http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108955326-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F2260-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D2015-0225 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F17-005 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D15-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/H05K7-20336 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28F17-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/H05K7-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28D15-02 |
| filingDate | 2018-07-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2020-03-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2020-03-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-108955326-B |
| titleOfInvention | Micro-channel gas-liquid separation evaporator device based on distribution and recovery channel |
| abstract | A vapor-liquid separation evaporator apparatus comprising: microchannel and recovery channel, the structural gaseous phase export that is equipped with of microchannel are equipped with working medium entry and liquid phase export on the recovery channel respectively, wherein: the microchannel and the recovery channel are separated by a wire mesh. The microchannel includes: heating the substrate, pin ribs and sintered surface; the recovery channel includes: the distribution cavity, the confluence unit and the backflow cavity; the bus bar unit includes: fluid infusion nozzle, distribution channel, backward flow hole and recovery passageway. The invention provides a gas-liquid separation evaporator device, which is characterized in that liquid supplementing and redundant liquid recovery are carried out through a distribution recovery structure, a porous sintering structure ensures that all areas of a heat exchange surface are in a wet state, a thin liquid film is evaporated on the surface, and two-phase flow in a cavity is similar to annular flow; the gas-phase working medium outlet and the liquid-phase working medium outlet are arranged, the gas-phase working medium enters the condenser or the liquid storage tank for cooling, the liquid-phase working medium enters the next evaporator for heat exchange continuously, and the series connection high-efficiency cooling of the plurality of heating elements is realized. |
| priorityDate | 2018-07-12-04:00^^<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/substance/SID418354341 http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID23978 |
Total number of triples: 18.