http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-112015000961-B4
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_fa2f9b2646f5d09d372c2bb8e267a804 |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F2250-08 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F13-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D15-0266 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D15-025 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28D15-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28D15-00 |
filingDate | 2015-02-20^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2021-03-18^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e2e5e810a52cb32a8020c1f932ddada0 |
publicationDate | 2021-03-18^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | DE-112015000961-B4 |
titleOfInvention | Method and device for heat transfer |
abstract | A method of transferring heat, comprising the steps of: Heating one or more evaporator tanks (1), which are filled with at least two different fluids, by a thermal energy source, a first fluid being in a gaseous phase and a second fluid being in a liquid phase; Causing a pressure increase in the evaporator tank and a transition of the liquid phase of the second fluid into a gaseous phase of the second fluid mixed with the gaseous phase of the first fluid by the heating; Providing, under the increased pressure in the evaporator tank, a flow of the mixture of the gaseous phases of the first and second fluids via one or more steam lines (2) into one or more condensers (3), where the gaseous phase of the second fluid with the release of condensation heat condensing on a thermal energy receiver and forming a liquid phase of the second fluid; Providing, under the increased pressure in the evaporator tank, a flow of the condensed liquid phase of the second fluid, which is mixed with a gaseous phase of the first fluid, via a liquid line (4) into a collection tank (5) until a pressure in the evaporator tank (1) exceeds a pressure in the collection tank (5); As soon as all of the second fluid in the evaporator tank has passed from the liquid phase to the gaseous phase, while condensation of the gaseous phase of the second fluid in the condenser continues, the pressure in the evaporator tank to a pressure value which is lower than that in the A collection tank, whereby a flow of the condensed liquid phase of the second fluid and the gaseous phase of the first fluid from the collection tank to the evaporator tank is ensured through one or more check valves attached to one or more return lines (6), wherein a separator (8) is further provided on the return line to divide the mixture of the gaseous phase of the first fluid medium and the condensed liquid phase of the second fluid leaving the collection tank into a flow (10) of the gaseous phase of the first fluid and a flow (9) to separate the liquid phase of the second fluid and to provide a delay between the arrival time of the gaseous phase of the first fluid and the arrival time of the liquid phase of the second fluid in the evaporator tank, with the gaseous phase of the first fluid arriving first and thereafter the liquid phase of the second fluid arrives. |
priorityDate | 2014-02-25^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
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