摘要
针对某厂的2种不同衍生气原料气,设计出3套低温甲醇洗工艺流程,流程1为8塔低温甲醇洗方案,最后得到净化产品气中酸性组分H_(2)S摩尔分数降到了0.1×10^(-6)以下,满足净化要求;流程2针对荒煤气衍生气中含有额外的C_(2)~C_(6)杂质尤其是苯杂质的特点而设计,为12塔低温甲醇洗方案,也可满足该厂的净化度要求;为进一步节能降耗,针对流程2又进行了换热网络分析,最终设计了流程3,将整个系统的冷公用工程降低了61.70%,热公用工程降低了61.14%,固定投资降低了37.89%,节省了投资。
Three sets of Rectisol process are designed for two different derived gases as feed gases in a certain plant.Among them,process 1 is an 8-tower Rectisol process designed for the first derivative gas,by which the content of H_(2)S in the purified product gas drops to less than 0.1 ppm,meeting the purification requirements.Process 2 is designed in view of the additional C_(2)-C_(6) impurities in the second wild coal gas derived gas,especially benzene impurities.Process 2 is a 12-tower Rectisol process,which can also meet the purification requirements of the plant.In order to further save energy and reduce consumption,heat exchange network analysis is carried out for process 2.Finally,process 3 is designed,which reduces the cold utilities of the entire system by 61.70%,the heat utilities by 61.14%,and the fixed investment by 37.89%,saving a lot of total investment.
作者
李昊洲
李燕
张述伟
LI Hao-zhou;LI Yan;ZHANG Shu-wei(State Key Laboratory of Fine Chemicals,Dalian University of Technology,Dalian 116024,China;School of Chemical Engineering,Dalian University of Technology,Dalian 116024,China)
出处
《现代化工》
CAS
CSCD
北大核心
2022年第4期237-244,共8页
Modern Chemical Industry
关键词
低温甲醇洗
荒煤气
苯杂质
工艺设计
模拟分析
Rectisol
wild coal gas
benzene impurities
process design
simulation analysis