DE3143534A1 - Continuously running absorption refrigeration unit without a refrigerant distillation process - Google Patents
Continuously running absorption refrigeration unit without a refrigerant distillation processInfo
- Publication number
- DE3143534A1 DE3143534A1 DE19813143534 DE3143534A DE3143534A1 DE 3143534 A1 DE3143534 A1 DE 3143534A1 DE 19813143534 DE19813143534 DE 19813143534 DE 3143534 A DE3143534 A DE 3143534A DE 3143534 A1 DE3143534 A1 DE 3143534A1
- Authority
- DE
- Germany
- Prior art keywords
- refrigerant
- distillation process
- absorption refrigeration
- continuously running
- refrigeration unit
- 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- Withdrawn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
- 239000003507 refrigerant Substances 0.000 title claims abstract description 14
- 238000005057 refrigeration Methods 0.000 title abstract description 11
- 238000010521 absorption reaction Methods 0.000 title abstract description 9
- 238000004821 distillation Methods 0.000 title abstract description 9
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 8
- 238000011084 recovery Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000009834 vaporization Methods 0.000 abstract 1
- 239000006096 absorbing agent Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000000034 method Methods 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
- F25B15/14—Sorption machines, plants or systems, operating continuously, e.g. absorption type using osmosis
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
Titel: Kontinuierlich arbeitende AbsorbtionskälteanlageTitle: Continuously operating absorption refrigeration system
ohne Kältemittel - Destillationsprozess.without refrigerant - distillation process.
Anwendungsgebiet: Die Erfindung betrifft eine Absorbtionskälteanlage,wie sie zur Kälteerzeugung verwendet wird.Field of application: The invention relates to an absorption refrigeration system, such as it is used to generate cold.
Zweck: Zweck der tfindung ist,den Wirkungsgrad von Absorbtionskälteanlagen so zu verbessern,daß dieser mindestens so gut wird wie der von Kompressoranlagen.Purpose: The purpose of the finding is to determine the efficiency of absorption refrigeration systems to be improved so that it is at least as good as that of compressor systems.
Stand der Technik: ie Funktion der Absorbtionskälteanlage ist bekannt.In einer solchen Anlage wird fast die gesamte zugeführte Energie dazu benötigt,im Austreiber das Kältemittel zu verdampfen.Der Kältemftteldampf wird wieder kondensiert,wodurch die zugeführte Energie wieder frei wird und abgeführt werden muß.Dieser Destillationsprozess ist bisher notwendig,weil nur das reine und flüssige Kältemit- -tel zur Kühlung verwendet werden kann.State of the art: The function of the absorption refrigeration system is known In such a system, almost all of the energy supplied is required in the expeller to evaporate the refrigerant. The refrigerant vapor is condensed again, as a result of which the supplied energy is released again and has to be dissipated. This distillation process has so far been necessary because only the pure and liquid refrigerant is used for cooling can be used.
Kritik: Der Destillationsprozess hat an der Kälteerzeugung keinen Anteil,sondern stellt nur einen unerwünschten Verbraucher dar.Criticism: The distillation process has no cold generation Share, but only represents an undesirable consumer.
Aufgabe: Die Aufgabe der Erfindung ist,eine Absorbtionskälteanlage ohne Destillationsprozess zu betreiben.Task: The task of the invention is to provide an absorption refrigeration system to operate without a distillation process.
Lösung: Diese Aufgabe wird erfindungsmäßig dadurch gelöst, daß an Stelle der Destillationsprozess - Apparatur ein Umkehr - Osmose - Filter verwendet wird.Solution: According to the invention, this object is achieved in that at A reverse osmosis filter is used in place of the distillation process apparatus will.
Vorteile: Die durch diese Erfindung erzielten Vorteile bestehen darin daß die zur Kälteerzeugung zur Verfügung stehende Kältemittelmenge nicht von der zugeführten Energiemenge,sondern haupsächlich von der Größe der Filteroberfläche abhängig ist.Advantages: The advantages achieved by this invention are therein that the amount of refrigerant available for refrigeration does not depend on the supplied amount of energy, but mainly on the size of the filter surface is dependent.
Die zugeführte Energie bringt über eine Pumpe die Lösung auf den für die Umkehr - Osmose erforderlichen Druck.I)afür ist jedoch im Verhältniss zur im Verdampfer umgesetzten Uärmeenergie relativ wenig zugeführte Energie notwendig, so daß ein Leistungsverhältniss von 1 zu 10 möglich ist.The supplied energy brings the solution to the for via a pump the pressure required for reverse osmosis. I) afor is, however, in proportion to the im Heat energy converted by the evaporator relatively little energy supplied is required, so that a performance ratio of 1 to 10 is possible.
Demgegenüber haben Kompressoranlagen nur ein solches von n zu 3 und Absorbtionskälteanlagen mit Destillationsprozess nur ein solches von 1 zu 0,7 Beschreibung der Zeichnung: Im Verdampfer ( 1) wird durch Zufuhr von Wärme aus dem abzukühlenden Medium das Kältemittel verdampft.Dieser Dampf wird im Absorber ( 2 ) durch die magere Lösung absorbiert.Dadurch wird die Verdampfungswärme wieder frei und muß durch Kühlung von außen abgeführt werden. Durch eine Pumpe ( 3 ) wird die nun reiche Lösung zum Umkehr - Osmose - Filter ( 4 ) transportiert und gleichzeitig auf den für die Umkehr -Osmose erforderlichen Druck gebracht.lm Umkehr - Osmose -Filter diffundiert nun das Kältemittel durch die Membran.In contrast, compressor systems only have one of n to 3 and Absorption refrigeration systems with a distillation process only have a rate of 1 to 0.7 description of the drawing: In the evaporator (1) is supplied with heat from the to be cooled Medium the refrigerant evaporates. This vapor is in the absorber (2) through the lean Solution absorbed. This releases the heat of evaporation and has to be cooled be discharged from the outside. The now rich solution is used by a pump (3) Reverse osmosis filter (4) transported and at the same time on the one for the reverse - Osmosis brought the required pressure. Im reverse - osmosis filter is now diffusing the refrigerant through the membrane.
Die Lösung wird dadurch wieder arm und fließt über ein Regelventil ( 5 ) zum Absorber zurück.Dieses Ventil wird so angesteuert,daß einerseits der Verdampferdruck im Absorber und andererseits der hohe Druck an der Membran erhalten bleibt.Das nun an der Verdampferseite des Umkehr-Osmose - Filters vorhandene Kältemittel fließt über ein Ventil ( 6 ) zum Verdampfer,wo es wiederum verdampft wird.The solution becomes poor again and flows through a control valve (5) back to the absorber. This valve is controlled in such a way that, on the one hand, the evaporator pressure in the absorber and on the other hand the high pressure on the membrane is maintained The refrigerant present on the evaporator side of the reverse osmosis filter flows Via a valve (6) to the evaporator, where it is again evaporated.
Dieses Ventil läßt nur das flüssige Kältemittel durch und verhindert somit daß der Verdampfungsvorgang schon an der Membran beginnt.This valve only lets the liquid refrigerant through and prevents it so that the evaporation process already begins at the membrane.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813143534 DE3143534A1 (en) | 1981-11-03 | 1981-11-03 | Continuously running absorption refrigeration unit without a refrigerant distillation process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813143534 DE3143534A1 (en) | 1981-11-03 | 1981-11-03 | Continuously running absorption refrigeration unit without a refrigerant distillation process |
Publications (1)
Publication Number | Publication Date |
---|---|
DE3143534A1 true DE3143534A1 (en) | 1983-06-01 |
Family
ID=6145472
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19813143534 Withdrawn DE3143534A1 (en) | 1981-11-03 | 1981-11-03 | Continuously running absorption refrigeration unit without a refrigerant distillation process |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE3143534A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2652884A1 (en) * | 1989-10-09 | 1991-04-12 | Air Liquide | METHOD AND INSTALLATION FOR REFRIGERATION USING A REFRIGERANT MIXTURE. |
WO1993013367A1 (en) * | 1991-12-24 | 1993-07-08 | Seishi Watanabe | Solar cooling apparatus |
DE19516630A1 (en) * | 1995-05-05 | 1996-11-07 | Electrolux Siegen Gmbh | Process for operating an absorption cooling unit and absorption cooling unit |
CN101943501A (en) * | 2010-09-26 | 2011-01-12 | 浙江大学 | Absorption refrigeration system of semipermeable membrane type |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51120455A (en) * | 1975-04-16 | 1976-10-21 | Mitsubishi Heavy Ind Ltd | Absorption type refrigerator |
-
1981
- 1981-11-03 DE DE19813143534 patent/DE3143534A1/en not_active Withdrawn
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51120455A (en) * | 1975-04-16 | 1976-10-21 | Mitsubishi Heavy Ind Ltd | Absorption type refrigerator |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2652884A1 (en) * | 1989-10-09 | 1991-04-12 | Air Liquide | METHOD AND INSTALLATION FOR REFRIGERATION USING A REFRIGERANT MIXTURE. |
EP0422973A1 (en) * | 1989-10-09 | 1991-04-17 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Refrigeration process and apparatus using a refrigerant mixture |
WO1993013367A1 (en) * | 1991-12-24 | 1993-07-08 | Seishi Watanabe | Solar cooling apparatus |
DE19516630A1 (en) * | 1995-05-05 | 1996-11-07 | Electrolux Siegen Gmbh | Process for operating an absorption cooling unit and absorption cooling unit |
DE19516630C2 (en) * | 1995-05-05 | 1998-09-24 | Electrolux Siegen Gmbh | Process for operating an absorption cooling unit and absorption cooling unit |
CN101943501A (en) * | 2010-09-26 | 2011-01-12 | 浙江大学 | Absorption refrigeration system of semipermeable membrane type |
CN101943501B (en) * | 2010-09-26 | 2012-05-30 | 浙江大学 | Absorption refrigeration system of semipermeable membrane type |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE10214183C1 (en) | Drive mechanism, for refrigeration, has absorption refrigeration machine connected to steam turbine, operated by steam extracted from turbine, preferably from low pressure part of turbine | |
DE69511962T2 (en) | System and device for converting thermal energy into mechanical or electrical power | |
DE2754626C2 (en) | Refrigeration system operating with an energy source at a relatively low temperature, in particular solar energy | |
DE10138255B4 (en) | Arrangement of cascade refrigeration system | |
US4333515A (en) | Process and system for boosting the temperature of sensible waste heat sources | |
EP1500802B1 (en) | Cooling device | |
EP2059104A2 (en) | Cooling device for a computer system | |
EP0021205B1 (en) | Hybrid compression-absorption method for operating heat pumps or refrigeration machines | |
DE19511709A1 (en) | Generating cold and heat with aid of absorption cooling machine | |
EP1706598B1 (en) | Method and installation for converting heat energy from refrigerating machines | |
DE3143534A1 (en) | Continuously running absorption refrigeration unit without a refrigerant distillation process | |
DE2936873C2 (en) | Process for the thermal regeneration of loaded sorbent materials | |
DE4415199A1 (en) | Refrigerating plant using absorption principle | |
DE19535840A1 (en) | Absorption chiller and method for its operation | |
EP0531293B1 (en) | Thermal processes for evaporating, condensing and absorbing and combination of said processes | |
DE69921871T2 (en) | Absorption refrigeration system with coupling of condensate and solution | |
DE102017100281B3 (en) | Absorption process and machine for the use of industrial waste heat | |
DE3129957A1 (en) | Refrigerating machine with a compressor and method of operating it | |
DE19500335A1 (en) | Prodn. of cold and heat using reversible osmotic driven sorption refrigerator | |
DE491065C (en) | Cold generating machine based on the absorption principle | |
DE10162934A1 (en) | Process and plant for solar thermal refrigeration | |
DE3327752A1 (en) | Method and device for increasing the efficiency of turbine processes | |
AT154276B (en) | Absorption chiller. | |
DE10161210A1 (en) | Seawater desalination process uses an open absorption apparatus to evaporate at low pressure, condense at high pressure | |
CH180774A (en) | Continuously working absorption chiller. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
OR8 | Request for search as to paragraph 43 lit. 1 sentence 1 patent law | ||
8105 | Search report available | ||
8110 | Request for examination paragraph 44 | ||
8139 | Disposal/non-payment of the annual fee |