LOW-MOLECULAR POLYISOBUTYLENE PRODUCTION PROCESS
FIELD: polymer production. SUBSTANCE: invention relates to producing polyisobutylene useful as thickening additive for industrial oils and for preparing viscous lubricants, adhesives, hermetics, and other. Polymerization is carried out in solvent constituting mixture of toluene and diisobutylene at...
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creator | MURACHEV V.B BYRIKHIN V.S GOL'BERG I.P KHLUSTIKOV V.I AKSENOV V.I ZOLOTAREV V.L GOLOVINA N.A GRUNIN G.N NESMELOV A.I BOBROVSKIJ N.A RJAKHOVSKIJ V.S SAZYKIN V.V KOLOKOL'NIKOV A.S GRISHCHENKO A.I |
description | FIELD: polymer production. SUBSTANCE: invention relates to producing polyisobutylene useful as thickening additive for industrial oils and for preparing viscous lubricants, adhesives, hermetics, and other. Polymerization is carried out in solvent constituting mixture of toluene and diisobutylene at weight ratio from 20:1 to 1:20 and at temperature from 30 to +60 C by way of successively introducing isobutylene into solvent to maintain its content within the range 10 to 60 wt % and titanium tetrachloride to its content 0.05 to 1.0 mol per 100 kg of monomer, after which reaction mixture is aged for at least 2 min and then supplemented by triisobutylaluminum. The latter is added in a mixture containing 3 to 50 mol % diisobutylaluminum hydride and/or 5 to 25 mol % tetraisobutylalumoxan. Titanium to aluminum molar ratio ranges from 0.5 to 100. Process enables producing low-molecular polyisobutylene with narrow molecular-mass distribution requiring reduced commercial catalytic system components intakes. Yield of polymer is quantitative and molecular mass of polymer is controllable within wide limits. EFFECT: enhanced process efficiency. 1 tble |
format | Patent |
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SUBSTANCE: invention relates to producing polyisobutylene useful as thickening additive for industrial oils and for preparing viscous lubricants, adhesives, hermetics, and other. Polymerization is carried out in solvent constituting mixture of toluene and diisobutylene at weight ratio from 20:1 to 1:20 and at temperature from 30 to +60 C by way of successively introducing isobutylene into solvent to maintain its content within the range 10 to 60 wt % and titanium tetrachloride to its content 0.05 to 1.0 mol per 100 kg of monomer, after which reaction mixture is aged for at least 2 min and then supplemented by triisobutylaluminum. The latter is added in a mixture containing 3 to 50 mol % diisobutylaluminum hydride and/or 5 to 25 mol % tetraisobutylalumoxan. Titanium to aluminum molar ratio ranges from 0.5 to 100. Process enables producing low-molecular polyisobutylene with narrow molecular-mass distribution requiring reduced commercial catalytic system components intakes. Yield of polymer is quantitative and molecular mass of polymer is controllable within wide limits. EFFECT: enhanced process efficiency. 1 tble</description><edition>6</edition><language>eng</language><subject>CHEMISTRY ; COMPOSITIONS BASED THEREON ; MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVINGCARBON-TO-CARBON UNSATURATED BONDS ; METALLURGY ; ORGANIC MACROMOLECULAR COMPOUNDS ; THEIR PREPARATION OR CHEMICAL WORKING-UP</subject><creationdate>1998</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=19980427&DB=EPODOC&CC=RU&NR=2109754C1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19980427&DB=EPODOC&CC=RU&NR=2109754C1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>MURACHEV V.B</creatorcontrib><creatorcontrib>BYRIKHIN V.S</creatorcontrib><creatorcontrib>GOL'BERG I.P</creatorcontrib><creatorcontrib>KHLUSTIKOV V.I</creatorcontrib><creatorcontrib>AKSENOV V.I</creatorcontrib><creatorcontrib>ZOLOTAREV V.L</creatorcontrib><creatorcontrib>GOLOVINA N.A</creatorcontrib><creatorcontrib>GRUNIN G.N</creatorcontrib><creatorcontrib>NESMELOV A.I</creatorcontrib><creatorcontrib>BOBROVSKIJ N.A</creatorcontrib><creatorcontrib>RJAKHOVSKIJ V.S</creatorcontrib><creatorcontrib>SAZYKIN V.V</creatorcontrib><creatorcontrib>KOLOKOL'NIKOV A.S</creatorcontrib><creatorcontrib>GRISHCHENKO A.I</creatorcontrib><title>LOW-MOLECULAR POLYISOBUTYLENE PRODUCTION PROCESS</title><description>FIELD: polymer production. SUBSTANCE: invention relates to producing polyisobutylene useful as thickening additive for industrial oils and for preparing viscous lubricants, adhesives, hermetics, and other. Polymerization is carried out in solvent constituting mixture of toluene and diisobutylene at weight ratio from 20:1 to 1:20 and at temperature from 30 to +60 C by way of successively introducing isobutylene into solvent to maintain its content within the range 10 to 60 wt % and titanium tetrachloride to its content 0.05 to 1.0 mol per 100 kg of monomer, after which reaction mixture is aged for at least 2 min and then supplemented by triisobutylaluminum. The latter is added in a mixture containing 3 to 50 mol % diisobutylaluminum hydride and/or 5 to 25 mol % tetraisobutylalumoxan. Titanium to aluminum molar ratio ranges from 0.5 to 100. Process enables producing low-molecular polyisobutylene with narrow molecular-mass distribution requiring reduced commercial catalytic system components intakes. Yield of polymer is quantitative and molecular mass of polymer is controllable within wide limits. EFFECT: enhanced process efficiency. 1 tble</description><subject>CHEMISTRY</subject><subject>COMPOSITIONS BASED THEREON</subject><subject>MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVINGCARBON-TO-CARBON UNSATURATED BONDS</subject><subject>METALLURGY</subject><subject>ORGANIC MACROMOLECULAR COMPOUNDS</subject><subject>THEIR PREPARATION OR CHEMICAL WORKING-UP</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1998</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDDw8Q_X9fX3cXUO9XEMUgjw94n0DPZ3Cg2J9HH1c1UICPJ3CXUO8fT3AzGdXYODeRhY0xJzilN5oTQ3g4Kba4izh25qQX58anFBYnJqXmpJfFCokaGBpbmpibOhMRFKADWwJr8</recordid><startdate>19980427</startdate><enddate>19980427</enddate><creator>MURACHEV V.B</creator><creator>BYRIKHIN V.S</creator><creator>GOL'BERG I.P</creator><creator>KHLUSTIKOV V.I</creator><creator>AKSENOV V.I</creator><creator>ZOLOTAREV V.L</creator><creator>GOLOVINA N.A</creator><creator>GRUNIN G.N</creator><creator>NESMELOV A.I</creator><creator>BOBROVSKIJ N.A</creator><creator>RJAKHOVSKIJ V.S</creator><creator>SAZYKIN V.V</creator><creator>KOLOKOL'NIKOV A.S</creator><creator>GRISHCHENKO A.I</creator><scope>EVB</scope></search><sort><creationdate>19980427</creationdate><title>LOW-MOLECULAR POLYISOBUTYLENE PRODUCTION PROCESS</title><author>MURACHEV V.B ; BYRIKHIN V.S ; GOL'BERG I.P ; KHLUSTIKOV V.I ; AKSENOV V.I ; ZOLOTAREV V.L ; GOLOVINA N.A ; GRUNIN G.N ; NESMELOV A.I ; BOBROVSKIJ N.A ; RJAKHOVSKIJ V.S ; SAZYKIN V.V ; KOLOKOL'NIKOV A.S ; GRISHCHENKO A.I</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_RU2109754C13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1998</creationdate><topic>CHEMISTRY</topic><topic>COMPOSITIONS BASED THEREON</topic><topic>MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVINGCARBON-TO-CARBON UNSATURATED BONDS</topic><topic>METALLURGY</topic><topic>ORGANIC MACROMOLECULAR COMPOUNDS</topic><topic>THEIR PREPARATION OR CHEMICAL WORKING-UP</topic><toplevel>online_resources</toplevel><creatorcontrib>MURACHEV V.B</creatorcontrib><creatorcontrib>BYRIKHIN V.S</creatorcontrib><creatorcontrib>GOL'BERG I.P</creatorcontrib><creatorcontrib>KHLUSTIKOV V.I</creatorcontrib><creatorcontrib>AKSENOV V.I</creatorcontrib><creatorcontrib>ZOLOTAREV V.L</creatorcontrib><creatorcontrib>GOLOVINA N.A</creatorcontrib><creatorcontrib>GRUNIN G.N</creatorcontrib><creatorcontrib>NESMELOV A.I</creatorcontrib><creatorcontrib>BOBROVSKIJ N.A</creatorcontrib><creatorcontrib>RJAKHOVSKIJ V.S</creatorcontrib><creatorcontrib>SAZYKIN V.V</creatorcontrib><creatorcontrib>KOLOKOL'NIKOV A.S</creatorcontrib><creatorcontrib>GRISHCHENKO A.I</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>MURACHEV V.B</au><au>BYRIKHIN V.S</au><au>GOL'BERG I.P</au><au>KHLUSTIKOV V.I</au><au>AKSENOV V.I</au><au>ZOLOTAREV V.L</au><au>GOLOVINA N.A</au><au>GRUNIN G.N</au><au>NESMELOV A.I</au><au>BOBROVSKIJ N.A</au><au>RJAKHOVSKIJ V.S</au><au>SAZYKIN V.V</au><au>KOLOKOL'NIKOV A.S</au><au>GRISHCHENKO A.I</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>LOW-MOLECULAR POLYISOBUTYLENE PRODUCTION PROCESS</title><date>1998-04-27</date><risdate>1998</risdate><abstract>FIELD: polymer production. SUBSTANCE: invention relates to producing polyisobutylene useful as thickening additive for industrial oils and for preparing viscous lubricants, adhesives, hermetics, and other. Polymerization is carried out in solvent constituting mixture of toluene and diisobutylene at weight ratio from 20:1 to 1:20 and at temperature from 30 to +60 C by way of successively introducing isobutylene into solvent to maintain its content within the range 10 to 60 wt % and titanium tetrachloride to its content 0.05 to 1.0 mol per 100 kg of monomer, after which reaction mixture is aged for at least 2 min and then supplemented by triisobutylaluminum. The latter is added in a mixture containing 3 to 50 mol % diisobutylaluminum hydride and/or 5 to 25 mol % tetraisobutylalumoxan. Titanium to aluminum molar ratio ranges from 0.5 to 100. Process enables producing low-molecular polyisobutylene with narrow molecular-mass distribution requiring reduced commercial catalytic system components intakes. Yield of polymer is quantitative and molecular mass of polymer is controllable within wide limits. EFFECT: enhanced process efficiency. 1 tble</abstract><edition>6</edition><oa>free_for_read</oa></addata></record> |
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subjects | CHEMISTRY COMPOSITIONS BASED THEREON MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVINGCARBON-TO-CARBON UNSATURATED BONDS METALLURGY ORGANIC MACROMOLECULAR COMPOUNDS THEIR PREPARATION OR CHEMICAL WORKING-UP |
title | LOW-MOLECULAR POLYISOBUTYLENE PRODUCTION PROCESS |
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