http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-S6310664-A
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_55911db9383dc3ba02a77f4eeb7b6b35 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0f705f295f4ba571f5311e5ef1b57807 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10C3-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10C3-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/D01F9-145 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/D01F9-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08L95-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10C3-10 |
filingDate | 1986-06-30^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d2c8682067a9ba8f46818cc3b05097ba http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_12bc70df434b66def4177c1a974cedd6 |
publicationDate | 1988-01-18^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | JP-S6310664-A |
titleOfInvention | Production of carbon precursor composed of thermosetting resin prepared from hydrogenated pitch |
abstract | PURPOSE: To obtain the title precursor which has a high carbonization yield and a low shrinkage factor during carbonization and allows graphatization to be freely controlled, by hydrogenating pitch to lower its softening point, adding a specified crosslinking agent thereto and heating the mixture in the presence of an acid catalyst. n CONSTITUTION: At least one pitch having a solftening point of not lower than 120°C selected from the group consisting of petroleum and coal pitches is hydrogenated to lower the softening point. A crosslinking agent mainly composed of an arom. compd. having at least two hydroxymethyl and/or halomethyl groups is added thereto. The mixture is heated in the presence of an acid catalyst at 60W300°C to obtain the desired carbon precursor. The pitch used has a carbonization yield of not lower than 50wt%. It is desirable that the pitch having a low softening point and a high carbonization yield is used as a starting material. It is preferred that the hydrogenation is carried out by a direct hydrogenation method wherein the hydrogenation is carried out in the presence of a catalyst in a hydrogen stream at a high temp. under a high pressure. n COPYRIGHT: (C)1988,JPO&Japio |
priorityDate | 1986-06-30^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
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