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浅谈如何延长天然气净化装置连续运行周期 被引量:2
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作者 王晓东 彭维茂 《石油与天然气化工》 CAS CSCD 北大核心 2006年第2期164-166,共3页
天然气净化装置的计划外停产损失重大。本文通过对计划外停产因素的分析,结合生产现状,提出了延长装置运行周期的几点措施。
关键词 天然净化装置 连续运行周期 原料气气质 设备管线腐蚀
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低温甲醇洗系统工艺优化调整小结
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作者 谢辉 《中氮肥》 CAS 2022年第3期36-39,共4页
安徽晋煤中能化工股份有限公司300 kt/a甲醇装置采用航天炉制气、可控移热变换、大连理工九塔流程低温甲醇洗工艺。2021年5月中旬,低温甲醇洗系统出口净化气硫含量超标且小幅波动。通过对系统运行情况进行彻底排查与梳理,确认是低温甲... 安徽晋煤中能化工股份有限公司300 kt/a甲醇装置采用航天炉制气、可控移热变换、大连理工九塔流程低温甲醇洗工艺。2021年5月中旬,低温甲醇洗系统出口净化气硫含量超标且小幅波动。通过对系统运行情况进行彻底排查与梳理,确认是低温甲醇洗系统存在氨累积所致。为此,一方面,增大系统带出氨量,减少返回系统的氨量;另一方面,从源头加以控制,减少变换气带入低温甲醇洗系统的氨量。经过近2周的工艺优化调整,低温甲醇洗系统运行工况有效改善,净化气硫含量达标。从本次异常工况的处理中总结经验,建议定期对低温甲醇洗系统甲醇循环中关键部位物料的氨含量进行分析,并抓好原料气气质管理等。 展开更多
关键词 低温甲醇洗系统 净化硫含量超标 原因分析 氨累积 工艺优化调整 经验总结 氨含量分析 原料气气质管理
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Energetic analysis of gasification of biomass by partial oxidation in supercritical water 被引量:1
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作者 关清卿 韦朝海 +5 位作者 柴欣生 宁平 田森林 谷俊杰 陈秋玲 庙荣荣 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第1期205-212,共8页
Partial oxidation gasification in supercritical water could produce fuel gases(such as H2, CO and CH4) and significantly reduce the energy consumption. In this work, an energetic model was developed to analyze the par... Partial oxidation gasification in supercritical water could produce fuel gases(such as H2, CO and CH4) and significantly reduce the energy consumption. In this work, an energetic model was developed to analyze the partial oxidative gasification of biomass(glucose and lignin) in supercritical water and the related key factors on which gasification under autothermal condition depended upon. The results indicated that the oxidant equivalent ratio(ER) should be over 0.3 as the concern about energy balance but less than 0.6 as the concern about fuel gas production. Feedstocks such as glucose and lignin also had different energy recovery efficiency. For materials which can be efficiently gasified, the partial oxidation might be a way for energy based on the combustion of fuel gases. Aromatic materials such as lignin and coal are more potential since partial oxidation could produce similar amount of fuel gases as direct gasification and offer additional energy. Energy recovered pays a key role to achieve an autothermal process. Keeping heat exchanger efficiency above 80% and heat transfer coefficient below15 k J·s-1is necessary to maintain the autothermal status. The results also indicated that the biomass loading should be above 15% but under 20% for an autothermal gasification, since the increase of biomass loading could improve the energy supplied but decrease the efficiency of gasification and gaseous yields. In general,some specific conditions exist among different materials. 展开更多
关键词 AUTOTHERMAL GASIFICATION Supercritical water BIOMASS Energetic model
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