http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2012072307-A
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9e1bf06f55de84b78abc9a057807f7eb |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08L77-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G69-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G69-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08J3-20 |
filingDate | 2010-09-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0698355e0b296444aad562ce25b36399 |
publicationDate | 2012-04-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | JP-2012072307-A |
titleOfInvention | Process for producing polycaproamide resin composition |
abstract | In a method for producing a polycaproamide resin composition, there is provided a method for producing a polycaproamide resin composition capable of simplifying the process and reducing energy consumption and easily dispersing the additive uniformly. . Polycaproamide containing 3 to 15% by mass of a hot water soluble component is charged into a twin screw extruder having one or more stages of reduced pressure vents and one or more side feeders, and the reduced pressure vent part When melt extrusion is performed under a condition that satisfies the following formula (1) with a vacuum pressure of 20 kPa or less, the additive is charged in a state where the melt viscosity of polycaproamide in the side feeder is 75 Pa ยท s or less. A method for producing a polycaproamide resin composition. (Formula 1) 50 <= Q / Ns / S <= 200. Q: Discharge (kg / h). Ns: Screw rotation speed (rpm). S: Screw cross-sectional area (m 2 ) [Selection] Figure 1 |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2018035282-A |
priorityDate | 2010-09-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 78.