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method for separating isoprene from c5 hydrocarbon mixtures containing isoprene.

机译:从含有异戊二烯的C5烃混合物中分离异戊二烯的方法。

摘要

1417733 Distilling hydrocarbons SNAMPROGETTI SpA 26 Jan 1973 [28 Jan 1972] 4244/73 Heading C5E Isoprene is separated from a C 5 cut, e.g. from steam-cracking, by (a) rectifying (at 17) to take overhead (3) C 4 hydrocarbons, low-boiling acetylenes and the greater part of the isopentane, to take off as bottoms (4) any polymers and part of the high-boiling hydrocarbons, and leave a side-stream (5) of impure isoprene; (b) subjecting this stream to an extractive distallation (26) with a solvent comprising a polar organic compound and water to take overhead (27) isoprene together with acrylic C 5 olefines, cyclopentene, normal pentane and the remainder of the isopentane, to take off as bottoms (28) solvent, and leave a side-stream (29) of cyclopentadiene monomer and other hydrocarbons soluble in the solvent; (c) subjecting the overhead (27) to a second extractive distillation (21) to take overhead (11) acyclic olefines, normal pentane and isopentane, and as bottoms (12) isoprene, cyclopentene and solvent; (d) flashing this bottoms stream (at 22) to give an isoprene stream (13) and a stream (24) comprising the solvent with enough isoprene to serve as reflux in the first extractive distillation, (e) rectifying the stream (13) of isoprene from the flash evaporator to take off as bottoms (15) the heavy hydrocarbons still remaining, as overhead (14) a stream of isoprene with traces of low-boiling hydrocarbons, which is recycled to the first rectification, and as a sidestream (16) isoprene of polymerization quality; and (f) recycling to the first extractive distillation (26) the bottoms from the flash evaporator. As shown, the solvent from the bottom of column 26 is that supplied to the top of column 21, by line 28. In a modification (Fig. 1, not shown), only two streams are taken off from the first extractive distillation, the bottoms comprise solvent, cyclopentadiene monomer and highboiling acetylenes, and are stripped, the solvent going to the second extractive distillation, and the hydrocarbons to a rectifying column (20) where a bottoms comprising cyclopentadiene monomer, high-boiling acetylenes and a large proportion of dienes other than isoprene is discarded (8), and an overhead stream (9) of isoprene is recycled to the first rectification. Polar organic compounds suitable for use in the solvent are N-formylmorpholine, morpholine, aniline, acetonitrile, furfural, dimethylformamide, dimethylacetamide, N-methylpyrrolidone, beta-methoxy-propionitrile, and mixtures of these with one another. Reference has been directed by the Comptroller to Specification 1,283,519.
机译:1417733蒸馏碳氢化合物SNAMPROGETTI SpA 1973年1月26日[1972年1月28日] 4244/73标题C5E异戊二烯与C 5馏分分离,例如(a)进行精馏(在17处)以除去塔顶馏出物(3)C 4碳氢化合物,低沸点乙炔和大部分异戊烷,从塔底馏出物作为残渣(4)除去任何聚合物和一部分高沸点碳氢化合物,并留下不纯异戊二烯的支流(5); (b)用包含极性有机化合物和水的溶剂对该物流进行萃取性远端化(26),以将塔顶(27)异戊二烯与丙烯酸C 5烯烃,环戊烯,正戊烷和其余的异戊烷一起吸收。除去作为底部溶剂(28),并留下环戊二烯单体和可溶于该溶剂的其他烃的支流(29); (c)将塔顶馏出物(27)进行第二次萃取蒸馏(21),以得到塔顶馏出物(11)无环烯烃,正戊烷和异戊烷,以及作为塔底馏出物(12)的异戊二烯,环戊烯和溶剂; (d)闪蒸该塔底料流(在22)以得到异戊二烯流(13)和包含具有足够异戊二烯的溶剂的流(24),以在第一萃取蒸馏中用作回流,(e)精馏该流(13)从闪蒸器分离出的异戊二烯作为残渣(15)除去残留的重烃,作为塔顶馏出物(14)除去痕量低沸点烃的异戊二烯流,将其再循环至第一精馏,并作为侧流( 16)异戊二烯的聚合质量; (f)将来自闪蒸器的塔底物再循环至第一萃取蒸馏(26)。如图所示,来自塔26底部的溶剂是通过管线28供应到塔21顶部的溶剂。在一种改进方案(图1,未显示)中,只有两股物流从第一萃取蒸馏中排出,塔底馏出物包括溶剂,环戊二烯单体和高沸点乙炔,并进行汽提,将溶剂进行第二次萃取蒸馏,并将烃类馏分至精馏塔(20),在精馏塔(20)中,塔底馏出物包括环戊二烯单体,高沸点乙炔和大部分二烯。除去异戊二烯以外的其他物质(8),并将异戊二烯的塔顶物流(9)再循环至第一精馏。适用于溶剂的极性有机化合物是N-甲酰基吗啉,吗啉,苯胺,乙腈,糠醛,二甲基甲酰胺,二甲基乙酰胺,N-甲基吡咯烷酮,β-甲氧基丙腈,以及它们的混合物。主计长已对规范1,283,519进行了引用。

著录项

  • 公开/公告号DK138845C

    专利类型

  • 公开/公告日1979-04-17

    原文格式PDF

  • 申请/专利权人 SNAM PROGETTI S.P.A.;

    申请/专利号DK19730000440

  • 发明设计人 RESCALLI C;GINNASI A;REBORA P;

    申请日1973-01-26

  • 分类号C07C11/18;C07C7/08;

  • 国家 DK

  • 入库时间 2022-08-22 20:47:53

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