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富气压缩系统的改进——直接水冷法 被引量:2
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作者 曹新波 段占庭 《现代化工》 EI CAS CSCD 北大核心 2002年第10期44-46,共3页
提出一种改进富气压缩系统的新工艺———直接水冷法 ,可大幅度提高富气压缩机的入口压力 ,从而降低压缩机功耗 ,增大其处理能力 ,同时还可改善分离效果。以 1 50万t/a规模的工业装置为基准 ,模拟结果表明 ,与原流程相比 ,采用直接水冷... 提出一种改进富气压缩系统的新工艺———直接水冷法 ,可大幅度提高富气压缩机的入口压力 ,从而降低压缩机功耗 ,增大其处理能力 ,同时还可改善分离效果。以 1 50万t/a规模的工业装置为基准 ,模拟结果表明 ,与原流程相比 ,采用直接水冷法后压缩机入口压力可提高约 50kPa ,压缩机功耗降低 1 1 8%。 展开更多
关键词 富气压缩系统 直接水冷法 技术改进 催化裂化装置
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催化裂化装置回收系统的进展和改进 被引量:2
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作者 曹新波 段占庭 《炼油技术与工程》 CAS 北大核心 2003年第3期23-26,共4页
分析了目前我国催化裂化装置回收系统存在的主要问题及其产生的原因 ,综述了国内催化裂化装置回收系统工艺技术和设备的进展情况 ,重点介绍了清华大学开发的一种新型回收工艺。该工艺提出了微分冷凝、直接水冷法、C5作为吸收剂等多项改... 分析了目前我国催化裂化装置回收系统存在的主要问题及其产生的原因 ,综述了国内催化裂化装置回收系统工艺技术和设备的进展情况 ,重点介绍了清华大学开发的一种新型回收工艺。该工艺提出了微分冷凝、直接水冷法、C5作为吸收剂等多项改进措施。对今后催化裂化装置回收系统的研究方向进行了探讨。 展开更多
关键词 催化裂化装置 回收系统 流程设计 微分冷凝 直接水冷法 吸收剂
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Waste heat water pumping model with direct contact cooling
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作者 Kittiwoot Sutthivirode Naris Pratinthong +2 位作者 Pichai Namprakai Natthaphon Roonprasang Taveewat Suparos 《Journal of Central South University》 SCIE EI CAS 2014年第10期3896-3910,共15页
The performance of a patented water pumping model with steam-air power was presented, which operates automatically by direct contact cooling method. The main objective was to study feasibility of a pumping model for u... The performance of a patented water pumping model with steam-air power was presented, which operates automatically by direct contact cooling method. The main objective was to study feasibility of a pumping model for underground water. In this model, a heater installed within the heat tank represented sources of waste heat as energy input for finding appropriate conditions of the 10 L pump model. The system operation had five stages: heating, pumping, vapor flow, cooling, and water suction. The overall water heads of 3, 4.5, 6 and 7.5 m were tested. At the same time, it was found that the pump with 50% air volume is sufficient for pumping water to a desired level. In the experiment, the temperatures in the heating and pumping stages were 100-103 ℃and 80-90 ℃, respectively. The pressure in the pumping stage was 12-18 kPa, and the pressure in the suction stage was about-80 kPa, sufficient for the best performance. It could pump 170 L of water at a 2 m suction head, 120 L at a 3.5 m suction head, 100 L at a 5 m suction head, and 65 L at a 6.5 m suction head in 2 h. A mathematical model for larger pumps was also presented, which operates nearly the same as the present system. Economic analysis of the 10 L pump was also included. 展开更多
关键词 direct contact cooling driving tank steam-air power liquid piston waste heat
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