Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen
Production of thermoplastic polyurethane elastomers (TPU) involves (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) (molecular weight (Mw) 500-5000) with (b) organic diisocyanate in isocyanate (NCO)-reactive/NCO group equivalent ratio of (1.1-5.0):1 in mixing aggregate with high shear energy...
Gespeichert in:
Hauptverfasser: | , , |
---|---|
Format: | Patent |
Sprache: | ger |
Schlagworte: | |
Online-Zugang: | Volltext bestellen |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | |
---|---|
container_issue | |
container_start_page | |
container_title | |
container_volume | |
creator | BRAEUER, WOLFGANG KAUOLD, WOLFGANG HEIDINGSFELD, HERBERT |
description | Production of thermoplastic polyurethane elastomers (TPU) involves (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) (molecular weight (Mw) 500-5000) with (b) organic diisocyanate in isocyanate (NCO)-reactive/NCO group equivalent ratio of (1.1-5.0):1 in mixing aggregate with high shear energy; (B) over 90% conversion to OH-terminated prepolymer (I) by reaction at over 80[deg]C; (C) mixing (I) with (c) chain extender(s) (Mw 60-490); (D) conversion to TPU by reaction with (b) to adjust overall equivalent ratio of NCO/NCO-reactive groups to (0.9-1.1):1. Production of thermoplastic polyurethane elastomers (TPU) with improved processability uses a multistage reaction comprising (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) of weight average molecular weight 500-5000 with (b) an organic diisocyanate in an equivalent ratio of isocyanate (NCO)-reactive groups to NCO groups of (1.1-5.0):1 in a mixing aggregate with high shear energy; (B) reacting the resultant mixture at temperatures above 80[deg]C to over 90% conversion with respect to (b), to a OH-terminated prepolymer (I); (C) mixing (I) with (c) chain extender(s) of molecular weight 60-490; (D) conversion to the TPU by reacting the mixture with component (b) in such an amount that the overall equivalent ratio of NCO/NCO-reactive groups is adjusted to (0.9-1.1):1. Stages (A) to (D) may take place in the presence of catalyst and with addition of 0-20 wt.% ancillaries and additives with respect to the total amount of TPU. An independent claim is included for use of the TPU for producing injection molded and extruded articles. |
format | Patent |
fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_DE102005039933B4</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>DE102005039933B4</sourcerecordid><originalsourceid>FETCH-epo_espacenet_DE102005039933B43</originalsourceid><addsrcrecordid>eNqNy7EKwjAURuEuDqK-QxZHIRoduqqV4uQgruW2_G0K8SbcJAV9ehF8AKezfGdeXB-QnqyA1TuLqiExwbnMg5o8q2QhTx8cxTTGzqoJQtJiTC19l5t3ryxIlhi8LGY9uYjVr4tifanup3qD4BvEQB0YqTlXW73T-qBNWRpz3Jt_3Qdq6Dfv</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen</title><source>esp@cenet</source><creator>BRAEUER, WOLFGANG ; KAUOLD, WOLFGANG ; HEIDINGSFELD, HERBERT</creator><creatorcontrib>BRAEUER, WOLFGANG ; KAUOLD, WOLFGANG ; HEIDINGSFELD, HERBERT</creatorcontrib><description>Production of thermoplastic polyurethane elastomers (TPU) involves (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) (molecular weight (Mw) 500-5000) with (b) organic diisocyanate in isocyanate (NCO)-reactive/NCO group equivalent ratio of (1.1-5.0):1 in mixing aggregate with high shear energy; (B) over 90% conversion to OH-terminated prepolymer (I) by reaction at over 80[deg]C; (C) mixing (I) with (c) chain extender(s) (Mw 60-490); (D) conversion to TPU by reaction with (b) to adjust overall equivalent ratio of NCO/NCO-reactive groups to (0.9-1.1):1. Production of thermoplastic polyurethane elastomers (TPU) with improved processability uses a multistage reaction comprising (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) of weight average molecular weight 500-5000 with (b) an organic diisocyanate in an equivalent ratio of isocyanate (NCO)-reactive groups to NCO groups of (1.1-5.0):1 in a mixing aggregate with high shear energy; (B) reacting the resultant mixture at temperatures above 80[deg]C to over 90% conversion with respect to (b), to a OH-terminated prepolymer (I); (C) mixing (I) with (c) chain extender(s) of molecular weight 60-490; (D) conversion to the TPU by reacting the mixture with component (b) in such an amount that the overall equivalent ratio of NCO/NCO-reactive groups is adjusted to (0.9-1.1):1. Stages (A) to (D) may take place in the presence of catalyst and with addition of 0-20 wt.% ancillaries and additives with respect to the total amount of TPU. An independent claim is included for use of the TPU for producing injection molded and extruded articles.</description><language>ger</language><subject>AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F,C08G ; CHEMISTRY ; COMPOSITIONS BASED THEREON ; COMPOSITIONS OF MACROMOLECULAR COMPOUNDS ; GENERAL PROCESSES OF COMPOUNDING ; MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONSONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS ; METALLURGY ; ORGANIC MACROMOLECULAR COMPOUNDS ; THEIR PREPARATION OR CHEMICAL WORKING-UP ; WORKING-UP</subject><creationdate>2007</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=20071227&DB=EPODOC&CC=DE&NR=102005039933B4$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,777,882,25545,76296</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20071227&DB=EPODOC&CC=DE&NR=102005039933B4$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>BRAEUER, WOLFGANG</creatorcontrib><creatorcontrib>KAUOLD, WOLFGANG</creatorcontrib><creatorcontrib>HEIDINGSFELD, HERBERT</creatorcontrib><title>Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen</title><description>Production of thermoplastic polyurethane elastomers (TPU) involves (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) (molecular weight (Mw) 500-5000) with (b) organic diisocyanate in isocyanate (NCO)-reactive/NCO group equivalent ratio of (1.1-5.0):1 in mixing aggregate with high shear energy; (B) over 90% conversion to OH-terminated prepolymer (I) by reaction at over 80[deg]C; (C) mixing (I) with (c) chain extender(s) (Mw 60-490); (D) conversion to TPU by reaction with (b) to adjust overall equivalent ratio of NCO/NCO-reactive groups to (0.9-1.1):1. Production of thermoplastic polyurethane elastomers (TPU) with improved processability uses a multistage reaction comprising (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) of weight average molecular weight 500-5000 with (b) an organic diisocyanate in an equivalent ratio of isocyanate (NCO)-reactive groups to NCO groups of (1.1-5.0):1 in a mixing aggregate with high shear energy; (B) reacting the resultant mixture at temperatures above 80[deg]C to over 90% conversion with respect to (b), to a OH-terminated prepolymer (I); (C) mixing (I) with (c) chain extender(s) of molecular weight 60-490; (D) conversion to the TPU by reacting the mixture with component (b) in such an amount that the overall equivalent ratio of NCO/NCO-reactive groups is adjusted to (0.9-1.1):1. Stages (A) to (D) may take place in the presence of catalyst and with addition of 0-20 wt.% ancillaries and additives with respect to the total amount of TPU. An independent claim is included for use of the TPU for producing injection molded and extruded articles.</description><subject>AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F,C08G</subject><subject>CHEMISTRY</subject><subject>COMPOSITIONS BASED THEREON</subject><subject>COMPOSITIONS OF MACROMOLECULAR COMPOUNDS</subject><subject>GENERAL PROCESSES OF COMPOUNDING</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><subject>WORKING-UP</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2007</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNy7EKwjAURuEuDqK-QxZHIRoduqqV4uQgruW2_G0K8SbcJAV9ehF8AKezfGdeXB-QnqyA1TuLqiExwbnMg5o8q2QhTx8cxTTGzqoJQtJiTC19l5t3ryxIlhi8LGY9uYjVr4tifanup3qD4BvEQB0YqTlXW73T-qBNWRpz3Jt_3Qdq6Dfv</recordid><startdate>20071227</startdate><enddate>20071227</enddate><creator>BRAEUER, WOLFGANG</creator><creator>KAUOLD, WOLFGANG</creator><creator>HEIDINGSFELD, HERBERT</creator><scope>EVB</scope></search><sort><creationdate>20071227</creationdate><title>Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen</title><author>BRAEUER, WOLFGANG ; KAUOLD, WOLFGANG ; HEIDINGSFELD, HERBERT</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_DE102005039933B43</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>ger</language><creationdate>2007</creationdate><topic>AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F,C08G</topic><topic>CHEMISTRY</topic><topic>COMPOSITIONS BASED THEREON</topic><topic>COMPOSITIONS OF MACROMOLECULAR COMPOUNDS</topic><topic>GENERAL PROCESSES OF COMPOUNDING</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><topic>WORKING-UP</topic><toplevel>online_resources</toplevel><creatorcontrib>BRAEUER, WOLFGANG</creatorcontrib><creatorcontrib>KAUOLD, WOLFGANG</creatorcontrib><creatorcontrib>HEIDINGSFELD, HERBERT</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>BRAEUER, WOLFGANG</au><au>KAUOLD, WOLFGANG</au><au>HEIDINGSFELD, HERBERT</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen</title><date>2007-12-27</date><risdate>2007</risdate><abstract>Production of thermoplastic polyurethane elastomers (TPU) involves (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) (molecular weight (Mw) 500-5000) with (b) organic diisocyanate in isocyanate (NCO)-reactive/NCO group equivalent ratio of (1.1-5.0):1 in mixing aggregate with high shear energy; (B) over 90% conversion to OH-terminated prepolymer (I) by reaction at over 80[deg]C; (C) mixing (I) with (c) chain extender(s) (Mw 60-490); (D) conversion to TPU by reaction with (b) to adjust overall equivalent ratio of NCO/NCO-reactive groups to (0.9-1.1):1. Production of thermoplastic polyurethane elastomers (TPU) with improved processability uses a multistage reaction comprising (A) mixing (a) linear hydroxyl (OH)-terminated polyol(s) of weight average molecular weight 500-5000 with (b) an organic diisocyanate in an equivalent ratio of isocyanate (NCO)-reactive groups to NCO groups of (1.1-5.0):1 in a mixing aggregate with high shear energy; (B) reacting the resultant mixture at temperatures above 80[deg]C to over 90% conversion with respect to (b), to a OH-terminated prepolymer (I); (C) mixing (I) with (c) chain extender(s) of molecular weight 60-490; (D) conversion to the TPU by reacting the mixture with component (b) in such an amount that the overall equivalent ratio of NCO/NCO-reactive groups is adjusted to (0.9-1.1):1. Stages (A) to (D) may take place in the presence of catalyst and with addition of 0-20 wt.% ancillaries and additives with respect to the total amount of TPU. An independent claim is included for use of the TPU for producing injection molded and extruded articles.</abstract><oa>free_for_read</oa></addata></record> |
fulltext | fulltext_linktorsrc |
identifier | |
ispartof | |
issn | |
language | ger |
recordid | cdi_epo_espacenet_DE102005039933B4 |
source | esp@cenet |
subjects | AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F,C08G CHEMISTRY COMPOSITIONS BASED THEREON COMPOSITIONS OF MACROMOLECULAR COMPOUNDS GENERAL PROCESSES OF COMPOUNDING MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONSONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS METALLURGY ORGANIC MACROMOLECULAR COMPOUNDS THEIR PREPARATION OR CHEMICAL WORKING-UP WORKING-UP |
title | Verfahren zur Herstellung von thermoplastisch verarbeitbaren Polyurethanen |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-17T23%3A33%3A53IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-epo_EVB&rft_val_fmt=info:ofi/fmt:kev:mtx:patent&rft.genre=patent&rft.au=BRAEUER,%20WOLFGANG&rft.date=2007-12-27&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EDE102005039933B4%3C/epo_EVB%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |