热力发电
熱力髮電
열력발전
Thermal Power Generation
2015年
10期
77-81
,共5页
吕凯%彭兆春%刘文华%李高潮%叶军%陈胜利
呂凱%彭兆春%劉文華%李高潮%葉軍%陳勝利
려개%팽조춘%류문화%리고조%협군%진성리
直接空冷机组%机组背压%板式蒸发式凝汽器%环境温度%空气湿度%冷凝量%水耗率
直接空冷機組%機組揹壓%闆式蒸髮式凝汽器%環境溫度%空氣濕度%冷凝量%水耗率
직접공랭궤조%궤조배압%판식증발식응기기%배경온도%공기습도%냉응량%수모솔
direct air-cooling unit%unit back pressure%plate evaporative condenser%environmental tempera-ture%ambient temperature%air humidity%condensation amount%water consumption rate
针对直接空冷机组在夏季时背压偏高、出力受限的问题,提出采用板式蒸发式凝汽器分流部分汽轮机排汽,以降低空冷岛热负荷,从而降低机组背压.以某300 MW直接空冷机组为例进行上述技术改造.改造后机组运行结果表明:额定负荷工况、环境温度30℃下,投运板式蒸发式凝汽器系统后,机组背压由33.47 kPa 降至29.05 kPa,达到了额定工况下,对机组背压的要求(设计值30 kPa);TRL工况、环境温度30℃下(湿球温度为17.68℃),板式蒸发式凝汽器系统冷凝能力为50.11 t/h,机组背压较投运前降低4.1 kPa;板式蒸发式凝汽器的水耗率为0.7~0.8;板式蒸发式凝汽器系统的运行效果随着环境温度的升高而提高;板式蒸发式凝汽器的冷凝量和补水流量随着外部空气湿度的增大而减小,且趋势相同,空气湿度增大到一定程度后,其冷凝量和补水流量趋于定值.
針對直接空冷機組在夏季時揹壓偏高、齣力受限的問題,提齣採用闆式蒸髮式凝汽器分流部分汽輪機排汽,以降低空冷島熱負荷,從而降低機組揹壓.以某300 MW直接空冷機組為例進行上述技術改造.改造後機組運行結果錶明:額定負荷工況、環境溫度30℃下,投運闆式蒸髮式凝汽器繫統後,機組揹壓由33.47 kPa 降至29.05 kPa,達到瞭額定工況下,對機組揹壓的要求(設計值30 kPa);TRL工況、環境溫度30℃下(濕毬溫度為17.68℃),闆式蒸髮式凝汽器繫統冷凝能力為50.11 t/h,機組揹壓較投運前降低4.1 kPa;闆式蒸髮式凝汽器的水耗率為0.7~0.8;闆式蒸髮式凝汽器繫統的運行效果隨著環境溫度的升高而提高;闆式蒸髮式凝汽器的冷凝量和補水流量隨著外部空氣濕度的增大而減小,且趨勢相同,空氣濕度增大到一定程度後,其冷凝量和補水流量趨于定值.
침대직접공랭궤조재하계시배압편고、출력수한적문제,제출채용판식증발식응기기분류부분기륜궤배기,이강저공랭도열부하,종이강저궤조배압.이모300 MW직접공랭궤조위례진행상술기술개조.개조후궤조운행결과표명:액정부하공황、배경온도30℃하,투운판식증발식응기기계통후,궤조배압유33.47 kPa 강지29.05 kPa,체도료액정공황하,대궤조배압적요구(설계치30 kPa);TRL공황、배경온도30℃하(습구온도위17.68℃),판식증발식응기기계통냉응능력위50.11 t/h,궤조배압교투운전강저4.1 kPa;판식증발식응기기적수모솔위0.7~0.8;판식증발식응기기계통적운행효과수착배경온도적승고이제고;판식증발식응기기적냉응량화보수류량수착외부공기습도적증대이감소,차추세상동,공기습도증대도일정정도후,기냉응량화보수류량추우정치.
In summer,the direct air cooling units will suffer high back pressure and its output power will be insufficient.Against this problem,the plate evaporative condensing system was proposed to diverge part of the turbine exhaust steam and reduce the heat load of air cooling island,thus the unit operating back pres-sure can be decreased.Taking a 300 MW direct air cooling unit as the example,the retrofitting was carried out.The operation results show that,under condition with rated load and ambient temperature of 30 ℃,af-ter the plate evaporative condensing system was put into service,the unit back pressure decreased from 33. 47 kPa to 29.05 kPa,satisfying the requirements under rated condition (30 kPa).Under the TRL condition and at ambient temperature of 30 ℃ (the wet bulb temperature of 17.68 ℃),the condensing ability of the plate evaporative condensing system was 50.11 t/h,and the unit back pressure decreased by 4.1 kPa.The water consumption rate of the plate evaporative condensing system was 0.7 to 0.8.The operation effect of the plate evaporative condensing system got better with an increase in the ambient temperature.As the hu-midity of the ambient air increased,both the steam flow and supplement circulating water flow decreased and with the similar trend.When the air humidity climbed to a certain value,the steam flow and supple-ment circulating water flow approached to a definite value.The results show the retrofit meets the design requirements and the system runs stably.