating flexibility.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: South Carolina Electric &amp; Gas Co.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Other areas of the plantthat were upgraded included the fuel oil backup system for the gas turbines and the chiller for their inlet air. The latter step, which boosted output of the GTs by up to 20 MW, entailed the installation of inlet coolers from Caldwell Energy and Environmental Inc. (Louisville, Ky.). The plant&#8217;s 1.2-million-gallon oil tank can supply both gas turbines for five 16-hour operating days.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Control upgrades included a new distributed control system (a Westinghouse Ovation), the addition of a GE Mark VI system for controlling the Unit 3 steam turbine, and new electro-hydraulic controls for the steam turbine control valves. Balance-of-plant upgrades weren&#8217;t overlooked either: Higher-capacity demineralized water system and condensate pumps were added to complement the existing water treatment system (Figure 5).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>5. Control system.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">A new plant distributed control system was added along with a new GE Mark VI control system for the Unit 3 steam turbine.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: South Carolina Electric &amp; Gas Co.</span></p>
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		<title>Fish-friendly hydro turbines move center stage</title>
		<link>http://powergen.wordpress.com/2008/06/24/fish-friendly-hydro-turbines-move-center-stage-2/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/fish-friendly-hydro-turbines-move-center-stage-2/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:10:51 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Environmental]]></category>
		<category><![CDATA[Power Plant]]></category>

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		<description><![CDATA[Hundreds of U.S. hydro plants come due for license renewal over the next decade, giving river and wildlife advocates an ideal time to push for fish-friendly turbine retrofits. With these new, e-&#8221;fish&#8221;-ent turbines, early retrofit projects have targeted up to 98% fish-passage efficiency and up to 15% more power output. The 91,000 MW of hydropower [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=96&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
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<blockquote><p><span style="font-size:12pt;font-family:Times New Roman;">Hundreds of U.S. hydro plants come due for license renewal over the next decade, giving river and wildlife advocates an ideal time to push for fish-friendly turbine retrofits. With these new, e-&#8221;fish&#8221;-ent turbines, early retrofit projects have targeted up to 98% fish-passage efficiency and up to 15% more power output.<br />
</span></p></blockquote>
<p><span style="font-size:12pt;font-family:Times New Roman;">The 91,000 MW of hydropower capacity in the U.S. comes from about 180 federal projects and more than 2,000 non-federal projects regulated by the Federal Energy Regulatory Commission (FERC). Although the country has substantial undeveloped hydropower resources, little new construction is expected, and hydropower&#8217;s share of the nation&#8217;s generation is predicted to decline through 2020, due to a combination of environmental issues, regulatory pressures, and changes in energy economics.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">FERC is the lead permitting agency for private hydroelectric plants. The U.S. Fish and Wildlife Service for the eastern part of the country, and the National Marine Fishery Service for the western part, are other agencies that make recommendations on fish mortality goals. In response to the 1986 Electric Consumers Protection Act, these agencies have set their target as &#8220;no fish production loss&#8221; for all new hydro projects as well as for any projects for which the hydraulic lease is expiring. That last phrase is key, because there are hundreds of plants in the U.S. that must pass through the relicensing minefield over the next decade. About 80% of California&#8217;s hydropower is subject to a FERC license, and about half of those facilities—approximately 4,000 MW at 150 projects—are due for license renewal in the next 15 years.</span></p>
<p><span id="more-96"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Save the fish<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Turbines installed decades ago were designed with one thing in mind: maximizing power output. Although fish ladders were typically built for migratory fish, little thought was given to the side effects of fish injury and mortality caused by passage through the turbines or lower levels of dissolved oxygen in downstream water. Fish mortality rates currently range from 5% for the least-harmful existing turbines to more than 30% for more-damaging turbines.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Fortunately, special fish-friendly designs developed over the past decade have come into operation at several hydro power stations, significantly improving fish-passage efficiency while increasing power output. In fact, the repowering of projects built 50 years ago could eventually improve plant output by as much as 15%, thereby making a fish-friendly retrofit project economically feasible. The fish win, and so do plant owners and electric consumers.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Turbine-passage survival is a complicated function of gap sizes, runner blade angles, wicket gate openings and overhang, and water passageway flow patterns (see box). The consequence to fish populations of unaccommodating turbines is especially serious among migratory species—such as salmon, steelhead, and American shad—and eels that must pass downstream all the way to the sea, perhaps through multiple turbines, to complete their life cycle. That&#8217;s why increasing the passage efficiency of juvenile salmonids at Pacific Northwest hydro plants is one of the major challenges facing the industry. According to the Bonneville Power Authority (BPA), juvenile salmonids outmigrating to the Pacific Ocean through the Columbia River Basin during high spring flows experience a 5% to 25% mortality rate at each hydroelectric project they encounter. During this time, BPA—already teetering on the verge of bankruptcy and rising electricity costs—must reduce its power generation potential by $160 million per year through increased spills and other operations designed to increase fish-passage efficiency.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The U.S. Army Corps of Engineers operates eight multipurpose dams on the lower Columbia and Snake Rivers as part of the Federal Columbia River Power System. The Corps&#8217; Columbia River Fish Mitigation program focuses on improving the passage of adult and juvenile salmon either around these dams with fish screens or through them with expensive fish-bypass structures. The Corps estimates that it will spend $1.4 billion implementing its fish-mitigation program, according to a 1998 report. About $908 million of this total will be spent on the construction of fish-passage projects and related studies from fiscal year 1999 through the scheduled completion of the program in fiscal year 2007, although currently shrinking budgets may place this goal in jeopardy.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>New turbine designs arrive<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The goal of the U.S. Department of Energy&#8217;s (DOE&#8217;s) Advanced Hydropower Turbine System (AHTS) program is to develop technology that will maximize the country&#8217;s hydropower resources while minimizing adverse environmental effects. The AHTS program is closely coordinated with industry and other stakeholders—such as Public Utility District No. 2 of Grant County (Washington), the Electric Power Research Institute, Corps of Engineers, U.S. Bureau of Reclamation, BPA, and National Marine Fishery Service—which all have a part to play in implementing advanced turbine designs.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The survival of turbine-passed fish depends greatly on characteristics of both the hydropower plant—the type and size of the turbine, environmental setting, and mode of operation—and the entrained fish—species, size, and physiological condition. Some small, Pelton-type turbines designed for high-head installations most likely cause complete mortality due to their basic design (Figure 2). On the other hand, the survival of small fish encountering turbine types with larger water passages—such as Kaplan, Francis, and bulb turbines—is commonly 70% or greater for current plants (Figure 3). Among the most fish-friendly conventional turbines, large Kaplan turbines used at the mainstem Columbia and Snake River dams have shown average fish survival (including both direct and indirect effects) of about 88% (Figure 4).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>2. Pelton turbine: nearly 100% mortality<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">In a Pelton or impulse turbine, the water is directed onto clamshell buckets attached to the periphery of the impeller wheel to impart a torque on the turbine impeller. High rotating speeds and tight clearances mean almost 100% fish mortality.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: VA Tech Hydro</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>3. Kaplan turbine<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">This cross section of a fish-friendly Kaplan turbine shows the details of the stay vanes, wicket gates, and runner with hub and water passages. Water enters through the semi-spiral case, passes through the stay vanes and wicket gates, then through the runner, and finally into the draft tube, exiting to the tail waters.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Voith Siemens Hydro</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>4. Francis turbine<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Francis turbines for power generation typically are used where high flow rates are available at medium hydraulic head—such as the world-famous Niagara Falls. Water enters the turbine through a volute casing and is directed onto the blades by wicket gates. The low-momentum water then exits the turbine through a draft tube.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: VA Tech Hydro</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">That&#8217;s why new fish-friendly turbine designs are a vital part of hydro&#8217;s future. The U.S. Department of Energy&#8217;s Advanced Hydropower Turbine System program has identified specific injury mechanisms, which include:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Turbulent flows or cavitation in turbine water passages resulting from low-efficiency designs or plant operating strategies where extremely low water pressures cause the formation of vapor bubbles, which subsequently collapse violently.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Turbulent flows and the trapping and cutting of fish in the zone of flow passing near the turbine hub when large gaps between blade and hub exist (characterizing the lower-output operation of Kaplan turbines).<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Strike of fish by turbine blades or impact of fish on structures including runner blades, stay vanes, wicket gates, and draft tube piers.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Shear stress when two bodies of water of different velocities collide across a fish&#8217;s body. The highest values of shear stress are found close to the interface between the flow and solid objects it speeds by, such as the blade leading edges, vanes, and gates.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Rapid and extreme pressure changes (water pressures within the turbine may increase to several times atmospheric pressure, then drop to sub-atmospheric pressure, all in a matter of seconds).<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Abrasion and grinding: Abrasion occurs with the rubbing action of a fish against rough turbine surfaces by flow turbulence and is dependent on flow discharge and velocity, number and spacing of turbine blades, and the geometry of flow passages. Grinding injury can occur when a fish is drawn into small clearances (gaps of sizes close to that of the fish) within the turbine system.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Testing of new designs with fish-friendly features has demonstrated even higher survival rates. The mission of the AHTS program has been to develop turbines that achieve 98% survival of turbine-passed fish.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Corkscrew turbine uncorked<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The original AHTS design teams selected by the DOE in 1995 are still involved in bringing the fish-friendly designs to market. They are:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Alden Research Laboratory (ARL, Holden, Mass.);<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Concepts NREC (White River Junction, Vt.), which was formed by the merger of Concepts ETI with Northern Research and Engineering Corp; and<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Voith Siemens Hydro Power Generation Inc (Heidenheim, Germany; U.S. office: York, Pa.) with team members Georgia Tech, Tennessee Valley Authority (TVA), MWH Consultants, and Normandeau Associates.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">The latest ARL-designed runner (the &#8220;runner&#8221; in a hydro turbine is analogous to an impeller in a pump) uses only three long blades, which are wrapped around the central hub in a corkscrew shape to gradually reduce pressure and minimize blade-induced injuries. This is much different than the 6 to 10 blades found on most traditional hydro turbines. The new runner minimizes the number of blade leading edges, reduces the pressure-versus-time and the velocity- versus-distance gradients within the runner, minimizes clearance between the runner and runner housing, and maximizes the size of flow passages.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">End result: Fish get more room in the water to swim through the turbine on their way to upstream spawning grounds or downstream to the ocean (Figure 5).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>5. New runner: nearly 100% survival<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Alden Research Lab designed a fish-friendly runner that minimizes internal clearances and maximizes flow passages with a minimal impact on turbine efficiency. Tests have demonstrated fish survival rates approaching 99%.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: U.S. Department of Energy</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Despite its dramatically different geometry, the new turbine has a predicted efficiency of only a few percentage points lower than a conventional turbine, although the power density is reduced. This means that, for modernizing a plant, the volume of the power house must increase to produce the same power output. For this reason the ARL design will focus on new installations. &#8220;The new fish-friendly turbine is expected to be used for new generation capacity, as replacements for existing turbines, and in fish-diversion systems installed near the main turbines,&#8221; says Thomas Cook, project manager for ARL. &#8220;We expect the cost of the new fish-friendly turbine to be comparable to existing hydraulic turbines.&#8221; Testing of a 2,000-hp full-scale model demonstrated control fish survival up to 99%, depending on fish size and turbine head. ARL has obtained patents for the new designs.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>E-&#8221;fish&#8221;-ent turbines<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">For its contribution to the AHTS program, Voith Siemens Hydro (VSH) proposed building on the success of ongoing internal R&amp;D programs and investigating the impact of existing turbine designs in relation to fish passage efficiency and developing new turbine designs that improve efficiency and reduce environmental effects for rehab projects. The results include design concepts for improved fish- passage survival in Kaplan and Francis turbines as well as designs for boosting dissolved oxygen levels in discharges from Francis turbines.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Elements of the advanced Kaplan designs were implemented in rehabilitated units recently installed at the Chelan County Public Utility District&#8217;s Rocky Reach powerplant, at the Corps of Engineers&#8217; Bonneville Dam, and at the Tennessee Valley Authority&#8217;s (TVA&#8217;s) Kentucky Dam. An even more advanced design has been developed and model-tested for the Grant County Public Utility District&#8217;s Wanapum Dam. These fish-friendly designs generally focused on modifications to a Kaplan turbine that eliminated runner gaps, improved blade shapes, and included an advanced control system to sense the presence of fish and adjust to fish-friendly operation (Figure 6). Other major VSH design features that came out of the AHTS program include:<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>6. Advanced Kaplan design<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Voith Siemens Hydro supplied the first 2 of 10 units being replaced at the Corps of Engineers Bonneville Powerhouse 1. The remaining eight units will be rehabilitated at the rate of one per year through 2008. Test on the first unit showed a fish survival rate of 93.8% to 97.5% for the MGR design.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Voith Siemens Hydro</span></p>
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<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">High efficiency over a wide operating range with reduced cavitation potential.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">A minimum gap runner (MGR) design, characterized as a design with a fully spherical discharge ring, no gap near the hub, and runner blades that tend to be thicker near the leading edge.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">A non-overhanging design for wicket gates.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Environmentally compatible hydraulic fluid and lubricants, and greaseless wicket gate bushing.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Smooth surface finishes in conjunction with upgrades for stay vanes, wicket gates, and draft tube cone.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">VSH and the Georgia Institute of Technology are employing computational fluid dynamics (CFD) simulations of turbulent jets to better understand the fluid stresses that fish experience as they pass through hydroelectric turbines. VSH is using the same CFD model to relate measured velocity fields in an experimental flume used to expose fish to shear and turbulence to predicted velocity fields in a turbine at the Wanapum Dam on the Columbia River. Additional software (VSH&#8217;s &#8220;Virtual Fish&#8221; model) is being used to estimate flow-induced loads on both flume-passed and turbine-passed fish.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">VSH has also developed several advanced computational tools for estimating trajectories of fish-like bodies passing through hydro turbines. The motion of the &#8220;virtual fish&#8221; is governed by a set of differential equations that account for the fish mass and various flow-induced forces. This model can be used not only to estimate the trajectory of a virtual fish from the forebay to the tailrace, but it also can provide specific information about a variety of flow-induced loads on fish passing through various zones of turbine flow.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Controls too<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The fish stand to benefit both from new turbine designs and from new control systems for those turbines. For example, VSH and TVA jointly developed new controls to operate their fish-friendly hydro turbines. And Hydro Resource Solutions (Norris, Tenn.) markets &#8220;WaterView,&#8221; the state of the art in real-time hydro plant performance optimization when constrained by factors such as fish-passage criteria, civitation limits, avoidance zones, and ramp rates. For example, WaterView can:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Limit turbine operation to fish-friendly modes when sensors indicate that fish are present and optimize plant performance whether fish are present or not.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Streamline the periodic updates of Kaplan turbine &#8220;digital cam surfaces&#8221; to most efficient operation at each head and flow, minimizing fish-injuring flow turbulence.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Sense active cavitation and limit turbine operation to noncavitating conditions.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Optimize plant output when fish are present to achieve targeted fish-passage survival based on fish presence, location, turbine-passage mortality, spillway fish mortality, fish bypass characteristics, and total dissolved gas generated during spilling.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Bonneville Dam<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The Corps of Engineers plans to install MGR on all 10 units at the Bonneville Powerhouse 1. The first units to be replaced were Unit 6—put into commercial operation on July 27, 1999—and Unit 4, which returned to service in September 1999. The remaining eight units will be rehabilitated at the rate of one per year through 2008.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The Corps conducted biological tests on Unit 6 after its retrofit to determine the unit&#8217;s ability to pass juvenile salmon safely. The survival of turbine-passed fish through Unit 6 was compared with the survival of fish passed through Unit 5, an adjacent, conventional Kaplan turbine. The goal of the biological testing was to determine if the MGR is at least equivalent to the existing machine in terms of fish-passage mortality. The biological tests, co-funded by the Corps, Grant County Public Utility District No. 2, DOE, and BPA, were conducted between November 1999 and January 2000 with a release of 7,200 balloon-tagged fish.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Overall injury rates among turbine-passed fish were impressively low for both units: 1.5% and 2.5% for the MGR and Kaplan unit, respectively. Survival rates of fish passing near the hub also were high (97% or greater) for both units, while survival rates for fish passing through the mid-blade region ranged from 95% to 97% and did not differ between units.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">At all four power levels tested, the MGR showed better survival rates than the conventional Kaplan for fish that passed near the blade tip. Survival for blade tip–released fish ranged from 90.8% to 95.6% for the conventional Kaplan and from 93.8% to 97.5% for the MGR.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Chelan County is first<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Public Utility District No. 1 of Chelan County in Washington State owns and operates the second-largest non-federal hydroelectric generating system in the U.S. The District&#8217;s three hydroelectric projects—Rocky Reach, Rock Island, and Lake Chelan—have a combined generating capacity of over 2,000 MW (Figure 7).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>7. Rocky Reach plant<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The Chelan County Public Utilities District is nearing completion of a major upgrade of all 11 units at its Rocky Reach plant.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: Chelan County Public Utility District</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Rocky Reach Units 1 to 7, six-bladed vertical Kaplan turbines rated 140,000 hp, were built in the early 1960s by Allis Chalmers (now VSH). Turbines for the remaining Units 8 to 11, originally vertical propeller turbines rated 177,000 hp, were built in the early 1970s.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In the early 1990s, Units 1 to 7 began experiencing severe runner blade cracking, starting at the interface between the blades and the trunnions and progressing diagonally into the blade leaves. In June 1994, after completing a round of competitive model testing, the District awarded a contract for the rehabilitation of Units 1 through 7 to Voith Riva Hydro (now VSH).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">While rehabilitation of Units 1 through 7 was moving forward, the rehabilitation of Units 8 to 11 became more pressing due to increased restrictions on unit operation to aid downstream fish passage. The VSH contract was amended to add turbine rehabilitation for Units 8 to 11.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">During the model development phase, new ideas related to the safe passage of juvenile fish through the turbines were identified, building on the Bonneville Powerhouse 1 designs. VSH completed additional testing and model development based on the elimination of wedge-shaped gaps between runner blades and adjacent components and minimizing the runner hub-blade gaps upstream and downstream of the blade trunnion.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Also, a fully spherical discharge ring was developed for Units 8 through 11, closing the gap between the runner blade periphery and the discharge ring along the entire length of the blade. This elimination of the upstream blade-hub gap was later applied to all 11 Rocky Reach turbines, as well as other hydroelectric projects along the Columbia River, such as the Wanapum and Bonneville.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Rehabilitation of all 11 Rocky Reach units is scheduled for completion this spring.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Grant County advances<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Last August, the DOE chose Washington State&#8217;s Grant County Public Utility District (PUD) to test a single fish-friendly turbine at its 1,038-MW Wanapum Dam on the Columbia River. &#8220;The new turbine is designed to allow salmon smolts to pass through the dam without injury,&#8221; says Stephen Brown, the PUD&#8217;s hydro engineering supervisor. But there&#8217;s also a nice side benefit: The proposed fish-friendly turbines are much more efficient than the existing turbines. The eventual uprating of all 10 Wanapum Dam units would provide an additional 300 MW of power to meet peak loads.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">New advances in understanding the correlation between the turbine operation point and fish survivability can also contribute to improved operating efficiencies on the mainstem dams. Tests of the existing turbines at Wanapum Dam used balloon-tagged fish to verify many of the fish mortality mechanisms. These tests clearly demonstrated increased fish survival rates at increased flow rates (beyond the turbines&#8217; &#8220;best-efficiency&#8221; points). The result: increased power generation and improved fish-passage survival.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">These results counter the conventional hydro plant wisdom that says fish survival is reduced under conditions of very low operating efficiency. Fish-passage studies of Kaplan turbines at Lower Granite, Rocky Reach, and Wanapum Dams have all failed to detect a direct relationship between the &#8220;1% of peak turbine efficiency&#8221; target that is employed in the Columbia River basin and probability of highest survival.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">&#8220;Our goal is to lessen injury on fish,&#8221; according to Brown. &#8220;We are looking for a 98% survival rate.&#8221; Brown said the federal government is picking up half of the $2.5-million engineering and biological testing cost. Grant PUD will cover the other $2.5 million, plus the cost of the turbine and installation, for a total of $14.5 million. The new turbine is scheduled for installation in late 2004, with testing set for spring 2005.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>McNary Dam rehab<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">McNary Dam, at 7,265 ft long and 183 ft high—one of the largest hydroelectric power facilities in the U.S.—is among a succession of dams on the Columbia River between Oregon and Washington that must be navigated by salmon during their annual downstream migration to the ocean. After nearly 50 years of constant use, the turbines at McNary Dam are being studied by the BPA and the Corps of Engineers for total replacement during a 13-year powerhouse overhaul. In June 2002, four contracts were awarded to firms specializing in manufacturing large hydroelectric turbines:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">VSH;<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Alstom Power (Littleton, Colo.);<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">G.E. Hydro Power (Pleasanton, Calif.); and<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">VA Tech Voest MCE (Charlotte, N.C.).<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Each of these firms will design, build, and test scale models of a new turbine they would propose to install at McNary. The full-size turbine will be subjected to in-stream biological testing and evaluated for both fish survival and hydraulic performance. The test results will be incorporated as part of the National Environmental Policy Act analysis required for the rehab permit.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">&#8220;The outcome of the testing, analysis, and the public input process could lead to a federal decision to replace all 14 of the existing 80-MW Kaplan turbines,&#8221; said Kevin Crum, project manager for the Corps of Engineers.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Fish gotta breathe too<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Mechanical injury is not the only fish- damaging aspect of hydro turbines. Dissolved oxygen (DO) levels downstream of a powerhouse tend to drop during warm months, effectively suffocating fish that had successfully passed through the turbines. This is a particular problem in the U.S. Southeast.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In the 1980s, VSH and TVA invested in a joint research partnership to enhance DO concentrations in releases from Francis-type turbines. &#8220;Auto-venting&#8221; (AVT), or &#8220;self-aerating&#8221; turbines, which use the low pressures created by flows entering the turbine to induce additional airflows, typically are the most cost-effective technologies for Francis turbines (Figure 8).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>8. Adding air to water<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Voith Siemens Hydro has revolutionized the design of auto-venting turbines by the use of hollow blades and aerating holes that increase the amount of dissolved oxygen added to the water passing through the turbine.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Voith Siemens Hydro</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">In the last 10 years, significant progress has been made. TVA has developed reliable line diffuser technologies and surface-water pumps for low-cost aeration of reservoirs upstream of hydro plants and effective labyrinth weirs and infuser weirs for aerating downstream flows.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">TVA&#8217;s Norris Dam was selected as the first site to demonstrate the AVT technologies. The two Norris AVTs have specially shaped turbine component geometries developed to enhance low pressures at locations for aeration outlets in the turbine water passage, to draw air into an efficiently absorbed bubble cloud, and to minimize aeration auxiliary power. Results show that up to 5.5 mg/l of additional DO uptake can be obtained for single-unit operation with all aeration options operating. In this case, the amount of air aspirated by the turbine is more than twice that obtained in the original turbines with hub baffles. Compared to the original turbines at the plant, these specially designed replacement units increased overall efficiency 3.5% and increased capacity by 10%. The new runners also have shown significant reductions in both cavitation and vibration.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The first uprated and rehabilitated AVT was recently returned to service at the Corps of Engineers&#8217; J. Strom Thurmond plant in Clarks Hill, South Carolina. The 48-yr-old plant—yes, it was named for the ageless senator that long ago—is being upgraded with Francis runners designed to increase the levels of DO in rivers with depleted or diminished gas content. Seasonal stratifications result in the discharge of water with less than 1 mg/l DO during the summer months as far as 16 miles downstream from the dam. Georgia and South Carolina have a standard of 5 mg/l for that portion of the Savannah River.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The modified Francis turbine design includes fewer blades, improved blade shapes, and larger spaces between blades that improve fish-passage survival as well. Initial tests last September of the first installed unit showed DO improvement of slightly more than 4.0 mg/l with minimal impact on turbine efficiency.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The first of seven new aerating turbines arrived at J. Strom Thurmond in March 2002. The second turbine is due to arrive March 2003, and by 2006 all seven should be installed and operating.</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">By Dr. Robert Peltier, PE, Sr. Editor</span></td>
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		<title>How fish-friendly turbines work</title>
		<link>http://powergen.wordpress.com/2008/06/24/how-fish-friendly-turbines-work/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/how-fish-friendly-turbines-work/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:09:25 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Environmental]]></category>
		<category><![CDATA[Power Plant]]></category>

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		<description><![CDATA[Quantifying the fish injuries caused by a hydroelectric turbine often has been based more on model predictions than actual measurements. Survival rates measured for fish passing directly through a modern large turbine range from 88% to 94%. By comparison, fish bypass system survival rates typically range from 95% to 98% percent and from 95% to [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=88&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span style="font-size:12pt;font-family:Times New Roman;">Quantifying the fish injuries caused by a hydroelectric turbine often has been based more on model predictions than actual measurements. Survival rates measured for fish passing directly through a modern large turbine range from 88% to 94%. By comparison, fish bypass system survival rates typically range from 95% to 98% percent and from 95% to 99% percent for a spillway system.</span></p>
<p><span id="more-88"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">It&#8217;s important to realize, however, that the net survival rates are substantially lower, because each fish has to pass through several turbines during its long journey to the sea (Figure 1).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">1. Hydro turbine system: Fish-passage issues<br />
</span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0715-howfishfrie1.jpg?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Turbine-passage survival is a complicated function of gap sizes, runner blade angles, wicket gate openings and overhang, and water passageway flow patterns.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: U.S. Department of Energy</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">That&#8217;s why new fish-friendly turbine designs are a vital part of hydro&#8217;s future. The U.S. Department of Energy&#8217;s Advanced Hydropower Turbine System program has identified specific injury mechanisms, which include:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Turbulent flows or cavitation in turbine water passages resulting from low-efficiency designs or plant operating strategies where extremely low water pressures cause the formation of vapor bubbles, which subsequently collapse violently.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Turbulent flows and the trapping and cutting of fish in the zone of flow passing near the turbine hub when large gaps between blade and hub exist (characterizing the lower-output operation of Kaplan turbines).<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Strike of fish by turbine blades or impact of fish on structures including runner blades, stay vanes, wicket gates, and draft tube piers.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Shear stress when two bodies of water of different velocities collide across a fish&#8217;s body. The highest values of shear stress are found close to the interface between the flow and solid objects it speeds by, such as the blade leading edges, vanes, and gates.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Rapid and extreme pressure changes (water pressures within the turbine may increase to several times atmospheric pressure, then drop to sub-atmospheric pressure, all in a matter of seconds).<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Abrasion and grinding: Abrasion occurs with the rubbing action of a fish against rough turbine surfaces by flow turbulence and is dependent on flow discharge and velocity, number and spacing of turbine blades, and the geometry of flow passages. Grinding injury can occur when a fish is drawn into small clearances (gaps of sizes close to that of the fish) within the turbine system.<br />
</span></li>
</ul>
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		<title>On-line cleaning of trans.former oil boosts reliability, dielectric properties</title>
		<link>http://powergen.wordpress.com/2008/06/24/on-line-cleaning-of-transformer-oil-boosts-reliability-dielectric-properties/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/on-line-cleaning-of-transformer-oil-boosts-reliability-dielectric-properties/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:08:42 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Power Plant]]></category>

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		<description><![CDATA[A technology called balanced-charge agglomeration (BCA) has proven its ability to restore oil to cleaner-than-new conditions in a variety of applications. BCA accelerates particulate agglomeration and removal of sub-micron material, eliminates the water-holding particles upon which emulsions form, and allows for faster and more complete water removal. Oil condition data published in 2001 makes reference [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=86&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<div>
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<td style="padding-top:7px;padding-left:7px;padding-right:7px;"><span style="font-size:12pt;font-family:ARIAL;">A technology called balanced-charge agglomeration (BCA) has proven its ability to restore oil to cleaner-than-new conditions in a variety of applications. BCA accelerates particulate agglomeration and removal of sub-micron material, eliminates the water-holding particles upon which emulsions form, and allows for faster and more complete water removal.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;">Oil condition data published in 2001 makes reference to the first application of this technology on steam-turbine lube oil. The research trial ran for more than five years and concluded that the lube oil tested at 16 times cleaner than new oil specifications (Figure 1). The technique essentially supercharges the filtration process by electronically removing sub-micron material and products of oxidation together, for removal by standard and proprietary filters.</span></p>
<p><span id="more-86"></span></p>
<p><span style="font-size:12pt;font-family:ARIAL;"><strong>1. Close-up of a compressor bearing<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0714-onlineclean1.jpg?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">The balanced-charge agglomeration process, which removes sub-micron contamination, has proved its ability to restore lubricating oil in rotating machinery. The on-line cleaning process is now applied to transformer fluids to boost dielectric resistance.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">Source: ISOPur Fluid Technology</span></p>
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<p><span style="font-size:12pt;font-family:ARIAL;">This process also can be applied to high-voltage transformer fluid, where it can increase the dielectric resistance of insulating fluids to better-than-new standards. In fact, recent studies suggest that particulate contamination may be as significant as water contamination in reducing the reliability of transformers and tap changers. As effective as water removal is in improving electrical resistance, removing these fine particles boosts dielectric strength even higher and blocks the pre-varnish discoloration that often is seen forming in tap-changer oil and on the contacts. During a typical on-line clean-up cycle, transformer oil was restored from 20 kV to 75 kV, preventing transformer downtime and improving equipment performance.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;">During a typical clean-up of transformer fluid for an industrial environment, particle count was reduced to such a low level that the dielectric strength was improved from 35 to 90 kV. This increase in kV resistance is much better than new oil specs, with the net result that the useful life of the oil is dramatically extended. Using a combination of the fluid technology process to remove sub-micron material together with a vacuum distillation process to reduce water contents to below 10 ppm and gas to less than 0.08% by volume results in fluid that has the maximum kV value attainable (Figure 2).<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;"><strong>2. Extending oil life<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0714-onlineclean2.jpg?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">Varnish that normally forms in fluid systems plates out in the fluid-collection cartridge. Because the spaces in the collection cartridge range from 50 to 300 microns, a large amount of sub-micron material and products of oxidation can be eliminated from the fluid.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">Source: ISOPur Fluid Technology</span></p>
</td>
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</tbody>
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<p><span style="font-size:12pt;font-family:ARIAL;">From hydraulic fluid at a major auto parts manufacturer to tap-changer switchgear, turbines, and compressors, dramatic reductions in particulates and the products of oxidation have documented the effectiveness of the BCA process. The process induces reformation of varnish within a fluid-collection cartridge, depositing varnish and sludge onto the proprietary depth media cartridge. Previous early indicators of films forming on switchgear in tap changers does not appear in the BCA-protected apparatus.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;">Recently, a new system incorporating a low-maintenance PetroTech vacuum dehydrator was installed at a major utility site in the Northeast. In addition to the significantly reduced particle counts, water and gas quickly dropped to extremely low levels (Figure 3). The proven ability to address all aspects of transformer oil condition using one cost-effective portable system has motivated ISOPUR Fluid Technology Inc (Rocky Hill, Conn.) to design smaller, permanent units with remote monitoring capabilities for installation on critical or troubled (high-maintenance) equipment.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;"><strong>3. PetroTech vacuum dehydrator<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0714-onlineclean3.jpg?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">During a typical clean-up of transformer fluid in an industrial environment, particle count was reduced to such a low level that the dielectric strength improved from 35 to 90 kV.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:ARIAL;">Source: ISOPur Fluid Technology</span></p>
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</tbody>
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<p><span style="font-size:12pt;font-family:ARIAL;">Standard mechanical filtration can remove larger particles but has no impact on the millions of smaller particulate matter that can easily pass through the filter and accumulate in critical equipment. These small particles pick up a low uniform static charge, causing the formation of varnish and sludge due to their attraction to grounded internal surfaces. The BCA process can gather together particles below the one-tenth micron size and remove them from the fluid. Because most soot particles range from one-tenth to three-tenths micron, the normal drop in kV resistance over time is eliminated. By creating floods of equal and opposite-charged particles, the BCA process eliminates net static charge and blocks varnish formation.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;">Essentially, the varnish that normally forms in machines plates out in the fluid-collection cartridge due to the BCA process. Because the spaces in the collection cartridge range from 50 to 300 microns, a large amount of sub-micron material and products of oxidation can be collected before change-out is required. A typical cartridge life is one year. Typical fluid life is expected to be measured in decades, even with troubled systems.<br />
</span></p>
<p><span style="font-size:12pt;font-family:ARIAL;">By Gerald Munson and C. Wesley Mitchell, ISOPUR Fluid Technology, and R. Haig Hachadoorian, Petroleum Technology Inc</span></td>
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</table>
</div>
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		<title>Canadian utility mixes oil and water</title>
		<link>http://powergen.wordpress.com/2008/06/24/canadian-utility-mixes-oil-and-water/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/canadian-utility-mixes-oil-and-water/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:07:57 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[New Construction]]></category>
		<category><![CDATA[New Technology]]></category>

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		<description><![CDATA[NB Power&#8217;s (Fredericton, N.B.) 1,050-MW Coleson Cove station has received approval to begin a $475-million refurbishment that includes a fuel switch from heavy oil to Orimulsion, environmental equipment upgrades, and a new pipeline and offshore unloading system to deliver the fuel to the plant. The upgrades to the three identical units at the plant are [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=82&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span><br />
<span style="font-size:12pt;font-family:Times New Roman;">NB Power&#8217;s (Fredericton, N.B.) 1,050-MW Coleson Cove station has received approval to begin a $475-million refurbishment that includes a fuel switch from heavy oil to Orimulsion, environmental equipment upgrades, and a new pipeline and offshore unloading system to deliver the fuel to the plant. The upgrades to the three identical units at the plant are required to meet new environmental standards that take effect in 2005. Coleson Cove, located in the Lorneville area of west Saint John, currently supplies over 30% of New Brunswick&#8217;s electrical power. The upgrade project is scheduled for completion in the fall of 2004.</span></span></p>
<p><span id="more-82"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><span>Orimulsion is a liquid fossil fuel consisting of 70% bitumen and 30% water. Bitumen is a highly viscous, naturally occurring petroleum hydrocarbon from the Orinoco belt region of Venezuela. To facilitate pumping and transportation (a larger pipeline to carry the additional mass flow is required), the natural bitumen must be mixed with water.<br />
</span></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><span>Coleson Cove will become the second powerplant in North America to use Orimulsion; NB Power has successfully used Orimulsion at its 300-MW Dalhousie station since 1994.<br />
</span></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><span>&#8220;The impact of Coleson Cove on the environment was a major factor in approving this project,&#8221; Environment and Local Government Minister Kim Jardine said. &#8220;The refurbishment will reduce SO2 emissions by 77%, particulate matter by 75%, and NOx by 70%. We can pay for the new NOx controls, flue gas desulphurization scrubbers, and wet electrostatic precipitator upgrades to the plant by switching fuel sources from heavy oil to Orimulsion.&#8221;<br />
</span></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><span>In addition to NB Power, other power producers firing Orimulsion include Energi E2 in Denmark; RWE Systems in Germany; Lithuanian State Power System; ENEL in Italy; Hokkaido Electric Power and Kashima Kita Electric Power in Japan; China National United Oil Corp in the People&#8217;s Republic of China; and PowerSeraya in Singapore.<br />
</span></span><span><br />
</span></p>
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		<title>Control system upgrades can save big bucks</title>
		<link>http://powergen.wordpress.com/2008/06/24/control-system-upgrades-can-save-big-bucks/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/control-system-upgrades-can-save-big-bucks/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:07:14 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[New Technology]]></category>
		<category><![CDATA[Power Plant]]></category>

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		<description><![CDATA[The decision to upgrade powerplant control systems is not a simple one; however, the economic payoff can be substantial. Recent studies by Siemens Westinghouse (Newcastle, UK) indicate that improvements in plant performance thorough controls modernization can be substantial. For a typical 540-MW coal-fired powerplant, instrumentation and controls changes are projected to save a combined $1.8 [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=81&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span style="font-family:Times New Roman;font-size:12pt;">The decision to upgrade powerplant control systems is not a simple one; however, the economic payoff can be substantial. Recent studies by Siemens Westinghouse (Newcastle, UK) indicate that improvements in plant performance thorough controls modernization can be substantial. For a typical 540-MW coal-fired powerplant, instrumentation and controls changes are projected to save a combined $1.8 million per year:<br />
</span></p>
<ul>
<li><span style="font-family:Times New Roman;font-size:12pt;">Fuel savings during normal operation: 0.4%—or $283,000/yr—is possible, mostly from tighter steam-temperature control, more accurate combustion and oxygen control, and conversion from fixed-pressure to sliding-pressure operation.<br />
</span></li>
<li><span style="font-family:Times New Roman;font-size:12pt;">Fuel savings during startup: 50%—approximately $17,000/yr—is possible. Automated controls enable a plant to adhere more closely to stress limitations.<br />
</span></li>
<li><span style="font-family:Times New Roman;font-size:12pt;">Fuel savings during load ramps: It is possible to achieve load-ramp rates of 5% of MCR/min above 60% load and 3%/min between 35% and 60% load. Improved ramp rates allow the unit to respond faster, thus &#8220;catching&#8221; higher market prices and reducing load quicker when the market prices drop. Savings are estimated at $532,000/yr.<br />
</span></li>
<li><span style="font-family:Times New Roman;font-size:12pt;">Fuel savings due to reduced forced-outage rates: National Electric Reliability Council data indicate that the average forced outage rate for a coal-fired unit lasts about 20 hours. If a plant can reduce that figure by more intelligent controls, safe run-back to partial loads instead of a trip, and improvements in trip-system reliability, then it can save just over $1 million/yr.<br />
</span></li>
</ul>
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		<title>Gas turbine combustors drive emissions toward nil</title>
		<link>http://powergen.wordpress.com/2008/06/24/gas-turbine-combustors-drive-emissions-toward-nil/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/gas-turbine-combustors-drive-emissions-toward-nil/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:06:14 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Environmental]]></category>
		<category><![CDATA[Gas Turbine]]></category>
		<category><![CDATA[Low NOx]]></category>
		<category><![CDATA[New Technology]]></category>
		<category><![CDATA[Power Plant]]></category>

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		<description><![CDATA[Best available control technology continues to be ratcheted down to achieve ever-lower NOx emissions. Some dry low-NOx combustors can achieve 9 ppm without post-combustion control, while newer catalytic combustors are operating below 5 ppm NOx. In the late 1980s, gas turbine original equipment manufacturers (OEMs) began to integrate dry low-NOx (DLN)—also referred to as dry [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=80&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<div>
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<td style="padding-top:7px;padding-left:7px;padding-right:7px;"><span style="font-size:12pt;font-family:Times New Roman;">Best available control technology continues to be ratcheted down to achieve ever-lower NOx emissions. Some dry low-NOx combustors can achieve 9 ppm without post-combustion control, while newer catalytic combustors are operating below 5 ppm NOx.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In the late 1980s, gas turbine original equipment manufacturers (OEMs) began to integrate dry low-NOx (DLN)—also referred to as dry low-emission (DLE)—combustion technology into their product lines to eliminate the need for steam or water injection, which had been the traditional method of NOx control. Many DLN technologies were evaluated, and lean premixed combustion emerged as the most promising approach for near-term application.</span></p>
<p><span id="more-80"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Throughout the next decade, lean premixed combustors installed in new models and retrofits to existing units dramatically slashed NOx emissions compared with conventional diffusion flame technology (Figure 1). But, like so many things in nature, the benefits of NOx reduction came at a price. Because the optimum flame temperature of a lean premixed combustor is close to the lean flammability limit, combustor performance is characterized by a CO/NOx tradeoff. At the combustor design point, both CO and NOx are below target levels; however, deviations from the design flame temperature cause emissions to increase. This tradeoff becomes particularly important during part-load turbine operation, when the combustor is required to run even leaner (Figure 2, p. 24).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>1. NOx limits<br />
</strong></span></p>
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<p style="text-align:center;"><img class="aligncenter" src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec1.png?w=32&#038;h=50" alt="" width="32" height="50" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Best available control technology (BACT) NOx limits have plummeted in the past 20 years. Will 5 ppm NOx soon become the national standard?<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: U.S. Department of Energy</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">The power output of a gas turbine is directly related to the firing temperature, which is directly related to flame temperature and the rate of thermal NOx formation. The formation of NOx increases dramatically when the temperature exceeds 2,900F on natural gas. Because traditional diffusion flame combustor temperatures can exceed 4,000F for brief periods, it is virtually impossible to achieve ultra-low NOx levels when a turbine is fired with a diffusion flame combustor.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Key: Low flame temps<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Low emissions of NOx, as well as CO, can be achieved with thorough fuel-air mixing and control of the adiabatic flame temperature below about 3,000F. If, on the other hand, the peak combustion temperature can be limited to about 2,800F, NOx levels can be less than a few parts per million (ppm). Unfortunately, at fuel-air ratios low enough to achieve such low NOx concentrations, flames are highly unstable and are susceptible to flame-out or fluctuations, which can cause severe combustor vibrations and fatigue failure of combustion components.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In contrast to lean premixed combustion, an alternative technology known as &#8220;catalytic combustion&#8221; does not involve issues of flame stability. The fuel-air ratio entering the catalyst simply needs to be high enough to generate the desired turbine-inlet temperature at full conversion of the fuel.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">One of the great difficulties with lean premixed systems is maintaining flame stability in the narrow flame temperature range between high NOx production and lean flame extinction. Aerodynamically stabilized injectors have very narrow ranges of operation, necessitating multiple burner staging (up to four stages in some systems) or piloting. Many turbine manufacturers have refined their DLN systems to sub-25 ppm NOx levels, and some Frame units have achieved single-digit, or sub-10 ppm, NOx levels.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Whereas the U.S. spends millions for increased capital and maintenance costs for the latest DLN technology and postcombustion cleanup equipment to reach ever-lower NOx limits at virtually all powerplants, the European Union has taken a different approach: The EU sets NOx limits based on plant efficiency. For example, the NOx requirement for simple-cycle units with an efficiency greater than 35% is approximately 24 ppm on natural gas and 58 ppm on liquid fuels. Gaseous fuels other than natural gas have a limit of 58 ppm.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">NOx limits are less stringent for gas turbines used in combined heat and power systems demonstrating an overall efficiency greater than 75% and for combined-cycle plants demonstrating an annual average electrical efficiency greater than 55%.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Solar does DLE<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The first two prototype production DLE systems manufactured by Solar Turbines Inc (San Diego, Calif.) were installed in 1992 for field evaluation. These were a Centaur 50S gas turbine, rated 4.1 MW, at El Paso Natural Gas Co&#8217;s Window Rock Station near Window Rock, Ariz., and a Mars 100S gas turbine, rated 10.5 MW, at the Pacific Gas Transmission station near Rosalia, Wash. Initially, high combustion pressure oscillations limited operation to 42 ppm NOx. The oscillations were controlled in the short term by raising pilot fuel flow, but this increased NOx and CO. The pilot fuel injector circuit is used mainly for light-off and low-load operation. During light-off and low-load operation, approximately 30% to 50% of the fuel passes through the pilot injector, providing a rich fuel-air mixture and improved combustion stability. Above 50% load, the pilot fuel is reduced to less than 5% of the total fuel flow to optimize emissions performance (Figure 3, p. 26).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>2. Emissions compromises<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec2.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Combustor design is a series of compromises between robust operation at all loads versus lower NOx and CO. Lean combustion also increases combustion noise–caused fatigue failure of combustion components in early DLN systems.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: Platts</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>3. Dry low-emission (DLE) fuel injectors<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec3.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">DLE fuel injectors are significantly larger than conventional ones due to the higher airflow through the injector air swirler and the required volume of the premixing chamber. The injector module includes a premixing main fuel injector and a pilot fuel injector.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Solar Turbines Inc</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Design of Solar&#8217;s fuel injector premixing section was optimized by the mid-1990s. This reduced combustor pressure oscillations and, when combined with injector design improvements, enabled emissions warranties of 25 ppm NOx on natural gas and 96 ppm NOx on liquid fuels. This guarantee was extended to all of Solar&#8217;s models.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In 2001, an augmented backside-cooled combustor liner was incorporated into the OEM&#8217;s Centaur 50S and Taurus 60S models, allowing a further emissions reduction to 15 ppm NOx and 25 ppm CO from 50 to 100% load, following more than 22,000 hrs of field testing.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The most significant difference in Solar Turbines&#8217; new lean premixed combustor liner is the increased combustor volume required for low CO and unburned hydrocarbon (UHC) emissions at the lower overall flame temperature. Because combustor length was constrained by field retrofit opportunities, the only option was to increase the diameter of the combustor liner. A second difference is the absence of large air injection ports in the combustor primary zone. All air used in the combustion process is introduced through the air swirler of the fuel injectors (Figure 4, p. 26).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>4. Larger-diameter combustor liners<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec4.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The increased volume of the DLE combustor required the diameter to increase while holding the length constant so existing engines could be retrofitted. High- time DLE combustor liners have more than 39,000 operating hours.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Solar Turbines Inc</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">The new DLE combustor incorporates the capability to regulate the combustor airflow and pilot fuel flow over the entire engine-operating map. The requirement to control these two parameters has added a degree of complexity to the control system that is not required in a conventional gas turbine. During start-up and low-load operation, the pilot flow rate has been optimized to achieve maximum flame stability to handle load transients. Below 50% load the combustor airflow is managed in the same way as in a conventional engine. Above 50% rated load, Solar&#8217;s DLE engine enters the &#8220;low emissions mode,&#8221; modulating either the bleed valves or inlet guide vanes to keep the combustion primary zone temperature within a specified range. Solar&#8217;s DLE gas turbine controls use the power turbine inlet temperature as an indirect measurement of the primary zone temperature to control the bleed valve or inlet guide vane position as a function of turbine load (Figure 5).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>5. SoLoNOx system<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec5.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">A Centaur 50 gas turbine with a dual-fuel SoLoNOx system supplies power and heat to a district energy system in Germany.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Solar Turbines Inc</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Local ambient conditions also affect emissions. NOx is observed to increase with increasing ambient temperature, decreasing relative humidity, and increasing barometric pressure, whereas CO emissions trend in the opposite way. However, field experience has shown that relative humidity and barometric pressure have only a small effect on the combustor primary zone temperature and, therefore, a small influence on emissions from DLE gas turbines. In practice, emissions from DLE packages vary less than 5 ppm from 0F to 120F. Many DLE packages are configured to increase pilot fuel flow at temperatures below 68F to augment flame stability. Below 0F, NOx and CO emissions increase.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Further reductions<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Future emissions reductions mean developing new technologies to take up where DLE leaves off. One area being explored by Solar Turbines is a surface-stabilized fuel injector for use with lean, premixed combustors. Developed by Alzeta Corp (Santa Clara, Calif.), surface-stabilized fuel injectors provide extended turndown and ultra-low NOx emission performance.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The new injectors form interacting radiant and blue-flame zones immediately above a selectively perforated porous metal surface. This allows stable operation at low reaction temperatures. A proof-of-concept injector in a full-pressure test rig at the U.S. DOE&#8217;s National Energy Technology Laboratory in Morgantown, W.Va., achieved sub-3 ppm NOx emissions with concurrent single-digit CO emissions. Operating conditions ranged between inlet pressures of 26.5 psia and 180 psia, inlet temperatures between 186F and 850F, and calculated adiabatic flame temperatures between 2,670F and 2,900F. Testing with prototype fuel injectors in test rigs at Solar Turbines yielded similar results. In May 2001, the OEM&#8217;s 1-MW Saturn gas turbine was operated to 95% load with a surface-stabilized injector. Currently, Alzeta and Solar Turbines are completing a multi-burner annular combustor test, which will then proceed to an engine test later this year. In addition, the companies have initiated a project to apply Alzeta&#8217;s nanoSTAR technology to the Titan 130 gas turbine.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Mitsubishi hits 15<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Mitsubishi Power Systems Inc&#8217;s (Lake Mary, Fla.) first DLN combustor was introduced in 1984 on a 50-Hz M701D gas turbine. By 1992, 25-ppm NOx levels were being commercially achieved in the OEM&#8217;s F-class turbine operating at full load, with a turbine inlet temperature of 2,460F.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Mitsubishi&#8217;s F-class fleet experience with DLN combustors now exceeds 1.5 million hours of meeting the 25 ppm NOx limit. The OEM reports that recent tests have achieved 15 ppm NOx.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The pilot nozzle and air bypass valve in this combustor make it possible to sustain a stable flame and accurately control the fuel-air ratio. The main nozzles are composed of air swirlers together with a fuel nozzle. The swirlers introduce highly turbulent air, causing complete mixing of gas and air, while the pilot nozzle allows stable combustion of the premixed gas by diffusion firing. A cone attached at the tip makes flame holding stable by recirculating combustion gases. The air bypass valve, infusing air directly into the transition piece, is installed at the transition piece, enabling an almost constant fuel-air ratio at various operating conditions, such as ignition, acceleration, and partial-load operation (Figure 6).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>6. Contrasting cooling schemes<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec6.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The cooling scheme in Mitsubishi&#8217;s F-class turbine uses proprietary &#8220;Platfin&#8221; cooling of the combustor basket, and &#8220;Mtfin&#8221; is used at transition piece. Around 10% of available air is used for cooling, and the rest is used for combustion. The G-class combustor uses steam for cooling (bottom).<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Mitsubishi Power Systems Inc</span></p>
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</div>
<p><span style="font-size:12pt;font-family:Times New Roman;">In 1996, a steam-cooled DLN combustor was developed for Mitsubishi&#8217;s G-class gas turbines. The M501G and M701G models feature a turbine inlet temperature of 2,730F and are designed to achieve a combined-cycle plant efficiency of greater than 58%. Prototype testing has shown the G series to be capable of 25 ppm NOx.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">To increase the turbine inlet temperature to 2,730F, almost all of the compressed air is needed for combustion, and steam is introduced to perform the cooling. (In conventional gas turbines, much of the compressed air is diverted to cool hot-gas-path components.) Overall, Mitsubishi&#8217;s G-class combustor has nearly the same configuration as its F class, except at the combustor basket, where the transition piece integrates the basket part and the liner. The cooling steam, supplied from a required bottoming steam cycle, cools that structure over the entire surface area of the combustor.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The M701G1 combustion chamber and first- and second-stage blades and vanes are similar to those used in the prototype 501G design, but the size has been increased to give a higher output. The 701G1 is a single-shaft machine with the generator at the compressor end of the turbine to allow the turbine exhaust to be directed into the heat-recovery steam generator. The turbine combustion chamber uses steam cooling to maintain temperature in the range 2,730F to 2,910F to keep NOx emissions at 25 ppm or less. Mitsubishi&#8217;s G-class fleet experience exceeds 75,000 hours on seven units.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Aero engines<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">GE Power Systems&#8217; (Atlanta, Ga.) DLE combustors have been developed for GE&#8217;s aeroderivative gas turbines—the gas-fueled 44-MW LM6000, the 23-MW LM2500, and the double annular 15-MW LM1600. Twenty-five ppm has been successfully demonstrated for the entire family of LM DLE products.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Factory testing of components and engine assembly on the first 41-MW DLE LM6000 gas turbine was completed in 1994 and demonstrated less than 15 ppm NOx, 10 ppm CO, and 2 ppm UHC at a firing temperature of 2,350F. In 1995, the 43-MW Ghent power station in Belgium became the first commercial operator to use the LM6000 fitted with the DLE combustor system, demonstrating 16 ppm NOx, 6 ppm CO, and 1 ppm UHC. The high-time LM6000 engine has accumulated more than 34,000 hours. As of the end of 2002, GE had more than 200 DLE LM engines in operation with almost 3.5 million operating hours.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The LM6000 DLE combustor employs a triple-dome design with staging of fuel and air flow to achieve lean premixed operation from light-off to full power—using the mid-dome at light-off, with the inner and outer domes brought on progressively as the engine is loaded. The middle and outer domes each consist of 30 premixers; the inner dome has 15. The domes of the combustor are protected from the hot combustion gases by segmented heat shields.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The middle and the inner dome premixers are identical, but the outer premixers are somewhat larger to manage the dome reference velocities in the three combustor domes within a narrow band. Spent cooling air from the heat shield is directed away from the flame-stabilization zones, permitting the combustor to operate at leaner fuel-air ratios. Turbine-nozzle cooling air is utilized to cool the liners convectively on the backside. Combustion acoustics are controlled by the use of passive devices on the exterior of the engine, fuel staging within premixers, and by the use of a control system that senses and alters the combustor operation to limit combustion-generated noise. A small amount of fuel (about 10% of the middle dome flow) is injected into the combustor from holes in the walls of the mixing duct. Another feature, Enhancing Lean Blow Out holes, increase the local fuel-air ratio in the mixing region between recirculating burned gases and fresh, incoming mixture and also provide axial staging of the fuel. The increased fuel-air ratio in the mixing region, along with axial staging, helps to decouple any fuel injection–related acoustic coupling mechanisms (Figure 7).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>7. Individual fuel controls<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec7.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The LM6000PD has individual fuel controls for each of the combustion system&#8217;s three domes.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: GE Power Systems</span></p>
</td>
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</tbody>
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</div>
<p><span style="font-size:12pt;font-family:Times New Roman;">The NOx emissions stay low as the combustor operates lean premixed over the entire operating envelope. CO emissions are less than 25 ppm levels at 50% power on up. UHC emissions are typically less than 10 ppm everywhere except during start-up. Higher emissions are encountered transiently during staging when additional domes are either being lit or extinguished.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The LM1600, LM2500, and the LM6000 are two-shaft engines. Unlike in single-shaft engines, the compressor discharge temperatures and pressures increase as the load increases. Higher combustor inlet air temperatures result in a decrease in flame quenching and thus the lean blowout limit moves to leaner fuel-air ratios and lower flame temperatures. The combustor can operate with lower flame temperatures as the load is increased. NOx emissions decrease slightly as the load on the engine is increased in the region where the flame temperatures are held constant with airflow control. Once the load increases past the point of airflow control, additional power is produced by simply increasing the flame temperature.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">CO emissions are strongly dependent on the quenching of the CO oxidation process in the neighborhood of the combustor liners. Leakage air from the heat shields also contributes to the early quenching of the CO oxidation reactions. In order to reduce quenching of the CO oxidation reactions in the forward regions of the primary combustion zone, cooling air and leakage airflows in this region have been kept at minimum by the use of advanced cooling technology and materials.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Single-digit NOx<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The only utility-scale gas turbine currently marketed with single-digit NOx guarantees is GE Power Systems&#8217; Frame 7FA outfitted with DLN-2.6. The first of these units was placed in service in March 1996 by Public Service Co of Colorado. The newer model reduced NOx levels from the OEM&#8217;s previous 25-ppm guarantee on the DLN-2 combustor down to 9 ppm. This required 6% more air to pass through the premixers in the combustor due to reductions in cap- and liner-cooling airflows and increased cooling effectiveness.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">However, without changes in the operation of the DLN-2 system, certain penalties would have been incurred for achieving 9 ppm baseload performance. The turndown of a DLN-2 combustor tuned to 9/9 operation (9 ppm NOx/9 ppm CO) was estimated to be about 70% load, compared with 40% load for the 25/15 system. A new combustor configuration was developed based on the DLN-2 burner because of its excellent flame-stabilization characteristics and operating experience. The key feature of the newer configuration is the addition of a sixth burner located in the center of the five existing DLN-2 burners. The presence of the center nozzle enables the DLN-2.6 to extend its 9/9 turndown well beyond the five-nozzle DLN-2.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">By fueling the center nozzle separately from the outer nozzles, the fuel-air ratio can be modulated relative to the outer nozzles leading to approximately 200F of turndown from baseload with 9 ppm NOx. Burners were turned and a fourth premixed manifold for injecting quaternary fuel was added to reduce combustion dynamics. The first three premixed manifolds, designated PM1, PM2, and PM3, are configured such that any number of burners can be operated at any time. The PM1 manifold fuels the center nozzle, the PM2 manifold fuels the two outer nozzles located at the cross-fire tubes, and the PM3 manifold fuels the remaining three outer nozzles. The five outer nozzles are identical to those used for the DLN-2, while the center nozzle is similar but with simplified geometry to fit within the available space. Emissions performance of the DLN-2.6 is 9 ppm NOx and CO over a 50% load range.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">GE recently announced a series of power and efficiency uprates, as well as NOx reductions, to its Frame units. This includes the PG6111FA (the uprated version of the Frame 6FA), which generates 75.9 MW with 15 ppm NOx at a firing temperature of 2,420F. The Frame 6FA machines are manufactured in GE&#8217;s facility in Belfort, France, and are scheduled to start shipping in the second quarter of 2003.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">GE also introduced the Frame 9FB, a 50-Hz version of the 7FB, which was introduced in 1999. The first 7FB was installed at a Reliant Energy project in Hunterstown, Pa., where it is being tested and is scheduled to enter commercial service in 2003. The Frame 9FB benefits from what GE calls an &#8220;advanced technology flowback&#8221; from the company&#8217;s planned steam-cooled H-class gas turbine. The 9FB will be equipped with GE&#8217;s advanced DLN-2+ combustion system, and NOx emissions will be less than 25 ppm. The Frame 9FB will be available for shipment in early 2004.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Catalytica cleans up<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">A technology called catalytic combustion promises to be an alternative to DLN technologies, with even lower NOx levels—below 5 ppm. Catalytica Energy Systems Inc (Mountain View, Calif.) took an early lead in this field in 2000, when it installed its Xonon system on a 1.4-MW Kawasaki gas turbine at Silicon Valley Power&#8217;s (Santa Clara, Calif.) Gianera station. Catalytica recognized that it&#8217;s tough to break into the gas-turbine business with a potentially revolutionary new product, especially when the product lies directly in the gas path. &#8220;Show me an operating turbine and then we&#8217;ll talk,&#8221; was the message.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">So the company went it alone by purchasing a used M1A Kawasaki engine, refurbishing it, and retrofitting its new combustion system designed from scratch. Catalytica did this before Kawasaki Motors Corp USA (Grand Rapids, Mich.) decided to come on board, license the technology, and develop what is now the commercial product. After 14,000 grid-connected hours and a yearlong 8,128-hr testing program, the Silicon Valley Power plant performed better than design. According to Catalytica, the results were:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">NOx emissions of 1.3 ppm (goal was less than 3 ppm)<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">CO emissions of 0.9 ppm (goal was less than 5 ppm)<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">UHC emissions of 1.3 ppm (goal was less than 5 ppm)<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Reliability of 99.2% (goal was 98%)<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Availability of 91.2% (goal was 96%)<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Kawasaki Heavy Industries Limited (Hyogo, Japan) produces the 1.4-MW M1A-13A gas turbine (referred to as the M1A-13X when Xonon is installed). The model has an unimpressive thermal efficiency of just 25.5%—equating to a 13,400 Btu/kWh heat rate. But it is convenient for a Xonon retrofit because it has a readily accessible, single, external can-type combustor. The M1A-13A has a pressure ratio of approximately 9.3 to 1, which is comparable to that found in many other industrial gas turbines in the 1- to 6-MW range. Also, the model&#8217;s low mass flowrate (18 lb/sec) allows the catalytic combustor to be maintained as a small system typical of large rig test units, thus reducing the cost of the total system. Finally, its low firing temperature of 1,839F makes the engine ideal for catalytic combustion, because the modest temperatures in the gas-phase burnout zone allow the use of existing liner-cooling technologies.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In the Xonon combustion system, compressor discharge air enters an annular plenum prior to entering the preburner. The preburner is a small DLN-type combustor that preheats the combustor air up to the catalyst operating temperature. Fuel is then injected into the warm air and thoroughly mixed before entering the catalyst module. In the catalyst module, some of the fuel-air mixture is combusted through a flameless catalytic process. The combustion process continues in the burnout zone until all of the remaining uncombusted fuel is reacted (Figure 8).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>8. Catalytic combustor<br />
</strong></span></p>
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec8.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Catalytic combustors burn lean fuel-air mixtures to achieve sub-5 ppm NOx. The maximum combustor exit temperature is 2,460F or lower—well below the NOx-formation temperature.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Catalytica Energy Systems Inc</span></p>
</td>
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<p><span style="font-size:12pt;font-family:Times New Roman;">According to Catalytica, its technology is superior if your target is 5 ppm NOx or less, meaning the life-cycle cost of a Xonon-equipped gas turbine is less than that for the same gas turbine equipped with a selective catalytic reduction system. The manufacturer points out that spent Xonon catalysts, which are expected to be depleted annually, are nontoxic and can be recycled to recover precious metals.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The OEM successfully completed an Equipment and Process Precertification Program administered by the California Air Resources Board (CARB), which verified the air quality–related performance claims of its Xonon Cool Combustion system last August. The Equipment and Process Precertification Program is a voluntary statewide program administered by CARB through which manufacturers of products that have a beneficial impact on air quality can have their product&#8217;s performance claims independently verified. The objective of the program is to simplify the permitting process by providing advanced independent evaluation of a technology, which can then be used as the basis for BACT (best available control technology) determination.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Last year, Xonon shipped catalysts for what was scheduled to be the first three commercial Xonon-equipped Kawasaki gas turbines for a government healthcare facility in Jamaica Plain, Mass. However, the plant was being developed by an Enron subsidiary, and the project was shelved after the turbines were shipped. After the three turbines had sat idle for over a year, Kawasaki repurchased them at an auction of Enron assets.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The first commercial application of Catalytica&#8217;s Xonon technology now is the Sonoma Developmental Center in Eldridge, Calif., where an existing Kawasaki M1A-13D gas turbine was retrofitted with a Kawasaki-designed Xonon-based combustor (Figure 9). The 12-yr-old unit provides supplemental heat and power for a staff of 2,200 and 850 residents across 120 buildings.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>9. First commercial catalytic combustor installation<br />
</strong></span></p>
<div>
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<td style="border-top:none;border-left:none;border-right:none;padding:1px;" valign="middle">
<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062408-0711-gasturbinec9.png?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The Sonoma Developmental Center is the first commercial catalytic combustor installation. A 12-yr-old Kawasaki gas turbine was retrofit with a Catalytica-licensed catalyst. Post-startup testing confirms that the 1.3-MW plant is operating at less than 3 ppmv NOx, less than 10 ppm CO, and less than 2 ppm VOC.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Catalytica Energy Systems Inc</span></p>
</td>
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</tbody>
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<p><span style="font-size:12pt;font-family:Times New Roman;">The six-week retrofit involved removing the current M1A-13D engine operating with a DLE combustor configuration, and replacing it with an advanced M1A-13X engine incorporating Xonon Cool Combustion. The reconfigured unit returned to service in November 2002. Post-startup testing confirms the 1.3-MW plant is operating at less than 3 ppm NOx—an overall 90% reduction. Additionally, the Xonon Cool Combustion system makes it possible for Kawasaki to guarantee CO levels of less than 10 ppm and VOC levels of less than 2 ppm.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Catalytica announced in December the purchase of a Kawasaki 1.4-MW GPB15X equipped with Xonon technology. The unit is part of a heating and cooling plant for the Reader&#8217;s Digest 650,000-square-foot global headquarters in Pleasantville, N.Y., servicing approximately 1,000 employees. The plant is expected to be in service by this July.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Catalytica reports that it also has demonstrated sub-5 ppm NOx levels on gas turbines manufactured by Rolls-Royce Allison (Indianapolis, Ind.). GE Power Systems plans to begin shipment of a Xonon-equipped 11-MW GE10 gas turbine in 2004. String testing is scheduled in Florence, Italy, this year with orders beginning this fall. Emissions targets for the GE10 are 3 ppm NOx, 100 ppm CO, and 10 ppm VOC.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">By Dr. Robert Peltier PE, Sr. Editor</span></td>
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</table>
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		<title>Designing and modifying HRSGs for cycling operation</title>
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		<comments>http://powergen.wordpress.com/2008/06/24/designing-and-modifying-hrsgs-for-cycling-operation/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:04:42 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Combined Cycle]]></category>
		<category><![CDATA[Gas Turbine]]></category>
		<category><![CDATA[Power Plant]]></category>
		<category><![CDATA[Steam Turbine]]></category>

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		<description><![CDATA[Designing and operating HRSGs for cycling duty requires close cooperation between the manufacturer and the user. Once HRSGs are in service, a monitoring system should provide a thorough picture of the mechanisms affecting the life and integrity of the boiler. Today&#8217;s heat-recovery steam generators (HRSGs), a vital component in the popular combined-cycle plant, are exposed [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=70&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span style="font-size:12pt;font-family:Times New Roman;">Designing and operating HRSGs for cycling duty requires close cooperation between the manufacturer and the user. Once HRSGs are in service, a monitoring system should provide a thorough picture of the mechanisms affecting the life and integrity of the boiler.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Today&#8217;s heat-recovery steam generators (HRSGs), a vital component in the popular combined-cycle plant, are exposed to more severe duty than merely running at baseload. Deregulation has spurred the development of merchant plants, which are required to start up, load follow, and shut down with minimal notice in response to market conditions. Unless properly designed and operated to withstand this cycling duty, the integrity of the HRSG will be compromised.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Industry professionals need to understand the various damage mechanisms that can result, as well as how to control them. For new projects, damage control begins with the specification of certain design features. Operation and maintenance practices also play an essential role in managing HRSG life, both for new and existing plants. Existing plants also should explore modifications and monitoring programs that can boost the reliability and extend the service life of HRSGs in cycling duty.</span></p>
<p><span id="more-70"></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Many components<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Existing HRSGs that are already in service pose another problem. Most of these were designed for baseload operation but now are being cycled. Users should explore the HRSG modifications that are discussed below to determine the applicability to their specific plants. At a minimum, users of existing HRSGs should implement a monitoring program, outlined here, to gauge the effects of cycling.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">A typical combined-cycle HRSG produces &#8220;main steam,&#8221; at three pressure levels, plus &#8220;reheat steam.&#8221; Supplemental firing through a duct burner often is installed, as well, to increase steam-production capacity. Most combined-cycle plants also have a feedwater heater to increase the heat recovery and reduce the deaerating load of the integral deaerator.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The heat-transfer sections of the HRSG are located in series along the exhaust-gas path to optimize heat recovery. It is not uncommon to have 15 to 20 different heat-transfer sections—superheaters, reheaters, evaporators, and economizers—at various locations along the gas path. Emissions-control regulations often require the addition of a selective catalytic reduction system (SCR) for NOx control and, in some cases, a separate catalytic converter for CO control. Some HRSGs also are equipped with an exhaust-gas bypass damper to enable simple-cycle gas-turbine operation, though these dampers have not found wide usage in the U.S.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Many mechanisms<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">All of these components are exposed to different temperatures and pressures at different times while the HRSG is started, operated, and shut down. How well the components react to the transients and steady-state conditions determines the integrity of the entire HRSG. The basic mechanisms affecting the life of an HRSG are:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Low-cycle fatigue (LCF). Damage occurs at a low number of stress cycles when the strain is high. LCF is the most dominant damage mechanism in today&#8217;s HRSGs.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Creep. Damage is caused by the material being at high temperature and stress for a considerable period of time.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Thermal shock. The impingement of cold water or steam on hot surfaces can damage the base material.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Oxidation. Oxidation and exfoliation can occur due to exposure to high temperatures.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Differential expansion. If adjacent tubes or pipes are at different temperatures, the resulting uneven expansion or contraction can stress both components. Piping supports also play a part in this.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Corrosion fatigue. A crack is initiated because of corrosion, and progressive damage occurs because of fatigue and corrosion. This typically occurs at a temperature range of 300F to 500F.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Corrosion in tubes. Improper water chemistry is the cause.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Flow-accelerated corrosion (FAC). The combination of high flow and poor chemistry control can cause FAC in specific HRSG locations.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Corrosion-product migration. The migration of corrosion products to other HRSG components may cause further corrosion or other damage.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Deposits. Temperature or water-chemistry fluctuations may result in deposits on heat-transfer surfaces.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Erosion. Transient high velocities may initiate or perpetuate erosion.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">All components in an HRSG can be affected by these damage mechanisms (see Table). However, some components are more vulnerable because of their location, construction, or exposure. These critical components need to be designed and monitored more closely for potential failures. The critical components typically are:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Superheater and reheater outlets.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Tube-to-header joints in hot sections.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Drum-to-downcomer nozzles in the high-pressure drum.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Bent portions of heat-transfer tubes.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Attemperators.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Bypass valves.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">To a plant operator, &#8220;cycling&#8221; refers to the quick start-up, load following, and shutdown of generating units. But to a materials engineer, cycling is the reversal of stresses in a component. Stress cycling can happen by the imposition and relaxation of loads or because of a reversal of temperatures. When a component is exposed to rapidly changing temperatures, all parts of the component may not heat up or cool down uniformly. The subsequent differential expansion creates high stresses and stress reversals.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The main causes of stress cycling are a change of plant load and emergencies. Plant load changes include short-notice start-ups, gas-turbine load changes, part-load operations, and varying duct-burner firing.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The way a boiler is shut down and laid up also can cause cycling. In an emergency—such as a steam-turbine trip—the boiler has to shut down very rapidly, causing undue, or reversing, stresses. Sometimes a boiler is force-cooled to make repairs during a short outage window. This force cooling can create temperature differentials. And the failure or abnormal operation of other plant equipment—such as pumps and valves—also can impose stress-cycling conditions on the HRSG.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Cycling relates to mechanisms<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Most of the time, cycling either creates or exacerbates the effect of damage mechanisms on HRSG components. Creep damage, by definition, is caused by a prolonged exposure to high temperature and stress. Though creep is not caused by cycling, it is exacerbated by it. Fatigue and fatigue damage are the most prevalent mechanisms affecting the boiler life, and they are a direct consequence of cycling.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Water-chemistry upsets that result in corrosion may be due to cycling or to a failure of water-chemistry controls. For example, for a rapidly starting HRSG, the superheater is exposed to high temperature on the outside of the tubes and headers, while the inside surfaces of tubes and headers may still be cool. This creates high thermal stress. Some specific examples of how cycling creates or exacerbates the damage mechanisms in critical components are discussed below.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Superheaters and reheaters:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Fatigue. The impingement of hot gasses on cold surfaces at start-up or of cold gasses on hot surfaces at shutdown creates thermal gradients. Similarly, the condensed steam in the tubes after shutdown impinge on hot surfaces if the condensate remains in the tubes. The high-pressure components are more vulnerable to fatigue effects due to their increased wall thicknesses.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Thermal shock. Condensate in a superheater section or colder reheat steam in the hotter and dry reheater section would result in thermal shock to the inner surfaces of the tubes and headers.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Creep. Only high-temperature components are prone to creep damage. High-temperature transients and continuous high-temperature operation may increase the creep rate. However, if the creep is coupled with fatigue due to cycling, the damage will be much higher than what can occur if the same fatigue or creep is working alone.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Oxidation. Exposure of the metal to higher temperature than what it was designed for, particularly during start-ups, can result in oxidation. Oxidation and exfoliation can happen both inside and outside the tubes and piping, caused by exhaust gas on one side or steam/water on the other. Dry reheater designs are particularly vulnerable.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Differential expansion. Uneven heating of tubes—caused by uneven distribution of (1) exhaust-gas or steam/water flows or (2) exhaust-gas temperatures—can cause adjacent tubes to expand or contract differently. Both compressive and tensile loads are imposed.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Deposits. Uneven or excessively fast ramp rates may result in the accumulation of condensate in the superheaters and, consequently, the formation of deposits.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Evaporators:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Low-cycle fatigue. This often occurs in natural-circulation evaporators during start-up, because circulation has not been fully established.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Differential expansion. Just as with superheaters and reheaters, the uneven heating of evaporator tubes—caused by uneven distribution of (1) exhaust-gas or steam/water flows or (2) exhaust-gas temperatures—can cause adjacent tubes to expand or contract differently. Both compressive and tensile loads are imposed.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Deposits. Uneven heating or heat-flux anomalies may result in local dry-outs and deposition of salts in evaporator tubes. These deposits further distort the flow and heat-flux distribution, so the problem can snowball.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Flow-accelerated corrosion. Two-phase flows in evaporator sections result in FAC, particularly in the low-pressure sections.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Corrosion-product migration. Corrosion products formed at one location may migrate to another, and, under the right conditions, may form deposits there. These deposits then result in uneven heat fluxes.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Erosion. Solids in the water, and water in two-phase flow systems, can cause erosion at higher velocities.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Economizers and feedwater heaters:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Low-cycle fatigue. The impingement of cold water on hot surfaces, particularly during a quick shutdown and restart, sets up LCF.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Differential expansion. Uneven heating of tubes due to flow- or temperature-distribution problems can cause adjacent tubes to expand differently. Both compressive and tensile loads are imposed.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Deposits. Uneven or excessively fast ramp rates can result in solids precipitation and deposition, causing uneven heating.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Flow-accelerated corrosion. Single-phase FAC in economizers is being recognized as one cause of failures. Often it occurs because, during startups and at transition time, the water chemistry may be out of control.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Corrosion fatigue. Chemical imbalances can create corrosion, and cyclic loading can exacerbate the effect due to fatigue.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Erosion. Solids in the water can cause erosion at higher velocities.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Design needs dynamic analysis<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In the design phase, the most important requirement is to make sure that all the factors affecting the life of the HRSG have been accounted for. This means that either the design features must be modified to mitigate the effect of the damaging factor, or the damaging factor must be eliminated. The most common way to ensure this is to do a life-cycle analysis, which typically consists of the following steps:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Define the basic operating conditions.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Establish the lifetime operating details.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Determine the most critical components.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Conduct a dynamic-response analysis of the critical components. This is perhaps the most critical factor in the life-cycle analysis. There are various software programs available that indicate the dynamic behavior of a component. However, these programs need to be custom-fitted to a given HRSG. To do this, the model has to be very well-defined. In addition, the expected operating conditions—such as pressure and temperature ramps that cause changes in the components—need to be defined thoroughly. Most of the life-cycle analyses currently on the commercial market do not give good results because of conservatism employed in the model. This often happens because the details of the component or the operating conditions are not worked out completely, and the model is not refined.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Calculate the cumulative damage factor (CDF). Various methods of calculating the CDF are available, including methods suggested by ASME, Germany&#8217;s TRD, and British Standards. It is important to use a consistent method rather than indiscriminately mixing various methods with different assumptions and data used in deriving the formulas.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Revise design or operating conditions if the CDF is higher than allowable.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Design features<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Some of the specific design features that help in minimizing or monitoring the damage due to cycling are listed below. It is possible to design an HRSG without these features and still maintain the integrity of the boiler over the intended life of the unit. The key is to do a life-cycle analysis. If the life-cycle requirements are met with only some of these features, then the design should still be acceptable. Features that improve the cycling ability include these:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Smaller-diameter tubes, headers, and steam drums<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Automated vents and drains<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">High-pressure superheater bypass to reheater<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Wet reheaters<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">On-line water-chemistry monitors<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Stack dampers<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Leak-proof valves<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Metal thermocouples<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Minimization of piping and tube bends<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Flexible connections<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Motorized blowdowns<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Economizer recirculation<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">No cascading blowdowns<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">External &#8220;kettle&#8221; boilers<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Ability to clean<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Spray coatings<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Higher-grade metal alloys<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Bypass dampers<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Multiple attemperators<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Good steam-/water-side flow distribution at all loads.<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Operating practices<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">How the boiler is started up is a key factor affecting HRSG life. Rapid starting exacerbates fatigue, so it should be minimized, if it can&#8217;t be avoided altogether. The manufacturer-supplied start-up procedure may have some contingency built in, which can be analyzed and possibly removed. However, this is possible only if all the operating conditions, including the condition of the HRSG when starting and at shutdown, are well-defined.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">After a &#8220;soak&#8221; period, which allows temperature differentials to be minimized, an HRSG can be ramped up or ramped down quickly. Ramping a running boiler is much faster than starting a new boiler. So it is advisable to ramp up the running unit and ramp down as the cold unit comes on-line.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Similar to ramping, load changes should be done gradually to minimize cycling effects. Often, HRSG manufacturers suggest making load changes in incremental steps rather than continuously. For example, instead of a continuous 10% change, the load may be changed in five 2% load changes with a dwell (or hold period) after each change.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Shutdowns by themselves may not be a big problem, unless purge requirements for the subsequent restart cause cold air to blow into a hot HRSG. Limitations on air flow should help minimize any damage.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The chemistry upsets and oxygen intrusion that frequently occur during HRSG layup substantially affect boiler life. When the boiler is put on-line, the heat will increase the damage.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Modifying existing units<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Many of the HRSGs in service today were designed for baseload conditions but now are required to run as cycling units. Plant owners need to determine the impact that this will have on reliability and life expectancy. To do so, an engineering firm—preferably an HRSG manufacturer—should be retained to conduct a condition-assessment study, suggest equipment modifications that can extend service life, and implement a monitoring program to track damage mechanisms.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The condition assessment includes:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Identification of critical components and determination of their condition<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Checking of instrumentation and controls<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Review of operational history<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Establishment of a baseline benchmark<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Equipment modifications can be suggested after the proposed operations are defined by the owner and a complete life-cycle analysis of the critical components is performed. Sometimes a modification is feasible and cost-effective, but it may not be permitted because of code requirements.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">A monitoring program should be implemented to track such variables as:<br />
</span></p>
<ul>
<li><span style="font-size:12pt;font-family:Times New Roman;">Temperatures, gas, water, and steam<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Drum levels<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Attemperator flows<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Steam and water flows and velocities<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Water chemistry<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Steam purity and constituents<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Gas-turbine and burner fuel<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">Exhaust-gas conditions<br />
</span></li>
</ul>
<p><span style="font-size:12pt;font-family:Times New Roman;">Data from the monitoring program should be reviewed and checked against the assumptions used in the equipment modifications. If there are any changes between the actual and initially specified operating conditions, these are noted and their effect on the life expectancy is assessed. Based on this assessment, some further adjustments may be necessary.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">After at least a year of operation following equipment modifications, a condition assessment should be performed again, including measurement of wall thicknesses and concentrations of corrosion products and deposits. The assessment should include both destructive and nondestructive testing of suspect components, and all data should be checked against the baseline benchmark. Based on this assessment, additional equipment modifications or changes to operating conditions may be suggested.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Keep talkin&#8217;<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">For long service life of HRSGs, it is essential to have long-term cooperation and open exchange of information between the operators and the designers (see box). Both new and existing HRSGs can meet the rigors of cycling duty with the right design features, modifications to equipment, and adjustments in operating practices.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">By Akber Pasha and Robert Allen, Vogt-NEM Inc</span></p>
<p><span style="font-size:10pt;font-family:Times New Roman;">Edited by R.C. Swanekamp, PE<br />
</span></p>
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		<title>Germany fires up latest supercritical plant</title>
		<link>http://powergen.wordpress.com/2008/06/24/germany-fires-up-latest-supercritical-plant/</link>
		<comments>http://powergen.wordpress.com/2008/06/24/germany-fires-up-latest-supercritical-plant/#comments</comments>
		<pubDate>Tue, 24 Jun 2008 07:02:28 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Uncategorized]]></category>

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		<description><![CDATA[The new Niederaussem-K 1,050-MW power station—one of the world&#8217;s largest and most advanced coal-fired units—was officially put into operation late last year. Niederaussem is a supercritical, lignite-fired powerplant complex west of Cologne, Germany (Figure 2). The first oftwo 150-MW units started up in 1962 and was followed byfour 300-MW units and two 600-MW units.Chancellor Gerhard [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=69&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
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<td style="padding-top:19px;padding-left:19px;padding-right:19px;"><span style="font-size:12pt;font-family:Times New Roman;">The new Niederaussem-K 1,050-MW power station—one of the world&#8217;s largest and most advanced coal-fired units—was officially put into operation late last year. Niederaussem is a supercritical, lignite-fired powerplant complex west of Cologne, Germany (Figure 2). The first oftwo 150-MW units started up in 1962 and was followed byfour 300-MW units and two 600-MW units.Chancellor Gerhard Schroeder was present at the commissioning and emphasized the role of local-sourced brown coal as a stabilizing factor in the energy mix for Germany.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>2. Niederaussem, Cologne, Germany<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The 1,050-MW Niederaussem Unit K is one of the most advanced coal-fired units in Europe. The lignite-fired, supercritical plant was officially put into operation late last year. Unit K is under construction on the far right.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: RWE Rheinbraun AG</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">The Niederaussem Unit K is a supercritical boiler with a boiler efficiency of almost 95% (LHV) with steam pressure of approximately 3,988 psig and steam temperatures of 1,076F. The plant electrical efficiency is over 43% (LHV). Alstom (Paris, France) was the consortium leader for the engineering, construction, and commissioning of the steam generator. The unit&#8217;s owner is RWE Rheinbraun AG (Essen, Germany).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Hammerfest, Norway, with 11,000 inhabitants, calls itself the world&#8217;s northernmost town. In December, tidal currents started turning the blades of a windmill-like turbine standing on the seabed near Kvalsund at the Arctic tip of the country. &#8220;We will be the first in the world to use tidal currents to generate electricity to be fed into the local grid,&#8221; said Harald Johansen, managing director of Hammerfest Stroem (Oslo, Norway).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Hammerfest Stroem uses proprietary water &#8220;wind mill&#8221; technology to convert the kinetic energy in a tidal current into electricity. In Kvalsund, the water flows at about 7.5 feet per second, apart from a pause at high and low tides. The 300-kW tidal stream turbine with 45- to 48-ft long blades is mounted on 200-ton towers placed on the seabed. The turbine automatically turns to face the tide when the currents change direction, and the propeller blades automatically adjust to their optimum orientation in the prevailing current (Figure 3).<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>3. Hammerfest Stroem, Norway<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Hammerfest Stroem&#8217;s underwater &#8220;wind mill&#8221; technology is being prototyped near Kvalsund at the Arctic tip of Norway. The 300-kW tidal stream turbine with 45- to 48-ft long blades, is mounted on towers placed on the seabed.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Hammerfest Strom AS</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Johansen reckons the project has cost $6.7 million so far and will cost almost $15 million to complete installation of all 20 turbines by 2004. The production cost of the electricity is estimated to be 4.3 to 5 cents/kWh, three times that of typical hydro-generated electricity in Norway. Tidal power will be added to the mix of electricity in the local grid, and consumers will be required to absorb the cost.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The biggest tidal powerplant in the world is on the La Rance River in northern France and has been in place since the 1960s. It has a 240-MW capacity, but Electricité de France has no plans to build new ones. Canada&#8217;s Bay of Fundy in Nova Scotia has the highest tides in the world, at about 39 ft. Nova Scotia Power&#8217;s 20-MW plant at Annapolis Royal, built in 1984, is the only one in North America; the company is focusing more on wind.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Experts are uncertain about the potential of tidal power, especially because of sub-sea maintenance costs. Storms have wrecked many experimental ocean-power stations.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;">The British firm Marine Current Turbines, which plans to test a similar tidal current system off Devon in southern England next year, says that maintenance could be a problem for Hammerfest. &#8220;When you have strong enough currents for tidal-energy generation, there are few slack tides when divers can work,&#8221; said Peter Fraenkel, the group&#8217;s technical director.</span></td>
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		<title>Plains End Power Plant, Arvada, Colorado</title>
		<link>http://powergen.wordpress.com/2008/06/23/plains-end-power-plant-arvada-colorado/</link>
		<comments>http://powergen.wordpress.com/2008/06/23/plains-end-power-plant-arvada-colorado/#comments</comments>
		<pubDate>Mon, 23 Jun 2008 02:14:33 +0000</pubDate>
		<dc:creator>japat30</dc:creator>
				<category><![CDATA[Diesel Engine]]></category>
		<category><![CDATA[Power Plant]]></category>
		<category><![CDATA[cooling tower]]></category>
		<category><![CDATA[gas fired]]></category>

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		<description><![CDATA[Owned by PG&#38;E National Energy Group, and operated by Wärtsilä North America Inc. Billed as the world&#8217;s largest natural gas–fired reciprocating engine generating station, the 111-MW Plains End Power Plant has successfully demonstrated that large distributed generation plants don&#8217;t necessarily have to be gas turbine–based. Plains End&#8217;s NOx and CO emissions are comparable to those [...]<img alt="" border="0" src="http://stats.wordpress.com/b.gif?host=powergen.wordpress.com&amp;blog=1986086&amp;post=57&amp;subd=powergen&amp;ref=&amp;feed=1" width="1" height="1" />]]></description>
			<content:encoded><![CDATA[<p><span style="font-size:12pt;font-family:Times New Roman;">Owned by PG&amp;E National Energy Group, and operated by Wärtsilä North America Inc.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Billed as the world&#8217;s largest natural gas–fired reciprocating engine generating station, the 111-MW Plains End Power Plant has successfully demonstrated that large distributed generation plants don&#8217;t necessarily have to be gas turbine–based. Plains End&#8217;s NOx and CO emissions are comparable to those of a plant powered by gas turbines with expensive catalysts, and its net efficiency comes close to that of a combined-cycle plant. One year&#8217;s operating experience proves that recip engines can compete with turbines for selected applications.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">By Sami Myllyviita, Wärtsilä North America Inc.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">In February 2001, Wärtsilä North America Inc. signed a contract with PG&amp;E National Energy Group (NEG) to engineer, procure, construct (EPC), and commission a 111-MW natural gas–fired reciprocating engine power plant for peaking service in the Rocky Mountains above Denver (Figure 1). Plains End now produces electricity under a 10-year power purchase agreement with Minneapolis-based Xcel Energy, which automatically dispatches the plant. Plains End LLC is a wholly owned, indirect subsidiary of NEG, which is headquartered in Bethesda, Md.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>1. Plains End.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The 111-MW Plains End plant is located in the foothills of the Rocky Mountains in Arvada, Colo., at an elevation of about 6,000 ft. It is said to be the world&#8217;s largest gas engine power plant.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Wärtsilä North America Inc.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">Construction of the power plant facility started in June 2002, and only 10 months later the plant was ready for commissioning. Wärtsilä was more than just the plant&#8217;s EPC contractor; it operates and maintains Plains End for NEG.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Bigger is better<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The innovative Plains End facility is the largest natural gas–fired, internal combustion generating installation in North America. It consists of a preengineered, prepackaged string of 20 gas-fired, spark-ignited reciprocating engine/generating sets from Wärtsilä.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">The power plant consists of two power blocks, each with 10 generating sets. The blocks are located at the sides of a central complex housing the control room, electrical annex, and workshops. The 20 Wärtsilä 18V34SG units, each rated at 5.7 MW, generate electricity at a voltage of 13.8 kV, which is then converted to a distribution voltage of 230 kV by two step-up transformers in an adjacent substation.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>The engine advantage<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;">Beyond their ability to be deployed quickly, reciprocating engines have several important advantages:<br />
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<li><span style="font-size:12pt;font-family:Times New Roman;">Unlike gas turbines, recip engines demonstrate consistent heat rate and output at mile-high elevations such as Arvada&#8217;s—even during hot summer days, when the ambient temperature can approach 104F. During its performance test, Plains End units achieved 44.2% efficiency (LHV) at full load, and 39.7% efficiency (LHV) at 50% load. Those numbers are significantly higher than those of comparable-size gas turbines at the same elevation.<br />
</span></li>
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<p><span style="font-size:12pt;font-family:Times New Roman;">• The plant requires little, if any, process water (Figure 2). No water is used for intake air conditioning, and the engines&#8217; cooling circuits reject their heat to the atmosphere through closed-loop radiators rather than cooling towers. This provides both economic and social benefits, because in many parts of the U.S. sufficient water is either unavailable for use by power plants or prohibitively expensive.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>2. Water wise.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The plant requires little, if any, process water. No water is used for intake air conditioning, and the engines&#8217; cooling circuits reject their heat to the atmosphere through closed-loop radiators rather than cooling towers.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Wärtsilä North America Inc.</span></p>
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<li><span style="font-size:12pt;font-family:Times New Roman;">The plant can go from a warm standby condition—the normal shutdown state for the engines—to full output in 10 minutes. The plant was actually dispatched in this fashion several times during the first several weeks of commercial operation.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">The design permits several start/stop cycles per day, with rapid load increases and reductions, without negative impact on the engines. This allows the scheduling of maintenance inspections to be based on actual operating hours rather than on calculated &#8220;equivalent hours&#8221; that take into account the number of start-stop cycles, changes in fuels, and operation at overload conditions.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">The plant is able to maintain its low heat rate by optimizing the number and load set points of each of the 20 engines. A quantifiable technology benefit is produced by the ability of the genset to be rapidly cycled several times a day without increasing maintenance costs.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">The plant requires only 65 psig of natural gas pressure to operate at full load—much lower than that of a gas turbine.<br />
</span></li>
<li><span style="font-size:12pt;font-family:Times New Roman;">The modular design of Plains End (Figure 3) and similar plants eliminates the need to shut the plant down completely for planned maintenance (Figure 4). Individual gensets can be taken off-line for inspection and maintenance during off-peak demand periods. Wärtsilä&#8217;s recommended maintenance schedule includes a major inspection after 64,000 operating hours.<br />
</span></li>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>3. Plant configuration.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The Plains End facility has twenty 5.7-MW Wärtsilä gas-fired, spark-ignited reciprocating engine/generating sets. They are configured in two power blocks of 10 units each.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Wärtsilä North America Inc.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>4. Modular advantages.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">The modular design of Plains End and similar plants eliminates the need to shut the plant down completely for planned maintenance. Individual gensets can be taken off-line for inspection and maintenance during off-peak demand periods.<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Wärtsilä North America Inc.</span></p>
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<li><span style="font-size:12pt;font-family:Times New Roman;">The plant can be dispatched remotely with minimum or no operating staff.<br />
</span></li>
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Meeting environmental concerns<br />
</strong></span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Local authorities were initially worried that Plains End might produce rising columns of exhaust smoke or continuous steam clouds, adding to those from power plants in the Denver metro area. However, the plant&#8217;s closed-loop radiators create no visible water vapor plumes. Likewise, its exhaust gases create no visible steam plumes. Nonetheless, the height of the exhaust gas stacks was kept to less than 60 ft to keep the plant&#8217;s profile reasonably low.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Plains End&#8217;s emissions are very low thanks to the technology employed by the reciprocating engines. They make use of precombustion chambers, individual cylinder temperature control, and lean-burn technology. CO and volatile organic compounds (VOCs) are further controlled by an oxidation catalyst. NOx emissions are controlled with selective catalytic reduction (SCR) technology, using urea as a reagent. At Plains End, stack emission levels have been well below the expected values of 18 ppm CO and 9 ppm NOx (see table, page 84).<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Highly reliable and available<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;">Moreover, when a specific plant dispatch mode is selected, the plant follows the AGC-initiated load demand by ramping the plant load up and down at a maximum rate of 12 MW/min between 50% and 100% of full-rated output. This enables Xcel to absorb load swings in its distribution system.<br />
</span></p>
<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>5. Remote control.<br />
</strong></span></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Plains End is operated remotely and dispatched by Xcel Energy&#8217;s Automated Generation Control (AGC) system. The plant follows the AGC-initiated load demand by ramping the plant load up and down at a maximum rate of 12 MW/min between 50% and 100% of full-rated output.<br />
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Courtesy: Wärtsilä North America Inc.</span></p>
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<p><span style="font-size:12pt;font-family:Times New Roman;">In its first 11 months of operation, Plains End achieved an availability of 98.7% while generating more than 154,587 MWh. Over this period, each of its engines operated an average of 1,463 hours.<br />
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<p><span style="font-size:12pt;font-family:Times New Roman;"><strong>Table<br />
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<p style="text-align:center;"><img src="http://powergen.files.wordpress.com/2008/06/062308-0219-plainsendpo6.jpg?w=550" alt="" /></p>
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<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Contract performance guarantees and acceptance test results<br />
</span></p>
<p style="text-align:center;"><span style="font-size:10pt;font-family:Times New Roman;">Source: Wärtsilä North America Inc.</span></p>
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