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天然气凝析液管道射流清管器清管效果分析
引用本文:朱海山,罗小明,姚海元,何立民,李清平.天然气凝析液管道射流清管器清管效果分析[J].石油与天然气化工,2013,42(6):598-601.
作者姓名:朱海山  罗小明  姚海元  何立民  李清平
作者单位:中国石油西南油气田公司重庆天然气净化总厂万州分厂;中国石油西南油气田公司重庆天然气净化总厂万州分厂;中国石油西南油气田公司天然气研究院;中国石油西南油气田公司重庆天然气净化总厂万州分厂
基金项目:国家科技重大专项课题“深水流动安全保障与水合物风险控制技术”(编号:2011ZX05026-004)。
摘    要:对万州天然气净化厂硫磺回收单元的蒸汽与凝结水构成进行了分析,并对蒸汽引射器重新选型以实现蒸汽梯级利用,以及采用凝结水罐排空蒸汽回收、凝结水循环利用、凝结水分压回收、蒸汽疏水阀优化选型以实现凝结水密闭式回收等优化措施作了详细的分析探讨。实施各项优化措施后,每处理1×10^4 m^3原料天然气(H2S质量分数为1%),综合能耗由1 303.38MJ降为最低约1 188.23MJ,与每处理1×10^4 m^3原料天然气(H2S质量分数为1%)综合能耗为2 010MJ的设计值相比,节能效果明显。

关 键 词:蒸汽  凝结水  优化  节能  硫磺回收
收稿时间:2013/9/16 0:00:00

Application analysis of by pass pigging for gas-condensed pipeline
Zhu Haishan,Luo Xiaoming,Yao Haiyuan,He Limin and Li Qingping.Application analysis of by pass pigging for gas-condensed pipeline[J].Chemical Engineering of Oil and Gas,2013,42(6):598-601.
Authors:Zhu Haishan  Luo Xiaoming  Yao Haiyuan  He Limin and Li Qingping
Affiliation:Wanzhou Branch of Chongqing Natural Gas Purification Plant General, PetroChina Southwest Oil & Gasfield Company, Chongqing 404001,China;Wanzhou Branch of Chongqing Natural Gas Purification Plant General, PetroChina Southwest Oil & Gasfield Company, Chongqing 404001,China;Research Institute of Natural Gas Technology, PetroChina Southwest Oil & Gasfield Company, Chengdu 610213, Sichuan, China;Wanzhou Branch of Chongqing Natural Gas Purification Plant General, PetroChina Southwest Oil & Gasfield Company, Chongqing 404001,China
Abstract:Based on the composition analysis of steam and condensation water of sulfur recovery unit in Wanzhou branch of Chongqing natural gas purification plant,this paper discussed these optimization measures.The steam ejector was redesigned to realize the application of stream cascading and the methods are used to realize the airtight recycling of condensation water such as recovering steam discharged from the condensation tank,recycling condensation water,recovering condensation water at partial pressure and optimizing the type of steam traps.The comprehensive energy consumption can be reduced from 1 303.38MJ to 1 188.23MJ per 1×10^4 m^3 containing 1%(mol)of H2 S after optimization.Compared with the design which consumes 2 010MJ per 1× 10^4 m^3 containing 1%(mol)of H2 S,the effect of energy saving is obvious.
Keywords:steam  condensation water  optimization  energy saving  sulfur recovery
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