http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-213643147-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_e19e4907d0b2ec427fd9440b5e28ed13 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-00 |
| filingDate | 2020-09-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2021-07-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4ca821955ec1c18f9db91d2811d67270 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b0ee08d107eddc3ebb3653e21cb6d16b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c1602358e9bfd13773fcd06ec3528d26 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0df834aa9e999fa7fbb514c9741dd288 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_963d766e5cae021fa7e43e1fcc72dfc1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a89ee56c0b85e7e7392a3d953de830a2 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7345950ee7f3db534353837a75f72dd5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_de08ed884e3890f4e45573cfd2eb625b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_81f2440df517790630c73f705f3d9fa5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bd0f1d004152bcf85a523a697fdba091 |
| publicationDate | 2021-07-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-213643147-U |
| titleOfInvention | Reaction and distillation control system in spice production process |
| abstract | The utility model provides a reaction in spices production process, distillation control system, including first reation kettle, first reation kettle's feed inlet is connected with first metering tank, second metering tank, third metering tank and fourth metering tank, first reation kettle is connected with the second reation kettle, the second reation kettle is connected with reaction liquid intermediate tank, the bottom discharge port of reaction liquid intermediate tank is connected with tubular reactor group, be connected with the gas-liquid separation jar on the tubular reactor group, the gas-liquid separation jar is connected with first acidizing hydrolysis kettle, the feed inlet of first acidizing hydrolysis kettle is connected with fifth metering tank and sixth metering tank, be connected with second acidizing hydrolysis kettle on the first acidizing hydrolysis kettle, be connected with the acidizing intermediate tank on the second acidizing hydrolysis kettle; the utility model provides a reaction, distillation control system production process go on in succession in the spices production process, and output cooling agent steady quality reduces operating personnel intensity of labour, promotes production efficiency. |
| priorityDate | 2020-09-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 27.