http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-102952007-B
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_3ec1e7a766cb78cc57892d8729052f7b |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-36 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C53-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C51-09 |
| filingDate | 2012-11-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2015-01-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d0805af1e8ebb11233f7d89d28601d57 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7dd27617c2468fe01bceecb841b584f6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c26b6ab715cad312370d68f4f38ca911 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6e0740d07e0b59dc161b498518ff7d9b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a1b46237066d8dc6118265bff9694044 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c98f991a77c9910012220afb33d7873e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cb54c119c16bca5f2d39f1076ac32709 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_939f6425ffa87ce08620aca5fe5e90a1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_01fce4d64af80a365bf145f826941135 |
| publicationDate | 2015-01-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-102952007-B |
| titleOfInvention | Production device capable of producing 100,000 tons of formic acid per unit per year |
| abstract | The invention discloses a production device capable of producing 100,000 tons of formic acid per unit per year, which mainly comprises a carbonyl reactor, a methyl ester rectifying tower, a methyl ester storage tank, a first hydrolysis reactor, a second hydrolysis reactor, a primary acid tower, a secondary acid tower and a tertiary acid tower, wherein the bottom outlet of the carbonyl reactor is connected with the middle inlet of the methyl ester rectifying tower, the top condensate of the methyl ester rectifying tower is connected with the top of the methyl ester storage tank, the bottom outlet of the methyl ester storage tank is connected with the bottom of the first hydrolysis reactor, the upper outlet of the first hydrolysis reactor is connected with the lower inlet of the second hydrolysis reactor, the upper outlet of the second hydrolysis reactor is connected with the middle inlet of the primary acid tower, the bottom outlet of the primary acid tower is connected with the middle inlet of the secondary acid tower, the lower outlet of the secondary acid tower is connected with the middle inlet of the tertiary acid tower, carbon monoxide gas distributors are arranged in the carbonyl reactor, and the first hydrolysis reactor and the second hydrolysis reactor adopt an internal heating method. The production device capable of producing 100,000 tons of formic acid per unit per year has the advantages that the device is safe and simple to operate, the production links are reduced, the production cost is decreased, the service life of equipment is prolonged and the economic benefits are improved. |
| priorityDate | 2012-11-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 31.