英语翻译本次设计为苯乙烯生产中年处理3.6万吨苯乙烯-乙苯分离装置的设计.我国苯乙烯生产通常采用负压绝热脱氢法,装置由乙苯脱氢和脱氢混合液精馏两部分组成.脱氢混合液的主要组成为

Question

英语翻译
本次设计为苯乙烯生产中年处理3.6万吨苯乙烯-乙苯分离装置的设计.
我国苯乙烯生产通常采用负压绝热脱氢法,装置由乙苯脱氢和脱氢混合液精馏两部分组成.脱氢混合液的主要组成为苯、甲苯、乙苯、苯乙烯和焦油等.其中乙苯(EB)与苯乙烯的分离是精馏的最关键技术.本文就是采用精馏的技术.
本文对苯乙烯-乙苯分离装置的物料衡算,热量衡算,还有精馏塔的塔体工艺尺寸的计算还有附属设备换热器、储罐、管径、泵的计算进行了计算.

Answer 1

The design for the production processing 36000 tons of styrene middle-aged styrene-ethylbenzene device design separation. Our country styrene by negative pressure production usually adiabatic dehydrogenation, ethylbenzene dehydrogenation and dehydrogenation device consists of a mixture of two parts, distillation. The main composition for the mixture of dhea benzene, toluene, ethylbenzene, styrene and tar, etc. Among them (EB) and analyses the separation of styrene is the most key technology of distillation. This paper is the distillation of the technology. This paper analyses the device-styrene separation material calculation, heat balance calculations, and the tower of the column of the size of the body process calculation and ancillary equipment heat exchanger, tanks, diameter, the calculation of the pump was calculated.
设计生产加工36000吨styrene-ethylbenzene苯乙烯的中年设备设计分离.我国苯乙烯生产通常由负压脱氢绝热,乙苯脱氢制和脱氢装置由两部分组成的混合物,蒸馏.主要成分对混合物的脱氢表雄酮苯、甲苯、乙苯、苯乙烯和焦油等.其中(EB)和分析了苯乙烯的分离是最关键的技术的蒸馏.摘要本文是蒸馏的技术.本文分析了计算device-styrene分离材料,热量平衡计算,该塔列身体的大小的工艺计算及辅助设备热交换器、坦克、直径、泵的计算进行了计算.