SE440550B - Absorption refrigeration device which works with hydrogen gas as an inert gas - Google Patents
Absorption refrigeration device which works with hydrogen gas as an inert gasInfo
- Publication number
- SE440550B SE440550B SE8404013A SE8404013A SE440550B SE 440550 B SE440550 B SE 440550B SE 8404013 A SE8404013 A SE 8404013A SE 8404013 A SE8404013 A SE 8404013A SE 440550 B SE440550 B SE 440550B
- Authority
- SE
- Sweden
- Prior art keywords
- hydrogen gas
- inert gas
- refrigerant
- substance
- gas
- Prior art date
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 239000011261 inert gas Substances 0.000 title claims abstract description 8
- 238000010521 absorption reaction Methods 0.000 title claims abstract 6
- 238000005057 refrigeration Methods 0.000 title abstract description 3
- 239000000126 substance Substances 0.000 claims abstract description 9
- 239000003507 refrigerant Substances 0.000 claims description 14
- 239000006096 absorbing agent Substances 0.000 claims description 11
- 238000009423 ventilation Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 239000012080 ambient air Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims 4
- 239000010936 titanium Substances 0.000 claims 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims 1
- 230000002745 absorbent Effects 0.000 claims 1
- 239000002250 absorbent Substances 0.000 claims 1
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 229910052747 lanthanoid Inorganic materials 0.000 claims 1
- 150000002602 lanthanoids Chemical class 0.000 claims 1
- 229910052748 manganese Inorganic materials 0.000 claims 1
- 239000011572 manganese Substances 0.000 claims 1
- 229910001092 metal group alloy Inorganic materials 0.000 claims 1
- 150000002739 metals Chemical class 0.000 claims 1
- 229910052719 titanium Inorganic materials 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 description 3
- 150000004678 hydrides Chemical class 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 150000004681 metal hydrides Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
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
- F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
- F25B15/10—Sorption machines, plants or systems, operating continuously, e.g. absorption type with inert gas
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
8404013-8 Från absorbatorkärlet lU stiger blandningen av köldmediumànga och inert gas upp genom absorbatorn 38 och möter där fattig lösning, som, driven av nivån 24, kommer från röret 22 via ett rör 4D in i absorbatorns 38 övre del vid 42. Vid sin strömning nedåt genom absorbatorn 38 absorberar den fattiga lösningen uppåtströmmande köldmedium- ånga under värmeavgivning till absorbatorns omgivning, varigenom den fattiga lösningen blir rik lösning igen innan den rinner ned i absorbatorkärlet 10 vid 44. Den uppâtstigande inerta gasen fortsätter från absorbatorn 38 till röret 32 och gär därefter på nytt in i föràngaren 30 och låter köldmediumkondensatet förangas i sig. From the absorber vessel 11, the mixture of refrigerant vapor and inert gas rises through the absorber 38 and meets there poor solution, which, driven by the level 24, comes from the tube 22 via a tube 4D into the upper part of the absorber 38 at 42. At its flow downwardly through the absorber 38, the poor solution absorbs upward refrigerant vapor during heat dissipation to the absorber environment, whereby the poor solution becomes rich solution again before flowing into the absorber vessel 10 at 44. The ascending inert gas continues from the absorber 38 to the tube 32 and then back into the evaporator 30 and allows the refrigerant condensate to evaporate on its own.
I ändamål att förhindra att köldmediumànga, som eventuellt inte kondenseras i kondensorn 26, och inert gas, som medföljer köldmediumkondensatet in i kondensorn, samlas i kondensorn och blockerar utströmningen av köldmediumkondensat från denna, är ett ventilationsrör 46 anordnat mellan kondensorns 26 utlopp och röret 36, vilket ventilationsrör leder bort gasformigt medium till absorbatorkärlet 10.In order to prevent refrigerant vapor, which may not be condensed in the condenser 26, and inert gas which accompanies the refrigerant condensate into the condenser, collect in the condenser and block the outflow of refrigerant condensate therefrom, a ventilation pipe 46 is provided between the outlet of the condenser 26 and the condenser 26 which vent pipe leads gaseous medium away to the absorber vessel 10.
Den Ovan beskrivna anordningar: är förut allmänt känd. Det nya hos uppfinningen skall nu beskrivas.The devices described above: are previously generally known. The novelty of the invention will now be described.
En behållare 50 är anordnad i värmeledande kontakt med ventilationsröret 46 och kommunicerar genom en ledning 52 med detta. Behållaren 50 innehåller ett ämne 54, som vid uppvärmning avger vätgas och vid avkylning absorberar vätgas. Om omgivninga- temperaturen blir så hög, att den ej förmår att kondensera köldmediet i kondensorn så ,, att köldmediumånga passerar ut genom kondenscrns utlopp, kommer detta att resultera i att ventilationsrörets temperatur stiger ca. 10 - 15 OCZ, varvid ämnet 54 i be- hållaren 50 värmes och avger vätgas till kylapparatens cirkulationssystem. Trycket stiger härvid i cirkulationssystemet med resultat att kondenseringstemperaturen i kondensorn 26 stiger, varvid köldmediet börjar kondensera igen och apparaten återtar sin förmåga att producera kyla.A container 50 is arranged in heat-conducting contact with the ventilation pipe 46 and communicates with a conduit 52 therewith. The container 50 contains a substance 54 which, on heating, emits hydrogen gas and on cooling absorbs hydrogen gas. If the ambient temperature becomes so high that it is unable to condense the refrigerant in the condenser so that refrigerant vapor passes out through the condenser outlet, this will result in the temperature of the ventilation pipe rising approx. 10 - 15 OCZ, whereby the substance 54 in the container 50 is heated and emits hydrogen gas to the refrigeration system's circulation system. The pressure then rises in the circulation system with the result that the condensing temperature in the condenser 26 rises, whereby the refrigerant begins to condense again and the apparatus regains its ability to produce cold.
När omgivningstemperaturen sjunker igen sjunker ventilationsrörets 46 och där- med ämnets 54 temperatur, varvid ämnet absorberar vätgas från cirkulationssystemet, så att trycket i detta sjunker mot normala värden.When the ambient temperature drops again, the temperature of the ventilation pipe 46 and thus of the blank 54 drops, whereby the blank absorbs hydrogen gas from the circulation system, so that the pressure therein drops towards normal values.
Behållaren 5D med ämnet 54 kan också påverkas direkt av omgivningstempera- turen, såsom visas med streckade linjer i figuren, där behållaren 50 är anordnad fritt i omgivande luft. Ämnet 54 kan vara en metall eller en förening, som bildar en hydrid med väte vid avkylning och där hydriden återgår till att vara metall eller förening och vätgas vid uppvärmning. Exempel pà en metall och förening som bildar reversibla metallhydrider är Ti respektive LaNis, som tillsammans med väte bildar Til~l2 respektive l.aNi5H?- å.The container 5D with the blank 54 can also be directly affected by the ambient temperature, as shown in broken lines in the figure, where the container 50 is arranged freely in ambient air. The substance 54 may be a metal or a compound which forms a hydride with hydrogen on cooling and where the hydride returns to being a metal or compound and hydrogen gas on heating. Examples of a metal and compound which form reversible metal hydrides are Ti and LaNis, respectively, which together with hydrogen form Til ~ l2 and l.aNi5H? - å, respectively.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8404013A SE440550B (en) | 1984-08-08 | 1984-08-08 | Absorption refrigeration device which works with hydrogen gas as an inert gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8404013A SE440550B (en) | 1984-08-08 | 1984-08-08 | Absorption refrigeration device which works with hydrogen gas as an inert gas |
Publications (2)
Publication Number | Publication Date |
---|---|
SE8404013D0 SE8404013D0 (en) | 1984-08-08 |
SE440550B true SE440550B (en) | 1985-08-05 |
Family
ID=20356675
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE8404013A SE440550B (en) | 1984-08-08 | 1984-08-08 | Absorption refrigeration device which works with hydrogen gas as an inert gas |
Country Status (1)
Country | Link |
---|---|
SE (1) | SE440550B (en) |
-
1984
- 1984-08-08 SE SE8404013A patent/SE440550B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
SE8404013D0 (en) | 1984-08-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6303006B1 (en) | System and method for distilling liquid | |
US2138688A (en) | Method and apparatus for the production of cold | |
SE440550B (en) | Absorption refrigeration device which works with hydrogen gas as an inert gas | |
US3038321A (en) | Absorption refrigeration system | |
US4137727A (en) | Absorption refrigeration system with precooler and inert gas control | |
US3279202A (en) | Concentration control for absorption refrigeration systems | |
GB2252738A (en) | Dehumidifier | |
JPS581739Y2 (en) | Absorption refrigeration equipment | |
US3078690A (en) | Absorption refrigeration apparatus | |
SE462350B (en) | FLAT COOLED ABSORPTION COOLING DEVICE | |
US4028904A (en) | Preheater for weak absorbent | |
JP2568709B2 (en) | Heat transfer device | |
US2266584A (en) | Refrigeration | |
US3695052A (en) | Concentration control for multiple stage absorption refrigeration systems | |
US3240262A (en) | Gas and liquid contact heat exchanger | |
CN209270864U (en) | Online distilling apparatus | |
JP3381094B2 (en) | Absorption type heating and cooling water heater | |
JP3729876B2 (en) | Air conditioner low temperature regenerator | |
JP2000121256A (en) | Heat exchanger | |
SE513444C2 (en) | Absorption chiller provided to prevent corrosion therein | |
JP2000121257A (en) | Heat exchanger | |
US2336411A (en) | Refrigeration | |
US3293873A (en) | Refrigerant control for absorption refrigeration systems | |
JP3133441B2 (en) | Bleeding device for absorption refrigerator | |
KR0147749B1 (en) | Regenerator for absorptive airconditioner |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
NUG | Patent has lapsed |
Ref document number: 8404013-8 Effective date: 19920306 Format of ref document f/p: F |