http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2016141698-A

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G85-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G69-28
filingDate 2015-01-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_218167190076a8fce39e15a8b5b81c13
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c871d63bf378620fa12ae68057785d70
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_336c19aa7a6877b08dcb4c68e0f64d80
publicationDate 2016-08-08-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber JP-2016141698-A
titleOfInvention Method for producing dehydrated polycondensation polymer
abstract In a method for producing a dehydrated polycondensation polymer having a step of dehydrating polycondensation of a prepolymer with an extruder having a vent part, a production method with high production efficiency is provided while suppressing vent-up. A method for producing a dehydrated polycondensation polymer comprising a step of dehydrating polycondensation of a prepolymer with an extruder having a vent part, wherein R defined by the following formula (1) is 2.50 or more and 4. The manufacturing method of the dehydration polycondensation type polymer made into 50 or less. R = S + 1.5 × V1 / V0 (1) V0: Effective space capacity in the extruder [cm 3 ] V1: Total capacity [cm 3 ] of prepolymer, polymer, and water vapor contained in the extruder S: Condensed water distillation rate per unit area from fore vent part [mg / (cm 2 × sec)] [Selection] Figure 2
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2023089941-A1
priorityDate 2015-01-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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