http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-214680083-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0d0b7f1128f2b581e914cd2fba0c83cc |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C7-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-06 |
| filingDate | 2021-06-10^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2021-11-12^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f35c45963377fcbb26ef5b0deb3e5f8a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_926064fb157e158592c9857bf756aece http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8f23b1e0b668fdcea2ba6133553fac6c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6b60d836440311b8eafdeb57ce480c47 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8f54a6dbb4b11ef320f589922d3b2b50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cee62e0b5eabaf19fbc559d301e858db http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4368e0746278435df126c5282070f880 |
| publicationDate | 2021-11-12^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-214680083-U |
| titleOfInvention | Ethane liquefied recovery device |
| abstract | The utility model discloses an ethane liquefied recovery unit, including main heat exchanger, low temperature separator, demethanizer, deethanizer and three-way valve, the feed gas passes through inside the three-way valve gets into main heat exchanger, the export of main heat exchanger with the entry of low temperature separator passes through the pipe connection, the export of low temperature separator with the entry of demethanizer passes through the pipe connection, the export of demethanizer with the entry of deethanizer passes through the pipe connection, still includes ethane liquefaction heat exchanger, the export of deethanizer with the entry of ethane liquefaction heat exchanger passes through the pipe connection, the export output product of ethane liquefaction heat exchanger, its production that can realize liquid ethane to can effectively reduce the energy consumption of liquid ethane production. The utility model has the advantages that: the energy consumption can be obviously reduced for the production of liquid ethane by using high-pressure feed gas; the whole process is optimized, the ethane recovery efficiency is improved, and more remarkable economic benefits are brought. |
| priorityDate | 2021-06-10^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
| Predicate | Subject |
|---|---|
| isDiscussedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID6324 http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID419559535 |
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