http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-03041831-A3
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c72d118f5664072de841f9c5c34b9d99 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D1-225 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G65-48 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D1-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G65-48 |
filingDate | 2002-10-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_900546d52b2b716854194591c73d8df1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6e62545ee8eec3618e4af14e0c897169 |
publicationDate | 2004-05-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | WO-03041831-A3 |
titleOfInvention | Method for isolating polyphenylene ether polymer resins from solution |
abstract | A method of removing substantially all solvent from a solution containing a polyphenylene ether polymer resin with little by-product formation (less than 250 ppm) is provided. The method employs a wiped thin film evaporator with a cylindrical heating chamber operating under conditions that satisfy the relationships defined by Equations I and II: 5.3*1024RLδexp(?-24123/T¿)/m < C (I), 100- (4960AP/Tm) < C (II); yields are maximized wherein values for feed rate (m) and percent solids (C) are selected to provide a maximum value for the output, Q, determined from the equation m * C = Q and the melt viscosity of the polyphenylene ether product is less than 50,000 centipoise at the operating temperature of the cylindrical heating chamber. |
priorityDate | 2001-11-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 19.