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文章主要介绍容错性控制在上海五号沟LNG扩建项目中的应用和实现。整套控制系统包括新老站区DCS系统的集成和容错方法。 相似文献
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A numerical model has been developed to study the mixing of two initially stratified layers which are subjected to a uniform lateral heat flux. An important distinction is made between the free surface and the liquid/liquid interface with regard to the different flow characteristics of the two layers. In the upper layer where warm liquid is cooled at the evaporating surface, the convective circulation is featured by a strong downward core flow; in contrast, the fluid flow in the lower layer is mainly confined to the wall boundary and is much weaker. Flow visualization experiments show that mixing of two stratified layers generally involves two stages in sequence: migration of the interface and rapid mixing between the remaining liquids. The interface movement is due to entrainment mixing at the interface. When the two layers approach density equalization, the interface becomes increasingly unstable and the core flow in the upper layer is able to break into the lower layer. The base to side heat flux ratio appears to be a major factor in determining the mode and intensity of the subsequent mixing at a rollover incident. 相似文献
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This paper has proposed an improved liquefied natural gas (LNG) fuelled combined cycle power plant with a waste heat recovery and utilization system. The proposed combined cycle, which provides power outputs and thermal energy, consists of the gas/steam combined cycle, the subsystem utilizing the latent heat of spent steam from the steam turbine to vaporize LNG, the subsystem that recovers both the sensible heat and the latent heat of water vapour in the exhaust gas from the heat recovery steam generator (HRSG) by installing a condensing heat exchanger, and the HRSG waste heat utilization subsystem. The conventional combined cycle and the proposed combined cycle are modelled, considering mass, energy and exergy balances for every component and both energy and exergy analyses are conducted. Parametric analyses are performed for the proposed combined cycle to evaluate the effects of several factors, such as the gas turbine inlet temperature (TIT), the condenser pressure, the pinch point temperature difference of the condensing heat exchanger and the fuel gas heating temperature on the performance of the proposed combined cycle through simulation calculations. The results show that the net electrical efficiency and the exergy efficiency of the proposed combined cycle can be increased by 1.6 and 2.84% than those of the conventional combined cycle, respectively. The heat recovery per kg of flue gas is equal to 86.27 kJ s?1. One MW of electric power for operating sea water pumps can be saved. The net electrical efficiency and the heat recovery ratio increase as the condenser pressure decreases. The higher heat recovery from the HRSG exit flue gas is achieved at higher gas TIT and at lower pinch point temperature of the condensing heat exchanger. Copyright © 2006 John Wiley & Sons, Ltd. 相似文献
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用于燃气调峰和轻烃回收的管道天然气液化流程 总被引:17,自引:3,他引:14
管道天然气的长途输送一般都采用高压管输的方式,高压天然气经各地的调压站降压后才能供应给普通用户使用,调压过程中会有大量的压力能损失。为解决城市燃气用户特有的用气不均匀性问题,介绍了一种利用高压天然气调压过程的压力能膨胀制冷的管道天然气液化流程。应用该流程可以将管道里的一部分天然气液化制成LNG并储存起来,在用气高峰时将储存的LNG再汽化以增加供气量,满足下游用户的需求。这样能够增强燃气企业的“调峰”能力,有利于天然气管网的平稳运行。同时,利用该流程还可以回收天然气中的轻烃资源,为石化工业提供优质的化工原料。 相似文献
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采用危险源辨识、合规性核查、HAZOP分析、自控系统评价、安全仪表系统评价、安全阀设置评价、人为因素分析等方法,对6座在役LNG加气站开展首次工艺危害分析。辨识出高、中、低风险隐患共计106项,主要体现在工艺系统设计不合理、自控与安全仪表系统功能设计不完善、安全阀设置不合理、操作与运行管理不规范、安全间距不足等方面。综合考虑隐患的风险等级与整改难易程度,制定了风险管控措施。建议对建站较早的在役LNG加气站尽快开展首次工艺危害分析,对新建、改建、扩建LNG加气站,应在设计阶段开展工艺危害分析,及时发现并整改安全隐患,确保工艺本质安全. 相似文献