Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7f9af914ed2fb00cd4f1b8b1a28964e4 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-10 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C68-06 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J31-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-96 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C68-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C68-08 |
filingDate |
1997-06-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
1999-02-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f00d66c3a91e0f20fc9f7840c3e54c9c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0d3e8fd1eb45802b060a4de6b79d48b1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_89ae331ae8a39477b9845638de552902 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_25fc9d909d9d37ef5c297077e2931343 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_08d132e4d5469af3765993846224bcdb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7f7609308b575bbfdae1c377ead8ef84 |
publicationDate |
1999-02-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-5874605-A |
titleOfInvention |
Process for preparing aromatic carbonic ester |
abstract |
PCT No. PCT/JP97/02000 Sec. 371 Date Feb. 3, 1998 Sec. 102(e) Date Feb. 3, 1998 PCT Filed Jun. 10, 1997 PCT Pub. No. WO97/47586 PCT Pub. Date Dec. 18, 1997An aromatic carbonate ester is continuously and efficiently prepared by the transesterification of an aromatic carboxylate with an aliphatic carbonate ester and/or aromatic.aliphatic carbonate ester. A raw material including an aromatic carboxylate, aliphatic carbonate ester and/or aromatic.aliphatic carbonate ester, and a catalyst are continuously fed to a first stage of a reactive distillation column (1) through a raw material feeding pipe (5). Meanwhile, an aliphatic carbonate ester (a) whose boiling point is lower than that of a reactant liquid that is present in a second stage lower than the first stage is continuously fed to the second stage through an aliphatic carbonate ester (a) feeding pipe (6). The second stage is preferably a column bottom section of the reactive distillation column (1). The amount of aliphatic carbonate ester (a) fed is preferably 0.001 to 5 times, by weight, more than the amount of the raw material fed. |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-0100560-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8309750-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-RE38995-E http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-6469191-B1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2009131706-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-6420588-B1 |
priorityDate |
1996-06-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |