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摘要
为满足2-PH装置对C4原料含水量的限制,对其上游MTBE装置的醚后C4进行脱水设计。通过对各脱水方案进行比较,最终流程采用"冷冻机+聚结器+分子筛"的方式,可以将C4的含水量由1 800×10-6降低至10×10-6。经装置实际运行检验,采用此方式进行C4脱水是可行有效的。
Abstract
In order to meet the restriction upon water content of C4 raw material in 2-propylheptanol (2-PH) plant,a design is done for the dehydration of post-esterification C4 fractions in MTBE plant.Through the comparison of various dehydration schemes,final process adopts the way of "freezer+coalescer+molecular sieve",which can reduce the water content in C4 feedstock from 1,800 ppm to 10 ppm.It is verified through actual operation that this process is feasible and effective.
关键词
醚后C4
/
再生
/
吸附
/
脱水
Key words
post-esterification C4 fractions
/
regeneration
/
adsorption
/
dehydration
醚后碳四脱水工艺设计[J].
现代化工, 2020, 40(11): 224-226,229 DOI:10.16606/j.cnki.issn0253-4320.2020.11.046