Polyester polyols continuous production unit
The utility model discloses a polyester polyols continuous production unit. The device includes thick liquids allotment jar, slurry transferring jar, esterifying kettle, polycondensation falling -film tower, the condensing tower is established at the esterifying kettle top, polycondensation falling...
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creator | LI HONGBIN WU BAOZHAI WANG SHAOPENG HAO XINGWU WANG XINLIANG GAN SHENGHUA |
description | The utility model discloses a polyester polyols continuous production unit. The device includes thick liquids allotment jar, slurry transferring jar, esterifying kettle, polycondensation falling -film tower, the condensing tower is established at the esterifying kettle top, polycondensation falling -film tower and vacuum gas lift union coupling. The raw materials polyhydric alcohol carries out continuous production with binary acid or acid anhydride through above -mentioned continuous production unit and obtains the polyester polyols product, and this production technology is including stage of esterifying and polycondensation stage, the stage of esterifying: directly heat up to 200 from the room temperature 245 DEG C, add the catalyst, constant temperature 0.5 get into the polycondensation stage after 1.5h, the polycondensation stage: with the vacuum primary governor control to getting together required vacuum 1000 5000Pa, the polymerization 1.5 2.5h. The utility model discloses a continuous production unit |
format | Patent |
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The device includes thick liquids allotment jar, slurry transferring jar, esterifying kettle, polycondensation falling -film tower, the condensing tower is established at the esterifying kettle top, polycondensation falling -film tower and vacuum gas lift union coupling. The raw materials polyhydric alcohol carries out continuous production with binary acid or acid anhydride through above -mentioned continuous production unit and obtains the polyester polyols product, and this production technology is including stage of esterifying and polycondensation stage, the stage of esterifying: directly heat up to 200 from the room temperature 245 DEG C, add the catalyst, constant temperature 0.5 get into the polycondensation stage after 1.5h, the polycondensation stage: with the vacuum primary governor control to getting together required vacuum 1000 5000Pa, the polymerization 1.5 2.5h. 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The device includes thick liquids allotment jar, slurry transferring jar, esterifying kettle, polycondensation falling -film tower, the condensing tower is established at the esterifying kettle top, polycondensation falling -film tower and vacuum gas lift union coupling. The raw materials polyhydric alcohol carries out continuous production with binary acid or acid anhydride through above -mentioned continuous production unit and obtains the polyester polyols product, and this production technology is including stage of esterifying and polycondensation stage, the stage of esterifying: directly heat up to 200 from the room temperature 245 DEG C, add the catalyst, constant temperature 0.5 get into the polycondensation stage after 1.5h, the polycondensation stage: with the vacuum primary governor control to getting together required vacuum 1000 5000Pa, the polymerization 1.5 2.5h. The utility model discloses a continuous production unit</description><subject>CHEMISTRY</subject><subject>COMPOSITIONS BASED THEREON</subject><subject>MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONSONLY INVOLVING UNSATURATED CARBON-TO-CARBON 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>2017</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZNAJyM-pTC0uSS1SKACy8nOKFZLz80oy80rzS4sVCoryU0qTSzLz8xRK8zJLeBhY0xJzilN5oTQ3g5Kba4izh25qQX58anFBYnJqXmpJvLOfkYGZsbG5kYFJaKgxUYoAYFsrlA</recordid><startdate>20170718</startdate><enddate>20170718</enddate><creator>LI HONGBIN</creator><creator>WU BAOZHAI</creator><creator>WANG SHAOPENG</creator><creator>HAO XINGWU</creator><creator>WANG XINLIANG</creator><creator>GAN SHENGHUA</creator><scope>EVB</scope></search><sort><creationdate>20170718</creationdate><title>Polyester polyols continuous production unit</title><author>LI HONGBIN ; WU BAOZHAI ; WANG SHAOPENG ; HAO XINGWU ; WANG XINLIANG ; GAN SHENGHUA</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN206337204UU3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>chi ; eng</language><creationdate>2017</creationdate><topic>CHEMISTRY</topic><topic>COMPOSITIONS BASED THEREON</topic><topic>MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONSONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS</topic><topic>METALLURGY</topic><topic>ORGANIC MACROMOLECULAR COMPOUNDS</topic><topic>THEIR PREPARATION OR CHEMICAL WORKING-UP</topic><toplevel>online_resources</toplevel><creatorcontrib>LI HONGBIN</creatorcontrib><creatorcontrib>WU BAOZHAI</creatorcontrib><creatorcontrib>WANG SHAOPENG</creatorcontrib><creatorcontrib>HAO XINGWU</creatorcontrib><creatorcontrib>WANG XINLIANG</creatorcontrib><creatorcontrib>GAN SHENGHUA</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>LI HONGBIN</au><au>WU BAOZHAI</au><au>WANG SHAOPENG</au><au>HAO XINGWU</au><au>WANG XINLIANG</au><au>GAN SHENGHUA</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Polyester polyols continuous production unit</title><date>2017-07-18</date><risdate>2017</risdate><abstract>The utility model discloses a polyester polyols continuous production unit. The device includes thick liquids allotment jar, slurry transferring jar, esterifying kettle, polycondensation falling -film tower, the condensing tower is established at the esterifying kettle top, polycondensation falling -film tower and vacuum gas lift union coupling. The raw materials polyhydric alcohol carries out continuous production with binary acid or acid anhydride through above -mentioned continuous production unit and obtains the polyester polyols product, and this production technology is including stage of esterifying and polycondensation stage, the stage of esterifying: directly heat up to 200 from the room temperature 245 DEG C, add the catalyst, constant temperature 0.5 get into the polycondensation stage after 1.5h, the polycondensation stage: with the vacuum primary governor control to getting together required vacuum 1000 5000Pa, the polymerization 1.5 2.5h. The utility model discloses a continuous production unit</abstract><oa>free_for_read</oa></addata></record> |
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subjects | CHEMISTRY COMPOSITIONS BASED THEREON MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONSONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS METALLURGY ORGANIC MACROMOLECULAR COMPOUNDS THEIR PREPARATION OR CHEMICAL WORKING-UP |
title | Polyester polyols continuous production unit |
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