http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104557371-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G3-00 |
| filingDate | 2014-12-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2016-02-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2016-02-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-104557371-B |
| titleOfInvention | A kind of fixed bed adiabatic reactor single stage method methanol conversion produces the method for hydrocarbon mixture |
| abstract | A kind of method that fixed bed adiabatic reactor single stage method methanol conversion produces hydrocarbon mixture is that first material benzenemethanol mixes with the process water from separator, gasify after carrying out heat exchange with the part in reactor outlet material, mix with circulation dry gas again, enter in the fixed bed adiabatic reactor that ZSM-5 molecular sieve catalyzer is housed and carry out the reaction that methanol conversion produces hydrocarbon mixture; Fixed bed adiabatic reactor outlet material is divided into three parts: three parts again pool together after heat exchange, after cooling further, enter oil-water-gas three-phase separator; It is hydrocarbon mixture that separation obtains oil-phase product.The present invention has gas circulation than little, and operation energy consumption is low, is applicable to the advantage that large-scale produces. |
| priorityDate | 2014-12-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 21.