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作 者:陈莹[1] 刘超锋[2] 梁基照[1] 赵彬[3] 倪平平[4]
机构地区:[1]华南理工大学机械与汽车工程学院,广州510640 [2]郑州轻工业学院化工系,郑州450002 [3]中国石化中原石油化工股份有限公司,河南457000 [4]西南石油大学机电工程学院,成都610500
出 处:《广州化工》2008年第6期77-78,共2页GuangZhou Chemical Industry
摘 要:简介了合成气一步法生产二甲醚的优点、反应原理。以年产1万吨二甲醚的固定床反应器设计为例,介绍固定床反应器工艺计算和结构计算情况。该固定床反应器工艺计算涉及物料恒算、热量恒算和传热计算,其结构计算严格依据GB150-1998。该固定床反应器结构不复杂,易于制造。Advantages and the principle about reaction of one-step producing dimethyl ether with synthesis gas were simply introduced. With fixed-bed reactor for producing dimethyl ether with an annual output of 10^4 tons as example, the calculation situations of process and structure of fixed-bed reactor were introduced. Process calculations of the fixed-bed reactor involved material balance, heat balance and heat-transfer calculations, and its structural calculation were based on GB150-1998. The fixed-bed reactor had not complex structure to make its manufacture easy.
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