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作 者:高峰 常晓 朱长春 Gao Feng;Chang Xiao;Zhu Changchun(MCC Capital Engineering & Research Incorporation Ltd.,Beijing 100176China;Qian’an Zhonghua Coal Chemical Co.,Ltd.,Tangshan 064400,China)
机构地区:[1]中冶京诚工程技术有限公司,北京100176 [2]迁安中化煤化工有限责任公司,唐山064400
出 处:《燃料与化工》2019年第4期41-43,共3页Fuel & Chemical Processes
摘 要:粗苯回收工段存在蒸汽、冷却水、煤气消耗多,粗苯收率低等问题。通过技术改造,蒸汽消耗量由5.5t/h降至4.35t/h,每天节约蒸汽27.6t。冷却水用量由1250m^3/h降至620m^3/h,煤气用量由1120m^3/h降至820m^3/h。粗苯收率由0.828%升至0.847%,达到了增产降耗的目的。In crude benzol recovery unit,there existed such problems as high consumption in steam,cooling water and gas,as well as low yield of crude benzol.Through technical upgrading,the steam consumption decreased from 5.5 t/h to 4.35 t/h,with daily reduction of 27.6 t in total.The cooling water consumption fell from 1 250 m^3/h to 620 m^3/h,and gas consumption from 1 120 m^3/h to 820 m^3/h.The yield of crude benzol increased from 0.828% to 0.847%.As a result,the technical upgrading helped to lower energy consumption and increase crude benzol yield.
分 类 号:TQ522.53[化学工程—煤化学工程]
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