发明名称 Process for 1,3-butadiene separation from a crude C4 stream with acetylene converter
摘要 <p>Disclosed 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>
申请公布号 KR101111015(B1) 申请公布日期 2012.04.04
申请号 KR20080069677 申请日期 2008.07.17
申请人 发明人
分类号 C10G45/32;C07C11/167;C10G65/12 主分类号 C10G45/32
代理机构 代理人
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