Method for producing cyclohexane by using starting materials originating from a steam cracking process

The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting mat...

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Hauptverfasser: JONI JONI, TSCHIRSCHWITZ STEFFEN, PFEIFFER DANIEL, DEUERLEIN STEPHAN, WISSEL-STOLL KATHRIN, BURKLE JOCHEN, KOSTOVA ALBENA, SCHMITT MARKUS, KINDLER ALOIS, SPUHL KATHARINA, BITTERLICH STEFAN, SCHREIBER MICHAEL, WLOKA VERONIKA, OEHLENSCHLAGER STEFFEN, BOSCH MARCO, PROCHAZKA ROMAN, MALKOWSKY DANIELA, AVERLANT GAUTHIER LUC MAURICE, BOCK MARTIN
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creator JONI JONI
TSCHIRSCHWITZ STEFFEN
PFEIFFER DANIEL
DEUERLEIN STEPHAN
WISSEL-STOLL KATHRIN
BURKLE JOCHEN
KOSTOVA ALBENA
SCHMITT MARKUS
KINDLER ALOIS
SPUHL KATHARINA
BITTERLICH STEFAN
SCHREIBER MICHAEL
WLOKA VERONIKA
OEHLENSCHLAGER STEFFEN
BOSCH MARCO
PROCHAZKA ROMAN
MALKOWSKY DANIELA
AVERLANT GAUTHIER LUC MAURICE
BOCK MARTIN
description The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.
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The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.</description><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY</subject><creationdate>2015</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&amp;date=20150624&amp;DB=EPODOC&amp;CC=CN&amp;NR=104736502A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,309,781,886,25569,76552</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20150624&amp;DB=EPODOC&amp;CC=CN&amp;NR=104736502A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>JONI JONI</creatorcontrib><creatorcontrib>TSCHIRSCHWITZ STEFFEN</creatorcontrib><creatorcontrib>PFEIFFER DANIEL</creatorcontrib><creatorcontrib>DEUERLEIN STEPHAN</creatorcontrib><creatorcontrib>WISSEL-STOLL KATHRIN</creatorcontrib><creatorcontrib>BURKLE JOCHEN</creatorcontrib><creatorcontrib>KOSTOVA ALBENA</creatorcontrib><creatorcontrib>SCHMITT MARKUS</creatorcontrib><creatorcontrib>KINDLER ALOIS</creatorcontrib><creatorcontrib>SPUHL KATHARINA</creatorcontrib><creatorcontrib>BITTERLICH STEFAN</creatorcontrib><creatorcontrib>SCHREIBER MICHAEL</creatorcontrib><creatorcontrib>WLOKA VERONIKA</creatorcontrib><creatorcontrib>OEHLENSCHLAGER STEFFEN</creatorcontrib><creatorcontrib>BOSCH MARCO</creatorcontrib><creatorcontrib>PROCHAZKA ROMAN</creatorcontrib><creatorcontrib>MALKOWSKY DANIELA</creatorcontrib><creatorcontrib>AVERLANT GAUTHIER LUC MAURICE</creatorcontrib><creatorcontrib>BOCK MARTIN</creatorcontrib><title>Method for producing cyclohexane by using starting materials originating from a steam cracking process</title><description>The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. 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The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.</abstract><oa>free_for_read</oa></addata></record>
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subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMISTRY
METALLURGY
ORGANIC CHEMISTRY
title Method for producing cyclohexane by using starting materials originating from a steam cracking process
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