首页> 外国专利> 'PROCESS FOR 1,3- BUTADIENE SEPARATION FROM A CRUDE C4 STREAM WITH ACETYLENE CONVERTER',

'PROCESS FOR 1,3- BUTADIENE SEPARATION FROM A CRUDE C4 STREAM WITH ACETYLENE CONVERTER',

机译:“从带有乙炔转化器的C4粗馏分中分离1,3-丁二烯的方法”,

摘要

pDisclosed is a method of recovering 1,3 -butadiene from a C4 stream containing butane, isobutane, 2-butene, 1-butene, isobutene, butadiene and acetylene. The process of recovering highly pure 1,3 -butadiene includes acetylene conversion for selectively converting acetylene through liquid-phase hydrogenation, so that the acetylene content is decreased to 70 wt ppm or less, and 1,3 -butadiene extraction using an extractive distillation column, a pre-separator, a solvent stripping column, a solvent recovery column, and a purification column. Through the acetylene conversion, the concentration of vinylacetylene is decreased to 70 wt ppm or less, after which 1,3-butadiene is recovered using only one extractive distillation column, thereby considerably decreasing the degree of utility and the loss of streams in the course of extraction. The number of units necessary for the process is decreased, thus remarkably reducing the time during which impurities can accumulate in a processing unit./p[WO2010008109A1]
机译:公开了一种从包含丁烷,异丁烷,2-丁烯,1-丁烯,异丁烯,丁二烯和乙炔的C4料流中回收1,3-丁二烯的方法。回收高纯度的1,3-丁二烯的过程包括乙炔转化,以通过液相加氢选择性地转化乙炔,从而使乙炔含量降至70 wt ppm或更小,以及使用萃取蒸馏塔萃取1,3-丁二烯,预分离器,溶剂汽提塔,溶剂回收塔和纯化塔。通过乙炔转化,乙烯基乙炔的浓度降低至70 wt ppm或更低,此后仅使用一个萃取蒸馏塔就可以回收1,3-丁二烯,从而大大降低了使用过程中的利用率和物流损失萃取。该过程所需的单元数减少了,从而显着减少了杂质在处理单元中累积的时间。 [WO2010008109A1]

著录项

  • 公开/公告号IN288114B

    专利类型

  • 公开/公告日2017-10-13

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN303/CHENP/2010

  • 发明设计人

    申请日2008-07-18

  • 分类号

  • 国家 IN

  • 入库时间 2022-08-21 13:37:55

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