首页> 外国专利> Improvements in and relating to the separation of aromatic hydrocarbons having conjugated unsaturated side groups from their mixtures with other aromatic hydrocarbons having no such characteristics, and especially to the purification of styrene, indene and similar compounds

Improvements in and relating to the separation of aromatic hydrocarbons having conjugated unsaturated side groups from their mixtures with other aromatic hydrocarbons having no such characteristics, and especially to the purification of styrene, indene and similar compounds

机译:从共轭不饱和侧基的芳烃与没有这种特性的其他芳烃的混合物中分离的改进,特别是苯乙烯,茚和类似化合物的提纯

摘要

Aromatic hydrocarbons having unsaturated side groups with a double bond in conjugated position to those of the aromatic nucleus are separated from their mixtures with aromatic hydrocarbons having no side groups or saturated side groups by distribution between two solvent layers which are immiscible or only partially miscible, and which dissolve preferentially hydrocarbons of the first and second types respectively, namely the solvent systems liquid sulphur dioxide-paraffinic hydrocarbons or aqueous alcohols-paraffinic hydrocarbons, and then separating the layers. Hydrocarbons of the first type include styrene, indene, a-methyl-, p-methyl-, and m-ethyl-styrenes, propenylbenzene, alkyl derivatives of indene, and polycyclic hydrocarbons such as vinyl-naphthalene. The second class includes benzene, naphthalene, anthracene, and derivatives with saturated side chains or saturated cyclic side groups such as toluene, ethylbenzene, xylene, and hydrindene. Mixtures of these occur in coal carbonization products, for example, benzoles and tars of which the 130-150 DEG C. fraction contains xylenes, ethylbenzene, and styrene, and the 170 DEG -190 DEG C. fraction contains indene with other aromatics; products of catalytic cracking or aromatization according to the processes of Specifications 552,115, 552,216, 574,963, 574,973, 575,766, 575,768, and 575,769, [all in Group IV], which contain styrene, and its derivatives, and indene; and dehydrogenation products of ethylbenzene. The paraffinic solvents may be either single paraffins such as liquid propane, isopentane or heptane or petroleum fractions of sufficiently different boiling range from the hydrocarbons to be separated. The aqueous alcohols are mixtures of water with one or more alcohols capable of dissolving 5-50 per cent. by weight thereof, e.g., methyl, ethyl, propyl, isopropyl, sec. and tert. butyl, ethylene chlorhydrin, ethylene glycol mono-alkyl ethers, propylene glycol and its mono-alkyl ethers. The aromatics with conjugated unsaturated side groups concentrate in the sulphur dioxide or aqueous alcohol, and the others in the upper paraffinic layer. Repeated distribution gives complete separation. Temperatures below normal are preferable. Multiple counter-current extraction in towers may be used continuously introducing the light and heavy solvents at bottom and top respectively, and the solute intermediately. Examples describe the extraction with liquid propane and sulphur dioxide at -50 or -55 DEG C. of mixtures of styrene with ethylbenzene or xylol, and indene with alkylbenzenes, and the extraction with isopentane and aqueous methanol or sulphur dioxide of styrene and ethylbenzene.ALSO:Aromatic hydrocarbons having unsaturated side groups with a double bond in conjugated position to those of the aromatic nucleus are separated from their mixtures with aromatic hydrocarbons having no side groups or saturated side groups by distribution between two solvent layers which are immiscible or only partially miscible, and which dissolve preferentially hydrocarbons of the first and second types respectively, namely the solvent systems liquid sulphur dioxide-paraffinic hydrocarbons or aqueous alcohols-paraffinic hydrocarbons, and then separating the layers. Hydrocarbons of the first type include styrene, indene, a -methyl-, p-methyl-, and m-ethyl-styrenes, propenylbenzene, alkyl derivatives of indene, and polycyclic hydrocarbons such as vinyl-naphthalene. The second class includes benzene, naphthalene, anthracene, and derivatives with saturated side chains or saturated cyclic side groups such as toluene, ethylbenzene, xylene, and hydrindene. Mixtures of these occur in coal carbonisation products, for example benzoles and tars of which the 130-150 DEG C. fraction contains xylenes, ethylbenzene, and styrene, and the 170-190 DEG C. fraction contains indene with other aromatics; products of catalytic cracking or aromatization according to the processes of Specifications 552,115, 552,216, 574,963, 574,973, 575,766, 575,768 and 575,769 which contain styrene and its derivatives, and indene; and dehydrogenation products of ethylbenzene. The paraffinic solvents may be either single paraffins such as liquid propane, isopentane or heptane or petroleum fractions of sufficiently different boiling range from the hydrocarbons to be separated. The aqueous alcohols are mixtures of water with one or more alcohols capable of dissolving 5-50 per cent by weight thereof, e.g. methyl, ethyl, propyl, isopropyl, sec. and tert. butyl, ethylene chlorhydrin, ethylene glycol mono-alkyl ethers, propylene glycol, and its mono-alkyl ethers. The aromatics with conjugated unsaturated side groups concentrate in the sulphur dioxide or aqueous alcohol, and the others in the upper paraffinic layer. Repeated distribution gives complete separation. Temperatures below normal are preferable. Multiple counter-current extraction in towers may be used continuously introducing the light and heavy solvents at bottom and top respectively, and the solute intermediately. Examples describe the extraction with liquid propane and sulphur dioxide at - 50 or - 55 DEG C. of mixtures of styrene with ethylbenzene or xylol, and indene with alkylbenzenes, and the extraction with isopentane and aqueous methanol or sulphur dioxide of styrene and ethylbenzene.
机译:通过在两个不互溶或仅部分互溶的溶剂层之间的分布,将具有不饱和侧基且在芳族原子上具有双键的不饱和侧基的芳族烃与不具有侧基或饱和侧基的芳族烃的混合物分离。分别优先溶解第一类和第二类烃的溶剂,即溶剂体系中的液态二氧化硫-链烷烃或含水醇-链烷烃,然后分离各层。第一类的烃包括苯乙烯,茚,α-甲基-,对甲基-和间乙基-苯乙烯,丙烯基苯,茚的烷基衍生物和多环烃,例如乙烯基萘。第二类包括苯,萘,蒽和具有饱和侧链或饱和环状侧基的衍生物,例如甲苯,乙苯,二甲苯和氢。它们的混合物存在于煤的碳化产物中,例如,苯甲酸酯和焦油,其中130-150℃的馏分包含二甲苯,乙苯和苯乙烯,而170--190℃的馏分包含茚与其他芳族化合物;根据规范552,115、552,216、574,963、574,973、575,766、575,768和575,769(均在第IV组中)的方法进行催化裂化或芳构化的产品,均包含苯乙烯及其衍生物和茚;和乙苯的脱氢产物。链烷烃溶剂可以是单一链烷烃,例如液态丙烷,异戊烷或庚烷,或者沸程与要分离的烃有足够不同的石油馏分。水性醇是水与一种或多种能够溶解5%至50%的醇的混合物。按其重量计,例如甲基,乙基,丙基,异丙基。和叔叔。丁基,乙烯氯醇,乙二醇单烷基醚,丙二醇及其单烷基醚。具有共轭不饱和侧基的芳族化合物集中在二氧化硫或含水醇中,其他则集中在上链烷烃层中。重复分配可以完全分离。低于正常温度是优选的。可在塔中多次逆流萃取,分别在底部和顶部连续引入轻溶剂和重溶剂,并在中间引入溶质。实施例描述了在-50或-55℃下用液态丙烷和二氧化硫萃取苯乙烯与乙苯或二甲苯醇的混合物,以及茚与烷基苯的混合物,并用异戊烷和苯乙烯或乙苯的甲醇或二氧化硫水溶液萃取。 :通过在不互溶或仅部分互溶的两个溶剂层之间的分布,将具有不饱和侧基且在芳族原子上具有双键的不饱和侧基的芳族烃与不具有侧基或饱和侧基的芳族烃的混合物分离分别优先溶解第一类和第二类烃,即溶剂体系的液态二氧化硫-链烷烃或含水醇-链烷烃,然后分离各层。第一类烃包括苯乙烯,茚,α-甲基,对甲基和间乙基苯乙烯,丙烯基苯,茚的烷基衍生物和多环烃,例如乙烯基萘。第二类包括苯,萘,蒽和具有饱和侧链或饱和环状侧基的衍生物,例如甲苯,乙苯,二甲苯和氢。它们的混合物存在于煤的碳化产物中,例如苯甲酸酯和焦油,其中130-150℃的馏分包含二甲苯,乙苯和苯乙烯,而170-190℃的馏分包含茚与其他芳族化合物;根据规范552,115、552,216、574,963、574,973、575,766、575,768和575,769的方法进行催化裂化或芳构化的产物,其中含有苯乙烯及其衍生物和茚;和乙苯的脱氢产物。链烷烃溶剂可以是单一链烷烃,例如液态丙烷,异戊烷或庚烷,或者沸程与要分离的烃有足够不同的石油馏分。含水醇是水与一种或多种能够溶解其重量的5-50%的醇的混合物,例如水。甲基,乙基,丙基,异丙基。和叔叔。丁基,乙烯氯醇,乙二醇单烷基醚,丙二醇及其单烷基醚。具有共轭不饱和侧基的芳烃集中在二氧化硫或含水醇中,其他位于上链烷烃层。重复分配可以完全分离。低于正常温度是优选的。可在塔中多次逆流萃取,分别在底部和顶部连续引入轻溶剂和重溶剂,并在中间引入溶质。实施例描述了在-50或-55℃下用液体丙烷和二氧化硫萃取苯乙烯与乙苯或二甲苯醇的混合物,以及茚与烷基苯的混合物,并用异戊烷和苯乙烯或乙苯的甲醇或二氧化硫水溶液萃取。

著录项

  • 公开/公告号GB585166A

    专利类型

  • 公开/公告日1947-01-31

    原文格式PDF

  • 申请/专利权人 ERNA MANDEL;HERBERT STEINER;SYDNEY WHINCUP;

    申请/专利号GB19440011524

  • 发明设计人

    申请日1941-06-16

  • 分类号C07C7/10;

  • 国家 GB

  • 入库时间 2022-08-24 02:52:09

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