LIGHT-COLORED, HIGH SOFTENING POINT HYDROCARBON RESINS AND METHOD FOR THEIR PREPARATION
1345619 Petroleum resins EASTMAN KODAK CO 26 Aug 1971 [27 Aug 1970] 40114/71 Heading C3P Light coloured, high softening point resins are prepared by polymerizing debutanized aromatic concentrate-B with aluminium chloride as catalyst in a two-stage reaction at 50 to 100 C. for 6 to 10 hours in the...
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creator | HOGAN, HAROLD E HAGEMEYER, HUGH J. (JR.) JOHNSON, SAM H. (JR.) |
description | 1345619 Petroleum resins EASTMAN KODAK CO 26 Aug 1971 [27 Aug 1970] 40114/71 Heading C3P Light coloured, high softening point resins are prepared by polymerizing debutanized aromatic concentrate-B with aluminium chloride as catalyst in a two-stage reaction at 50 to 100 C. for 6 to 10 hours in the first stage and at 125 to 150 C. for 6 to 10 hours in the second stage, to obtain a solution of crude resin, removing chlorides from the solution by methanol extraction or high temperature lime treatment followed by hydrogenation at 100 to 1000 psig. and/or alumina treatment, followed by hydrogenation at 3000 to 6000 psig. and above 300 C. to remove colour and reduce unsaturation, and thereafter stripping the resin solution to obtain the hydrocarbon resin. The methanol extraction may be effected at 40 to 65C. or the lime treatment at 230 to 250 C. The low pressure hydrogenation may be effected at 260 to 280 C. in the presence of supported nickel catalyst or at 290 to 310 C. in the presence of a palladium or alumina catalyst. The high pressure hydrogenation may be effected at 315 to 325 C. over a nickel catalyst. Apparatus for conducting the process continuously is described and illustrated. |
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(JR.)</creatorcontrib><description>1345619 Petroleum resins EASTMAN KODAK CO 26 Aug 1971 [27 Aug 1970] 40114/71 Heading C3P Light coloured, high softening point resins are prepared by polymerizing debutanized aromatic concentrate-B with aluminium chloride as catalyst in a two-stage reaction at 50 to 100 C. for 6 to 10 hours in the first stage and at 125 to 150 C. for 6 to 10 hours in the second stage, to obtain a solution of crude resin, removing chlorides from the solution by methanol extraction or high temperature lime treatment followed by hydrogenation at 100 to 1000 psig. and/or alumina treatment, followed by hydrogenation at 3000 to 6000 psig. and above 300 C. to remove colour and reduce unsaturation, and thereafter stripping the resin solution to obtain the hydrocarbon resin. The methanol extraction may be effected at 40 to 65C. or the lime treatment at 230 to 250 C. The low pressure hydrogenation may be effected at 260 to 280 C. in the presence of supported nickel catalyst or at 290 to 310 C. in the presence of a palladium or alumina catalyst. The high pressure hydrogenation may be effected at 315 to 325 C. over a nickel catalyst. 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The methanol extraction may be effected at 40 to 65C. or the lime treatment at 230 to 250 C. The low pressure hydrogenation may be effected at 260 to 280 C. in the presence of supported nickel catalyst or at 290 to 310 C. in the presence of a palladium or alumina catalyst. The high pressure hydrogenation may be effected at 315 to 325 C. over a nickel catalyst. Apparatus for conducting the process continuously is described and illustrated.</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>1975</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqFyrEKwjAQgOEuDqK-gtwDWAgogmNMLk2g3oXrQXEqReIkWqjvjw7uTj8f_Muqb1MTtXbcsqDfQfwSOg6KlKiBzIkU4tULOytnJhDsEnVgycMFNbKHwAIaMQlkwWzFamJaV4v7-JjL5tdVtQ2oLtZleg1lnsZbeZb34OzpeDDG2P3f4QOhGS-f</recordid><startdate>19750304</startdate><enddate>19750304</enddate><creator>HOGAN, HAROLD E</creator><creator>HAGEMEYER, HUGH J. (JR.)</creator><creator>JOHNSON, SAM H. 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(JR.)</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>LIGHT-COLORED, HIGH SOFTENING POINT HYDROCARBON RESINS AND METHOD FOR THEIR PREPARATION</title><date>1975-03-04</date><risdate>1975</risdate><abstract>1345619 Petroleum resins EASTMAN KODAK CO 26 Aug 1971 [27 Aug 1970] 40114/71 Heading C3P Light coloured, high softening point resins are prepared by polymerizing debutanized aromatic concentrate-B with aluminium chloride as catalyst in a two-stage reaction at 50 to 100 C. for 6 to 10 hours in the first stage and at 125 to 150 C. for 6 to 10 hours in the second stage, to obtain a solution of crude resin, removing chlorides from the solution by methanol extraction or high temperature lime treatment followed by hydrogenation at 100 to 1000 psig. and/or alumina treatment, followed by hydrogenation at 3000 to 6000 psig. and above 300 C. to remove colour and reduce unsaturation, and thereafter stripping the resin solution to obtain the hydrocarbon resin. The methanol extraction may be effected at 40 to 65C. or the lime treatment at 230 to 250 C. The low pressure hydrogenation may be effected at 260 to 280 C. in the presence of supported nickel catalyst or at 290 to 310 C. in the presence of a palladium or alumina catalyst. The high pressure hydrogenation may be effected at 315 to 325 C. over a nickel catalyst. Apparatus for conducting the process continuously is described and illustrated.</abstract><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 | LIGHT-COLORED, HIGH SOFTENING POINT HYDROCARBON RESINS AND METHOD FOR THEIR PREPARATION |
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