EP0145639A2 - Pompe à chaleur chimique à accumulateur chimique de longue durée - Google Patents
Pompe à chaleur chimique à accumulateur chimique de longue durée Download PDFInfo
- Publication number
- EP0145639A2 EP0145639A2 EP84730093A EP84730093A EP0145639A2 EP 0145639 A2 EP0145639 A2 EP 0145639A2 EP 84730093 A EP84730093 A EP 84730093A EP 84730093 A EP84730093 A EP 84730093A EP 0145639 A2 EP0145639 A2 EP 0145639A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- refrigerant
- reaction
- chemical
- heat pump
- exergy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000000126 substance Substances 0.000 title claims abstract description 12
- 230000007774 longterm Effects 0.000 title abstract 2
- 239000003507 refrigerant Substances 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 239000002594 sorbent Substances 0.000 claims abstract description 13
- 206010011968 Decreased immune responsiveness Diseases 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 238000005086 pumping Methods 0.000 claims abstract description 5
- 238000003795 desorption Methods 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 239000007795 chemical reaction product Substances 0.000 claims description 7
- 239000000376 reactant Substances 0.000 claims description 5
- 239000006096 absorbing agent Substances 0.000 claims description 4
- 230000008020 evaporation Effects 0.000 claims 3
- 238000001704 evaporation Methods 0.000 claims 3
- 230000002441 reversible effect Effects 0.000 claims 2
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 239000002918 waste heat Substances 0.000 abstract description 2
- 239000010457 zeolite Substances 0.000 description 8
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 7
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000006163 transport media Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
Definitions
- the invention relates to a chemical heat pump that is heated by heat, i.e. is driven by thermal energy, for pumping anergy from a room of reference temperature into a room of higher temperature according to the preamble of claim 1.
- the annual consumption figure ⁇ defined as the ratio of exergy supplied to total thermal energy given off this corresponds to the Carnot factor of the heating task averaged over the heating period.
- the relationship also applies if the ratio of stored exergy E to the heat generated by pumps (E + A) is referred to as the annual consumption figure cp.
- ⁇ has values for one location of the heat pump in the climate region of Central Europe around 0.07; Due to the unavoidable losses of exergy, the values of the annual consumption figure that can actually be achieved are between 0.25 and 0.7.
- the prior art for heat pumps with storage are characterized by zeolite storage heat pumps.
- Zeolites are solids that can absorb water vapor while releasing energy. Zeolites can therefore be used as sorbents when water is used as the refrigerant; absorption and desorption of the two reactants in the strict sense are not a chemical reaction but rather a physical adsorption process.
- the zeolite heat pumps are nevertheless mentioned because chemical heat pumps with chemical storage have not been described so far. (Chemical heat pumps without storage are not quite correctly called absorption heat pumps, because they are also used for desorption processes. In the conventional heat pumps, it is not water, but NH 3, for example, that is the refrigerant, which is why they are eliminated compared to the invention.)
- Zeolite storage heat pumps pose a number of fundamental problems due to the fact that the sorbent is a solid.
- the heat transfer to the water-saturated zeolite, for example via heat exchangers, requires a large number of surfaces and reliable contact with the solid; Because of the low partial pressure of the refrigerant water, the entire desorption process must be carried out in a fine vacuum. Since the zeolite can only be poured to a limited extent, the distinction between desorber and storage (as well as between absorber and storage) becomes obsolete: the storage itself with the zeolite supply is both absorber and desorber.
- the invention has for its object to enable the storage of the exergy of the thermal drive energy for the heat pump over a longer period of time, sufficient for one season, chemically inexpensively, with minimal technical effort and minimal exergy requirement for auxiliary units, which should be pointed out da8 desorption and absorption can also run in parallel with different outputs if required.
- the advantage of solving this problem is when a simple and inexpensive liquid with extremely low vapor pressure at ambient temperature and water as the refrigerant is used as the sorbent, for example air as a heat transfer medium and water vapor transport means for both desorption and absorption can, the free reaction enthalpy should be high in the reaction of sorbent and refrigerant.
- this eliminates in particular with aggressive sorbents such as. e.g. Sulfuric acid is in direct contact with the heat exchanger, since, for example, the drive heat is supplied to the air and the heat is extracted from the air.
- the desorption can be carried out at a relatively low temperature at ambient pressure, since the partial pressure of the water vapor loading is now almost independent of the absolute pressure in the desorber.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3331825 | 1983-09-01 | ||
| DE19833331825 DE3331825A1 (de) | 1983-09-01 | 1983-09-01 | Chemische waermepumpe mit chemischem langzeitspeicher |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0145639A2 true EP0145639A2 (fr) | 1985-06-19 |
| EP0145639A3 EP0145639A3 (fr) | 1985-10-30 |
Family
ID=6208159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP84730093A Withdrawn EP0145639A3 (fr) | 1983-09-01 | 1984-08-31 | Pompe à chaleur chimique à accumulateur chimique de longue durée |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0145639A3 (fr) |
| DE (1) | DE3331825A1 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2609535A1 (fr) * | 1987-01-08 | 1988-07-15 | Gradient Rech Royallieu | Pompe a chaleur a produit de sorption |
| EP0397482A3 (fr) * | 1989-05-12 | 1991-10-30 | Baltimore Aircoil Company, Inc. | Procédé et appareil frigorifique à absorption |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| USRE20933E (en) * | 1938-11-29 | Apparatus and process for condition | ||
| DE278076C (fr) * | 1911-08-11 | |||
| DE2645265A1 (de) * | 1976-10-07 | 1978-04-13 | Krupp Gmbh | Verfahren und anlage zur nutzung von sonnenenergie in verdampferanlagen |
| DE2719995A1 (de) * | 1977-05-04 | 1978-11-09 | Linde Ag | Absorptionskaelteanlage |
| US4151721A (en) * | 1977-09-09 | 1979-05-01 | Kumm Emerson L | Solar powered air conditioning system employing hydroxide water solution |
| DE2900388A1 (de) * | 1979-01-04 | 1980-07-10 | Borsig Gmbh | Absorptionskaeltemaschine mit speichereinrichtung fuer den betrieb mit zeitlich unterschiedlichem anfall von heizenergie und kaeltebedarf |
| US4338268A (en) * | 1980-08-13 | 1982-07-06 | Battelle Development Corporation | Open cycle thermal boosting system |
| DE3044580C2 (de) * | 1980-11-26 | 1986-11-27 | Siemens AG, 1000 Berlin und 8000 München | Wärmepumpe und Verfahren zu ihrem Betrieb |
| DE3129999A1 (de) * | 1980-11-26 | 1983-02-17 | Siemens AG, 1000 Berlin und 8000 München | "waermepumpe mit einer speichereinrichtung und verfahren zu ihrem betrieb" |
| DE3136273A1 (de) * | 1981-09-12 | 1983-03-24 | Philips Patentverwaltung Gmbh, 2000 Hamburg | "verfahren und vorrichtung zur nutzbarmachung von ausserhalb der spitzenverbrauchszeiten anfallender elektrischer energie" |
-
1983
- 1983-09-01 DE DE19833331825 patent/DE3331825A1/de not_active Ceased
-
1984
- 1984-08-31 EP EP84730093A patent/EP0145639A3/fr not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2609535A1 (fr) * | 1987-01-08 | 1988-07-15 | Gradient Rech Royallieu | Pompe a chaleur a produit de sorption |
| EP0397482A3 (fr) * | 1989-05-12 | 1991-10-30 | Baltimore Aircoil Company, Inc. | Procédé et appareil frigorifique à absorption |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0145639A3 (fr) | 1985-10-30 |
| DE3331825A1 (de) | 1985-03-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
| TCNL | Nl: translation of patent claims filed | ||
| PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
| AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 19860701 |
|
| RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: RADEBOLD, REINHART, DR. |