SU632717A1 - Working body - Google Patents

Working body

Info

Publication number
SU632717A1
SU632717A1 SU752113034A SU2113034A SU632717A1 SU 632717 A1 SU632717 A1 SU 632717A1 SU 752113034 A SU752113034 A SU 752113034A SU 2113034 A SU2113034 A SU 2113034A SU 632717 A1 SU632717 A1 SU 632717A1
Authority
SU
USSR - Soviet Union
Prior art keywords
temperature
mixture
cooling
section
working fluid
Prior art date
Application number
SU752113034A
Other languages
Russian (ru)
Inventor
Мойтцнер Клаус
Лоренц Аксель
Original Assignee
Феб Монсатор Хаусхальтгросгеретекомбинат Шварценберг Бетриб Дкк Шарфенштейн (Инопредприятие)
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 Феб Монсатор Хаусхальтгросгеретекомбинат Шварценберг Бетриб Дкк Шарфенштейн (Инопредприятие) filed Critical Феб Монсатор Хаусхальтгросгеретекомбинат Шварценберг Бетриб Дкк Шарфенштейн (Инопредприятие)
Application granted granted Critical
Publication of SU632717A1 publication Critical patent/SU632717A1/en

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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
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D11/00Self-contained movable devices, e.g. domestic refrigerators
    • F25D11/02Self-contained movable devices, e.g. domestic refrigerators with cooling compartments at different temperatures
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/04Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
    • C09K5/041Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
    • C09K5/044Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/04Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
    • C09K5/041Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
    • C09K5/044Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
    • C09K5/045Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
    • 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
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/006Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant containing more than one component
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2205/00Aspects relating to compounds used in compression type refrigeration systems
    • C09K2205/10Components
    • C09K2205/12Hydrocarbons
    • C09K2205/122Halogenated hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2205/00Aspects relating to compounds used in compression type refrigeration systems
    • C09K2205/10Components
    • C09K2205/12Hydrocarbons
    • C09K2205/128Perfluorinated hydrocarbons

Description

1one

Изобрегение огносигс  к холодильной технике, касаетс  рабочих тел бытовых устройств с охлаждающими секци ми, имеющими разную температуру, и может быть применено, например, дл  двухтемператзфных домашних холодильников, работающих на компрессионном принципе охлаждени  и имеющих в каждой охлаждающей секции испаритель.The image of ognosigs for refrigeration technology concerns the working bodies of household appliances with cooling sections having different temperatures, and can be used, for example, for two-temperature household refrigerators operating on the compression principle of cooling and having an evaporator in each cooling section.

Известны неазеофопные рабочие тела, которые используютс  в холодильных машинах на основе фреокЗ R 114 ij .Non-azeophore working bodies are known, which are used in refrigerating machines based on the Frev3 R 114 ij.

Недостатком этих рабочих тел  вл етс  невозможность обеспечени  соответствующих температур, которые могли бы служить гарантией долгосрочного сохранени  замороженных продуктов в холодильных машинах.The disadvantage of these working fluids is the impossibility of providing appropriate temperatures, which could serve as a guarantee for the long-term preservation of frozen food in refrigeration machines.

Например, к двух температурным домашним холодильникам предъ вл ютс  опрёделенные требовани , в соответствии с которыми в секции с нормальной степенью охлаждени  должна поддерживатьс  температура в пределах О-5 С с возможностью регулировани , а в секции с высокой степенью охлаждени  температура от (-18) С и ниже.For example, certain temperature requirements are imposed on two temperature domestic refrigerators, according to which in a section with a normal degree of cooling, the temperature should be maintained within -5 ° C with controllability, and in a section with a high degree of cooling from (-18) ° C and below.

Целью изобретени   вл етс  создание такихнеазеотропных рабочих тел, которые могли бы обеспечить соответствующие температуры испарени  в различных секци х холодильников.The aim of the invention is to create such azeotropic working fluids that could provide appropriate evaporation temperatures in different sections of refrigerators.

Поставленна  цель достигаетс  тем, что рабочее тело дополнительно содержит слепующие фреоны из р да , К13 В1 R22 ,R115 при следующем соотнощеннн кокпто енгов, вес. ч:The goal is achieved by the fact that the working fluid additionally contains blinding freons from a row, K13 B1 R22, R115 with the following relative ratio of cockpto engs, weight. h:

R1I4 / ,85-0,95R1I4 /, 85-0.95

илиor

TR13 В10,5 -0,8 TR13 B10.5 -0.8

ИЛ1$IL1 $

,4 -О,7 4-O, 7

илиor

R114/ R115О,2-О,45R114 / R115О, 2-О, 45

Claims (1)

Дл  обеспечени  соответстви  средних темпфагур испарени  и необходимых температур в секци х холодильника к достижени  необходимого давлени  при всасываний (около 1 ат) и допустимого давпени  ожижени  указанные неаэвогропные смеси заливают в холодный агрегат двух- температурного холодильника в у..нных выше концентраци х, Выбор окончательной :о;::,це ггратдки. С1Ле си рабочего тела зависит в каждом конкратном случае от объема нагнетани , растворимости обоих компонентов смеси в холодильном машинном масле, от степени изол ции секций холодильника в диапазоне изменени  внешних температур. Пример. Расширенна  в дросселирующем устройстве охлаждающа  смесь начинает испар тьс  на входе в .исааригель секции глубокого охлаждени  при низкой температуре, завис щей от давлени  испарени  и конч1енграции смеси. По мере притока тепла и дальнейшего испарени  температура смеси постепенно повышаетс  вследствие посто нного изменени  состава , в результате чего она покидает иоааритель с более высокой температурой и не испар етс  полностью. При этой температуре смесь влажных паров поступает в испаритель секции с нормальной степенью охлаждени , где продолжаетс  процесс повышени  температуры под вли нием дальнейшего притока тепла. Смесь рабочего тела покидает испаритель секции с нор мальной степенью охлаждени  с несколь-, ко более низкой температурой чем га, котора  имеетс  в этой секции и находитс  Б парообразном состо нии. Без учета вли ни  охладительного машинного масла смесь паров имеет ту же концентрацию, что и жкдка  смесь перед дросселированием. Смесь паров отсасываетс  компрессором, сжимаетс  и сжижаетс  в конденсаторе, где смесь измен ющегос  состава проходит через весь тем- .пературный интервал и затем с-прежней концентрацией поступает в дроссельное устройство. Преимущества предлагаемого рабочего тела состо т в том, что на базе простоYx3 контура циркул ции рабочего тела мо 63 74 жет работать двухтемпературный холодильник , у которого в секции глубокого охлаждени  достигаетс  температура (-18) С и , а в секции с нормальной степенью охлаждени  имеетс  возможность автоматического оттаивани  испарител  во врем  фазы остановки компрессора, причем отсутствует необходимость в дополнительной энергии и обеспечиваетс  относительно высока  влажность воздуха и низкое потребление мощности, вследствие благопри тных с термодинамической точки прени  соотношений перепада температур испарителей и конденсатора. Кр9Ме того, небольша  разница между температурой в помещении и в испарителе секции с нормальной степенью охлаждени  в большей Мере гарантирует оттаивание этого испарител  во врем  остановки компрессора. При этом воздух в холодильнике и его содержимое подвергаегс  высушиванию в меньшей степени. Формула изобретени . Рабочее тело, состо щее из неазотропных веществ на основе фреона 15114 дл  домашних холодильников, отличающ е е с   тем, что, с цепью обеспечени  соответствующих температур испарени , оно дополнительно содержит следующие |)реоны из р да К13, RlSBl, R 22, К 115 при следующем соотношении компонентов , вес. ч. Ria 0,85-0,95 R114/ Т 13В 1 0,5 -0,8 0,4-0,7 Т 22 Б114/ ,2-0,45 Источники информации, прин тые во внимание при экспертизе: 1, Авторское свидетельство 153866, кл. С О9 К 3/О2, 1961.In order to ensure that the average evaporation tempos and the required temperatures in the refrigerator sections reach the required suction pressure (about 1 atm) and the allowable liquefaction pressure, these non-ehropropic mixtures are poured into the cold unit of the two-temperature cooler at all .. higher concentrations. : o; ::, tse ggratdki. In each case, C1Lei of the working fluid depends on the pumping volume, solubility of both components of the mixture in engine oil, on the degree of insulation of the refrigerator sections in the range of variation of external temperatures. Example. The cooling mixture expanded in the throttling device begins to evaporate at the inlet to the aiargel of the deep-cooling section at a low temperature, depending on the evaporation pressure and on the final separation of the mixture. As heat flows in and further evaporates, the temperature of the mixture gradually rises due to a constant change in composition, as a result of which it leaves the heater with a higher temperature and does not evaporate completely. At this temperature, the mixture of wet vapors enters the evaporator section with a normal degree of cooling, where the process of temperature increase continues under the influence of further heat influx. The mixture of working fluid leaves the evaporator section with a normal degree of cooling with a somewhat lower temperature than the hectare that is in this section and is in the vapor state. Without taking into account the effect of the cooling engine oil, the vapor mixture has the same concentration as the liquid mixture before throttling. The vapor mixture is sucked off by the compressor, compressed and liquefied in a condenser, where the mixture of varying composition passes through the entire temperature interval and then with the same concentration enters the throttle device. The advantages of the proposed working fluid are that, on the basis of the simple Yx3 circulation circuit of the working fluid, a two-temperature refrigerator can work, in which the temperature reaches (-18) C in the deep cooling section and, in the section with normal cooling degree, it is possible automatic defrosting of the evaporator during the phase of stopping the compressor, and there is no need for additional energy and relatively high air humidity and low power consumption, due to the thermodynamic points of interest are the ratios of the temperature difference between the evaporators and the condenser. In addition, the small difference between the temperature in the room and in the evaporator section with a normal degree of cooling in the larger measure ensures that the evaporator is defrosting when the compressor is stopped. At the same time, the air in the refrigerator and its contents are dried to a lesser extent. Claims. The working fluid consisting of non-azotropic substances on the basis of freon 15114 for household refrigerators, is different from the fact that, with a chain of ensuring appropriate evaporation temperatures, it additionally contains the following factors from the series K13, RlSBl, R 22, K 115 in the following ratio of components, weight. h. Ria 0.85-0.95 R114 / T 13B 1 0.5-0.8 0.4-0.7 T 22 B114 /, 2-0.45 Sources of information taken into account during the examination: 1 , Copyright certificate 153866, cl. C O9 C 3 / O2, 1961.
SU752113034A 1971-03-23 1975-03-14 Working body SU632717A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DD15395671 1971-03-23

Publications (1)

Publication Number Publication Date
SU632717A1 true SU632717A1 (en) 1978-11-15

Family

ID=5483626

Family Applications (1)

Application Number Title Priority Date Filing Date
SU752113034A SU632717A1 (en) 1971-03-23 1975-03-14 Working body

Country Status (7)

Country Link
BG (1) BG25238A3 (en)
CS (1) CS174829B2 (en)
DE (1) DE2203728A1 (en)
FR (1) FR2130556B1 (en)
RO (1) RO62413A (en)
SE (1) SE379093B (en)
SU (1) SU632717A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5918787A (en) * 1982-07-21 1984-01-31 Daiei Yakuhin Kogyo Kk Fron type refrigerant
JPS59147075A (en) * 1983-02-12 1984-08-23 Daiee Shokuhin Kogyo Kk Freon refrigerant

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2474151A1 (en) * 1980-01-21 1981-07-24 Inst Francais Du Petrole METHOD OF PRODUCING HEAT USING A HEAT PUMP USING A SPECIFIC MIXTURE OF FLUIDS AS A WORKING AGENT
AT392570B (en) * 1980-10-16 1991-04-25 Vni Ex K I Elektro METHOD FOR FREEZING AND STORING PRODUCTS AND REFRIGERANTS FOR THEIR IMPLEMENTATION
US4580415A (en) * 1983-04-22 1986-04-08 Mitsubishi Denki Kabushiki Kaisha Dual refrigerant cooling system
FR2554571A1 (en) * 1983-11-04 1985-05-10 Inst Francais Du Petrole Method of heat exchange between a hot and cold fluid using a fluid mixture as the heat-carrying medium and producing a circulation of the heat-carrying medium by capillary attraction
KR860002704A (en) * 1984-09-06 1986-04-28 야마시다 도시히꼬 Heat pump
US5049296A (en) * 1989-01-28 1991-09-17 Chujun Gu Working media for a thermodynamic engineering device operating in accordance with the Gu thermodynamic cycle
FR2682683B1 (en) * 1991-10-22 1994-01-14 Froilabo NON AZEOTROPE REFRIGERANT MIXTURE.

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5918787A (en) * 1982-07-21 1984-01-31 Daiei Yakuhin Kogyo Kk Fron type refrigerant
JPS59147075A (en) * 1983-02-12 1984-08-23 Daiee Shokuhin Kogyo Kk Freon refrigerant
JPH0254391B2 (en) * 1983-02-12 1990-11-21 Daiee Shokuhin Kogyo Kk

Also Published As

Publication number Publication date
FR2130556A1 (en) 1972-11-03
CS174829B2 (en) 1977-04-29
BG25238A3 (en) 1978-08-10
FR2130556B1 (en) 1974-09-13
RO62413A (en) 1977-11-15
SE379093B (en) 1975-09-22
DE2203728A1 (en) 1972-09-28

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