Process for the separation of diethylbenzene in carbon deka-aromatic hydrocarbons
The invention relates to a method for utilizing an extractive distillation process to separate diethyl benzene from C10 arene, comprising: firstly, mixed components of meta-diethyl benzene in C10 arene and other high boiling point components are separated off, with a rectification temperature of bet...
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creator | LIU JIAN CHEN JIMIN HUANG FENSHENG DU JIANWEI ZHANG WEIXING |
description | The invention relates to a method for utilizing an extractive distillation process to separate diethyl benzene from C10 arene, comprising: firstly, mixed components of meta-diethyl benzene in C10 arene and other high boiling point components are separated off, with a rectification temperature of between 176 and 182DEG C; then an extractant is added in a meta-diethyl benzene mixture for separating out m-diethyl benzene, wherein, the extractant is dimethyl phthalate, dibutyl phthalate or a mixture thereof; and the extractant and the mixed components of meta-diethyl benzene have a feeding weight ratio of 5 to 20:1, the charging temperature of the extractant is between 120 and 190 DEG C, and the separation temperature is 160 to 190 DEG C; and finally the extractant and the p-diethyl benzene are separated for recovering the extractant through distillation separation; and the method has advantages of simple process, stable operation, low energy consumption, high purity of separated products, good separation effect |
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then an extractant is added in a meta-diethyl benzene mixture for separating out m-diethyl benzene, wherein, the extractant is dimethyl phthalate, dibutyl phthalate or a mixture thereof; and the extractant and the mixed components of meta-diethyl benzene have a feeding weight ratio of 5 to 20:1, the charging temperature of the extractant is between 120 and 190 DEG C, and the separation temperature is 160 to 190 DEG C; and finally the extractant and the p-diethyl benzene are separated for recovering the extractant through distillation separation; and the method has advantages of simple process, stable operation, low energy consumption, high purity of separated products, good separation effect</description><language>chi ; eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY</subject><creationdate>2009</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20090114&DB=EPODOC&CC=CN&NR=101343207A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20090114&DB=EPODOC&CC=CN&NR=101343207A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>LIU JIAN</creatorcontrib><creatorcontrib>CHEN JIMIN</creatorcontrib><creatorcontrib>HUANG FENSHENG</creatorcontrib><creatorcontrib>DU JIANWEI</creatorcontrib><creatorcontrib>ZHANG WEIXING</creatorcontrib><title>Process for the separation of diethylbenzene in carbon deka-aromatic hydrocarbons</title><description>The invention relates to a method for utilizing an extractive distillation process to separate diethyl benzene from C10 arene, comprising: firstly, mixed components of meta-diethyl benzene in C10 arene and other high boiling point components are separated off, with a rectification temperature of between 176 and 182DEG C; 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then an extractant is added in a meta-diethyl benzene mixture for separating out m-diethyl benzene, wherein, the extractant is dimethyl phthalate, dibutyl phthalate or a mixture thereof; and the extractant and the mixed components of meta-diethyl benzene have a feeding weight ratio of 5 to 20:1, the charging temperature of the extractant is between 120 and 190 DEG C, and the separation temperature is 160 to 190 DEG C; and finally the extractant and the p-diethyl benzene are separated for recovering the extractant through distillation separation; and the method has advantages of simple process, stable operation, low energy consumption, high purity of separated products, good separation effect</abstract><oa>free_for_read</oa></addata></record> |
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subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS CHEMISTRY METALLURGY ORGANIC CHEMISTRY |
title | Process for the separation of diethylbenzene in carbon deka-aromatic hydrocarbons |
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