http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-204607626-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a99d0130a313a96359d84f8e309688a7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a96cf4fa27955cdfb7512d5b92b05e54 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-129 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-10 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01C1-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-16 |
| filingDate | 2015-04-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2015-09-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_21151505c8ad0c5d8b29a0bdbca14ece http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ff9d3ce15cbe24320fd79ab5b7e0b3cf http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_adc3783f0808d559003c0c505d66fc0f http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_954b3e7dd9b8ca9ba679610a56af4b67 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_166970265e8db02583d01ddec21e7649 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b06060f858f5f55eb6089f47e2f2882d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_97165eee38ecd04486e7de626afb60c9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_984d773de21eb4d4432977f8c76fd21f http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e889563bc3a69bbd7e95749a72d459fe |
| publicationDate | 2015-09-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-204607626-U |
| titleOfInvention | Coal gas primary cooler waste heat ammonia steaming device |
| abstract | The utility model discloses coal gas primary cooler waste heat ammonia steaming device, comprise ammonia still, ammonia still comprises flash zone, dephlegmator, ammonia still top is provided with remained ammonia import, wastewater outlet is provided with bottom flash zone, wastewater outlet top is provided with waterwater entrance, wastewater outlet is connected with waste water circulation pump, waste water circulation pump is connected with primary cooler epimere, primary cooler epimere is connected with the waterwater entrance on ammonia still flash zone top, the top exit of dephlegmator is connected with the entrance of condenser, the outlet of condenser is connected with the entrance in the middle part of gas-liquid separator, gas-liquid separator upper outlet is connected with vacuum system, the non-condensable gas that vacuum system is extracted out is sent back in gas line, outlet bottom gas-liquid separator is connected with follow-up system.The utility model utilizes high-temperature part heat in the saturated raw gas of gas recovery primary cooler as remained ammonia ammonia still process thermal source, decreases distilled ammonia wastewater discharge, substantially reduce the number the usage quantity of primary cooler recirculated cooling water, reach the target of energy-saving and emission-reduction. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-112499710-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-110092432-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104787825-A |
| priorityDate | 2015-04-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 33.