首页> 外文期刊>Coke and chemistry >REMOVING THIOPHEN FROM COKING BENZENE AND MAKING PURE THIOPHEN FROM THE THIOPHEN FRACTION BY EXTRACTIVE RECTIFICATION. INDUSTRIAL PLANT DESIGN
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REMOVING THIOPHEN FROM COKING BENZENE AND MAKING PURE THIOPHEN FROM THE THIOPHEN FRACTION BY EXTRACTIVE RECTIFICATION. INDUSTRIAL PLANT DESIGN

机译:通过萃取整流从焦化苯中除去噻吩并从噻吩组分中制取噻吩。工业厂房设计

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摘要

In the 1960s and 1970s, the technological laboratory at this institute devised a method of making pure thiophen by extractive rectification of the commercial thiophen fraction (30-35 percent) made at the Makeev coking and chemical plant by periodic rectification with a high-performance column with large phlegm numbers (R = 30-50). The process involved considerable energy consumption, which made it not very competitive. As separating agents, proposals have been made for organic solvents such as A^AZ-dimethylformamide (DMFA), V-methylpyrrolidone, and certain others [1]. These compounds increase the relative volatility in the benzene-thiophen system from a =1.13 to a = 1.45-1.60, so rectification columns of ordinary performance could be used with low phlegm numbers. The products are purified benzene and pure thiophen. The method was checked out with an enlarged test system (patch column of diameter 70 mm) in continuous operation by the use of DMFA as separating agent.
机译:在1960年代和1970年代,该研究所的技术实验室设计了一种方法,该方法是通过萃取精制在马凯夫焦化和化工厂生产的商业噻吩馏分(30-35%),并使用高性能色谱柱定期精馏来制备纯噻吩痰量大(R = 30-50)。该过程涉及大量的能源消耗,这使其竞争力不强。作为分离剂,已经提出了对有机溶剂如A ^ AZ-二甲基甲酰胺(DMFA),V-甲基吡咯烷酮和某些其他溶剂的建议[1]。这些化合物将苯噻吩系统中的相对挥发性从a = 1.13增加到a = 1.45-1.60,因此可以使用具有低痰液数的常规性能精馏塔。产物是纯苯和纯噻吩。在连续操作中,使用DMFA作为分离剂,使用扩大的测试系统(直径70毫米的接插柱)对方法进行了检验。

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