DE3143534A1 - Continuously running absorption refrigeration unit without a refrigerant distillation process - Google Patents

Continuously running absorption refrigeration unit without a refrigerant distillation process

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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Withdrawn
Application number
DE19813143534
Other languages
German (de)
Inventor
Joachim 2930 Varel Rieder
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to DE19813143534 priority Critical patent/DE3143534A1/en
Publication of DE3143534A1 publication Critical patent/DE3143534A1/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/14Sorption machines, plants or systems, operating continuously, e.g. absorption type using osmosis

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  • 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

The principle of continuously running absorption refrigeration units has been known for about 125 years. The major drawback of these units is the very low efficiency. With this principle, the energy which must be supplied is almost twice the refrigeration output generated. The reason is that the refrigerant distillation process in the stripper/condenser unit naturally requires at least the same energy consumption as the subsequent vaporisation of the refrigerant for the actual generation of cold. According to the invention, this refrigerant distillation process is replaced by reverse osmosis, so that the absorption refrigeration unit runs substantially more economically.

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)

Patentanspruch: Absorbtionskälteanlage zur Erzeugung von Kälte,zur Wärmerückgewinnung und zur Umwandlung von Wärme in mechanische Energie,dadurch gekennzeichnet,daß zur Rückgewinnung des Kältemittels aus der Lösung ein Umkehr - Osmose - Filter verwndet wird.Claim: Absorbtionskälteanlage for generating cold, for Heat recovery and for converting heat into mechanical energy, characterized in that a reverse osmosis filter is used to recover the refrigerant from the solution will.
DE19813143534 1981-11-03 1981-11-03 Continuously running absorption refrigeration unit without a refrigerant distillation process Withdrawn DE3143534A1 (en)

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

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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

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Country Link
DE (1) DE3143534A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51120455A (en) * 1975-04-16 1976-10-21 Mitsubishi Heavy Ind Ltd Absorption type refrigerator

Patent Citations (1)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

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