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《国际自然能源杂志》2012,33(1):50-57
ABSTRACTCombined power plants are among the most attractive options to optimally utilise conventional fuel energy with respect to energy conversion and the environment. In the present study, a dual-pressure heat recovery steam generator (HRSG) used in a gas/steam combined cycle power plant is investigated. This paper presents exergy and economic analysis of a dual-pressure HRSG. The parameters used for the investigation of the exergo-economic study are pinch point, fuel price, cost of exergy losses, gas turbine inlet temperature and cycle pressure ratio. A parametric study shows that the considered parameters have a huge impact on the total annual cost per unit exergy of steam produced in the HRSG. It is seen that best exergo-economic conditions are obtained at the pinch point value of 10?K to get the total annual cost per unit exergy of steam produced to be the minimum. 相似文献
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介绍了武汉钢铁集团公司的燃气-蒸汽联合循环发电站(CCPP)的特点和变频启动技术在这个项目中应用。重点介绍了CCPP启动变频器整体结构、组成及几种控制功能。 相似文献
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以西门子SGT5-4000F型联合循环机组为例,就对机组启停及运行具有重要影响的排气温度控制进行了分析,说明了排气温度控制的作用、控制原理以及影响排气温度控制的各种因素,为相关的事件分析和优化工作提供了基础。 相似文献
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Do-Hwan Kim Jae-Hwan Cha Soon-Heon Hong Dong-Youn Kim Chang-Won Kim 《Korean Journal of Chemical Engineering》2009,26(1):90-101
The corrosion of metal pipes in water distribution networks is a complex electrochemical and physicochemical phenomenon between
a metal surface and corrosive water. The level of corrosion in water distribution systems was controlled by manipulating the
calcium carbonate precipitation potential (CCPP) concentration, and the corrosive water quality was controlled in two steps
within the advanced water treatment plant (AWTP) constructed at the Institute of Water Quality Research (IWQR), Busan Metropolitan
City, Korea. The 1
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control step was located before a coagulation process included on a rapid mixer, and the 2
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control step was located after a biological activated carbon (BAC) process. The capacity of the AWTP in IWQR was 80 m3/day. The CCPP concentration was controlled from the calcium hardness, alkalinity, and pH by adding calcium hydroxide (Ca(OH)2), sodium carbonate (Na2CO3), and carbon dioxide (CO2) in the above two steps. A CCPP control system was installed and operated according to the developed algorithm to maintain
a CCPP range of 0–4 mg/L. The CCPP range was reasonably controlled to induce the formation of a CaCO3 film on the surface of the simulated water distribution system (SWDS). From the result of the corrosive water control, the
CCPP formed greater than 0.0 mg/L. The crystalloid structure of the scale produced by CCPP control in the inner surface of
pipe was zinc carbonate hydroxide hydrate (Zn4CO3(OH)6·H2O). 相似文献
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