KR0136205Y1 - Absorptive type airconditioner - Google Patents

Absorptive type airconditioner Download PDF

Info

Publication number
KR0136205Y1
KR0136205Y1 KR2019950001486U KR19950001486U KR0136205Y1 KR 0136205 Y1 KR0136205 Y1 KR 0136205Y1 KR 2019950001486 U KR2019950001486 U KR 2019950001486U KR 19950001486 U KR19950001486 U KR 19950001486U KR 0136205 Y1 KR0136205 Y1 KR 0136205Y1
Authority
KR
South Korea
Prior art keywords
heat
cooling
absorption
refrigerant
absorber
Prior art date
Application number
KR2019950001486U
Other languages
Korean (ko)
Other versions
KR960027565U (en
Inventor
이인배
Original Assignee
김광호
삼성전자주식회사
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 김광호, 삼성전자주식회사 filed Critical 김광호
Priority to KR2019950001486U priority Critical patent/KR0136205Y1/en
Publication of KR960027565U publication Critical patent/KR960027565U/en
Application granted granted Critical
Publication of KR0136205Y1 publication Critical patent/KR0136205Y1/en

Links

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
    • F25B15/02Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • F25B15/06Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide
    • 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
    • F25B2315/00Sorption refrigeration cycles or details thereof
    • F25B2315/006Reversible sorption cycles
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/01Geometry problems, e.g. for reducing size
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/228Heat exchange with fan or pump

Abstract

본 고안은 리튬브로마이드 수용액등을 사용하여 냉난방은 물론 냉온수공급기능을 갖는 흡수식 냉난방기에 관한 것으로서, 적어도 연소열에 의해 가열을 행하는 발생기, 응축기, 증발기, 용액열교환기 및 흡수기를 갖춘 흡수식 냉난방기에 있어서, 냉매의 응축에 따라 발생된 응축열 및 흡수기(29)내에서 냉매의 흡수에 따라 발생된 흡수열이 하나의 열교환기(22)에서 냉각되도록 하여 응축기내에서 냉매의 응축에 따른 응축열 및 흡수기내에서 용액이 냉매를 흡수할때 발생되는 흡수열을 냉각시킨 냉각수를 하나의 열교환기에서 냉각시킴으로써 설비전체를 소형화할 수 있고, 특히 냉각수가 반복적으로 순환됨으로써 냉각수를 보충할 필요가 없으므로 관리가 용이하게 될 뿐만 아니라 냉각효율이 향상되는 것이다.The present invention relates to an absorption type air conditioner having a cooling / heating function as well as a cold / hot water supply function using a lithium bromide aqueous solution, and the like, at least in a generator of a heating type, a condenser, an evaporator, a solution heat exchanger, and an absorber, which are heated by combustion heat, The heat of condensation generated by the condensation of the refrigerant and the heat of absorption generated by the absorption of the refrigerant in the absorber 29 is cooled in one heat exchanger 22 so that the solution in the condenser and the absorber of the condensation of the refrigerant in the condenser is cooled. The whole plant can be miniaturized by cooling the cooling water cooled by the absorption heat generated when absorbing the refrigerant in one heat exchanger. Especially, since the cooling water is repeatedly circulated, it is not necessary to replenish the cooling water. Cooling efficiency is improved.

Description

흡수식 냉난방기Absorption air conditioner

제1도는 종래 흡수식 냉난방기의 일예를 나타내는 개략도.1 is a schematic view showing an example of a conventional absorption type air conditioner.

제2도는 종래 흡수식 냉난방기의 다른예를 나타내는 개략도.2 is a schematic view showing another example of a conventional absorption type air conditioner.

제3도는 본 고안이 적용된 흡수식 냉난방기의 전체구성을 나타내는 개략도이다.3 is a schematic view showing the overall configuration of the absorption type air conditioner to which the present invention is applied.

* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings

22 : 열교환기 22a : 응축기22: heat exchanger 22a: condenser

22b : 간냉기 29 : 흡수기22b: intercooler 29: absorber

33 : 냉각수관 34 : 냉각팬33: cooling water pipe 34: cooling fan

본 고안은 리튬브로마이드수용액등을 사용하여 냉난방은 물론 냉온수공급기능을 갖는 흡수식 냉난방기에 관한 것으로서, 특히 응축기 및 흡수기에서 발생된 응축열 및 흡수열을 하나의 열교환기에서 냉각시키도록된 흡수식 냉난방기에 관한 것이다.The present invention relates to an absorption type air conditioner using lithium bromide aqueous solution and the like as well as cooling and heating as well as a cooling and hot water supply function. In particular, the present invention relates to an absorption type air conditioner configured to cool condensation heat and absorption heat generated in a condenser and an absorber in one heat exchanger. .

종래의 흡수식 냉난방기는 제1도에 도시한 바와같이 발생기(1)에서는 버너(1a)에서 가스등을 연소시켜 가열을 행하면 냉매를 흡수시킨 희용액에서 냉매증기와 농용액을 발생시키게 되며, 상기 발생기(1)에서 발생된 냉매증기는 분리되어 응축기(2)에서 액화냉매로 응축된후 팽창밸브(3)에서 소정의 압력으로 감압되어 증발기(4)로 보내지며, 상기 증발기(4)내로 유입된 액화냉매는 증발하면서 냉각작용을 행하여 실내기(5)에서 냉방이 이루어지게되며, 상기 증발기(4)내에서 증발된 냉매는 흡수기(6)내로 유입되어 진다.As shown in FIG. 1, the conventional absorption type air conditioner generates a refrigerant vapor and a concentrated solution in a rare solution in which the refrigerant is absorbed when the generator 1 burns a gas or the like in the burner 1a and heats it. The refrigerant vapor generated in 1) is separated, condensed into liquefied refrigerant in the condenser (2), decompressed to a predetermined pressure in the expansion valve (3) and sent to the evaporator (4), the liquefaction introduced into the evaporator (4) The coolant performs cooling while evaporating, thereby cooling the indoor unit 5, and the coolant evaporated in the evaporator 4 is introduced into the absorber 6.

한편, 상기 발생기(1)에서 냉매증기를 방출한 고온의 농용액은 용액열교환기(7)에서 희용액과 열교환된후 온도가 낮추어져 상기 흡수기(6)내로 공급되며, 상기 흡수기(6)내로 공그된 농용액은 증발기(4)내에서 증발된 냉매를 흡수하여 희용액으로 되는데 이때에는 다량의 흡수열이 발생하게 되며, 이 흡수열은 흡수기(6)내에 설치된 냉각수관(8)을 흐르는 냉각수에 의해 냉각되어지고, 상기 흡수기(6)내에서 흡수열에 의해 가열된 냉각수관(8)내에 냉각수는 별도의 냉각탑(9)에서 또 다른 냉각수에 의해 냉각되도록 구성되어 있다.On the other hand, the hot concentrated solution which discharged the refrigerant vapor from the generator (1) is heat-exchanged with the rare solution in the solution heat exchanger (7) is lowered in temperature and supplied into the absorber (6), into the absorber (6) The concentrated agricultural solution absorbs the refrigerant evaporated in the evaporator 4 to form a rare solution. In this case, a large amount of heat of absorption is generated, and the heat of absorption is the cooling water flowing through the cooling water pipe 8 installed in the absorber 6. The cooling water in the cooling water pipe 8 which is cooled by the heat exchanger in the absorber 6 and heated by absorption heat is configured to be cooled by another cooling water in a separate cooling tower 9.

그러나, 이와같은 흡수식 냉난방기에서는 응축기(2) 및 흡수기에서 발생된 열을 수냉식으로 냉각시킴에 따라 별도의 냉각탑등의 장치를 필요로함에 따라 설비전체의 크기가 대형화될 뿐만 아니라 배관등이 복잡하게되고, 특히 주기적으로 냉각수를 보충하여야 하는 등의 문제점들이 내재되어 있었따.However, in this type of absorption air conditioner, as the heat generated by the condenser 2 and the absorber is cooled by water, it requires a separate cooling tower or the like, which not only increases the size of the entire facility but also complicates the piping. In particular, problems such as the need to replenish the cooling water periodically are inherent.

종래에도 이런점에 비추어서 공기에 의해 냉각을 행하는 흡수식 냉난방기가 제안되어 있는데, 이는 제2도에 도시한 바와같이 응축기(2) 및 흡수기(6)의 일측에 각각 냉각핀(10a)(10b)을 설치하고, 상기 응축기(2) 및 흡수기(6)에서 발생된 응축열 및 흡수열을 냉각팬(10a)(10b)의 작동에 따라 발생되는 공기에 의해 냉각시키도록 구성되어 있다.Conventionally, in view of this, an absorption type air conditioner for cooling by air has been proposed. As shown in FIG. 2, cooling fins 10a and 10b are provided on one side of the condenser 2 and the absorber 6, respectively. And condensation heat and absorption heat generated in the condenser 2 and the absorber 6 are cooled by air generated by the operation of the cooling fans 10a and 10b.

그러나, 이와같은 종래의 흡수식 냉난방기는 설비전체의 크기는 어느정도 줄일 수 있으나, 물보다 공기의 열전단율이 작음에 따라 수냉식과 동일한 냉각효과를 얻기 위해서는 응축기 및 흡수기의 전열면적을 크게 형성시켜야 함으로써 설비전체의 크기를 소형화하기 어려울 뿐만 아니라 만족할 만한 냉각효과를 얻을 수 없다고 하는 ㄷㅇ의 여러가지 문제점들이 있었다.However, the conventional absorption type air conditioner can reduce the size of the entire installation to some extent, but the heat transfer rate of the air is smaller than that of water, so that the heat transfer area of the condenser and the absorber must be large to obtain the same cooling effect as the water cooling type. In addition to the difficulty of miniaturizing the size of the system, there were various problems of ㅇ that the satisfactory cooling effect could not be obtained.

본 고안은 상술한 바와같은 종래기술의 문제점들을 해결하기 위하여 안출된 것으로서,본 고안의 목적은 하나의 열교환기에서 응축기 및 흡수기에서 발생된 응축열 및 흡수열을 냉각시켜 설비전체를 소형화하는 것이 가능케됨과 동시에 냉각효율을 현저하게 향상시킬 수 있는 흡수식 냉난방기를 제공하는데 있다.The present invention has been made to solve the problems of the prior art as described above, the object of the present invention is to cool down the condensation heat and absorption heat generated in the condenser and absorber in one heat exchanger and to make the whole size of the installation and At the same time to provide an absorption air-conditioner that can significantly improve the cooling efficiency.

이와같은 목적을 실현하기 위하여 이루어진 본 고안에 따른 흡수식 냉난방기는 적어도 연소열에 의해 가열을 행하는 발생기, 응축기, 증발기, 용액열교환기 및 흡수기를 갖춘 흡수식 냉난방기에 있어서, 냉매의 응축에 따라 발생된 응축열 및 흡수기내에서 냉매의 흡수에 따라 발생된 흡수열이 하나의 열교환기에서 냉각되도록 하여 응축기내에서 냉매의 응축에 따른 응축열 및 흡수기내에서 용액이 냉매를 흡수할때 발생되는 흡수열을 냉각시킨 냉각수를 하나의 열교환기에서 냉각시킴으로써 설비전체를 소형화할 수 있고, 특히 냉각수가 반복적으로 순환됨으로써 냉각수를 보충할 필요가 없으므로 관리가 용이하게 될 뿐만 아니라 냉각효율이 향상되는 것을 그 특징으로 한다.Absorption air conditioner according to the present invention made to achieve this purpose is an absorption air-conditioner equipped with a generator, a condenser, an evaporator, a solution heat exchanger and an absorber for heating by at least combustion heat, the heat of condensation and absorption generated by the condensation of the refrigerant The heat of absorption generated by the absorption of refrigerant in the aircraft is cooled in one heat exchanger, so that the heat of condensation due to the condensation of the refrigerant in the condenser and the cooling water that cools the absorption of heat generated when the solution absorbs the refrigerant in the absorber. By cooling in the heat exchanger of the entire facility can be miniaturized, in particular, because the cooling water is repeatedly circulated, it is not necessary to replenish the cooling water, it is characterized by not only easy management but also improved cooling efficiency.

이하, 본 고안의 바람직한 실시예를 첨부된 도면 제3도에 따라서 더욱 상세하게 설명한다.Hereinafter, preferred embodiments of the present invention will be described in more detail with reference to FIG. 3.

도면에서 부호(20)은 버너(20a)의 연소열에 의해 가열된 용액중에서 냉매증기 및 농용액을 발생시키는 발생기를 나타내고 있다.In the figure, reference numeral 20 denotes a generator for generating refrigerant vapor and a concentrated solution in a solution heated by the heat of combustion of the burner 20a.

상기 발생기(20)의 일측에는 냉매증기관(21)을 통하여 유입된 냉매증기를 응축시키는 열교환기(22)가 설치되어 있고, 상기 열교환기(22)에서 응축된 액화냉매는 팽창밸브(23)에서 충분하게 감압된후 증발기(24)에서 증발되도록 구성되어 있다.One side of the generator 20 is provided with a heat exchanger 22 for condensing the refrigerant vapor introduced through the refrigerant steam engine 21, the liquefied refrigerant condensed in the heat exchanger 22 is expanded in the expansion valve (23) It is configured to evaporate in the evaporator 24 after sufficiently depressurizing.

그리고, 상기 증발기(24)내에서 증발되지 않은 냉매는 냉매순환펌프(25)의 작동에 따라 순환되면서 증발이 이루어지게 되며, 상기 증발기(24)내에는 냉매의 증발작용에 따라 냉각되어 실내기(26)에서 냉방이 이루어지도록 하는 냉수관(27)이 설치되어 있다.In addition, the refrigerant not evaporated in the evaporator 24 is circulated according to the operation of the refrigerant circulation pump 25, and evaporation is performed. The evaporator 24 is cooled according to the evaporation of the refrigerant, and the indoor unit 26 is cooled. ) Is provided with a cold water pipe 27 for cooling.

한편, 상기 증발기(24)의 일측에는 증발된 냉매가 분리판(28)을 통하여 유입되는 흡수기(29)가 형성되어 있으며, 상기 흡수기(29)내로는 발생기(20)에서 발생된 농용액이 용액열교환기(30)에서 희용액과 열교환된후 유입되어 농용액순환펌프(31)의 작동에 따라 순환되어지고, 상기 흡수기(29)내에서 냉매를 흡수함에 따라 발생된 흡수열은 냉각수순환펌프(32)의 작동에 따라 순환되는 냉각수관(33)내의 냉각수에 의해 냉각되어 진다.Meanwhile, an absorber 29 is formed at one side of the evaporator 24 through which the evaporated refrigerant flows through the separator 28, and the concentrated solution generated from the generator 20 is a solution in the absorber 29. After exchanged with the rare solution in the heat exchanger (30), it is circulated according to the operation of the agricultural liquid circulation pump (31), and the heat of absorption generated by absorbing the refrigerant in the absorber (29) is a cooling water circulation pump ( It is cooled by the cooling water in the cooling water pipe 33 circulated in accordance with the operation of 32).

그리고, 상기 흡수기(29)내에서 발생되는 흡수열에 의해 가열된 냉각수는 상기 열교환기(22)에서 냉각되어 진다.In addition, the cooling water heated by the absorption heat generated in the absorber 29 is cooled in the heat exchanger 22.

상기 열교환기(22)는 발생기(20)내에서 발생된 냉매증기를 응축시키는 응축기(22a)와, 상기 흡수기(29)내에서 흡수열에 의해 가열된 냉각수를 냉각시키는 간냉기(22b)로 이루어지며, 그 일측에는 상기 응축기(22a)에서 발생되는 응축열 및 흡수기(29)내에서 흡수열에 의해 가열된 냉각수를 냉각시키기 위한 냉각팬(34)이 모터등의 구동수단에 의해 회전되도록 구성되어 있다.The heat exchanger 22 is composed of a condenser 22a for condensing the refrigerant vapor generated in the generator 20, and an intercooler 22b for cooling the cooling water heated by absorption heat in the absorber 29, On one side, a cooling fan 34 for cooling the cooling water heated by the heat of absorption in the absorber 29 and the condensation heat generated by the condenser 22a is configured to rotate by a driving means such as a motor.

한편, 상기 발생기(20)와 흡수기(29)에는 발생기(20)내에서 발생된 농용액이 용액열교환기(30)에서 열교환된후 흡수기(29)내로 유입되도록 하는 농용액관(35)이 접속됨과 동시에 흡수기(29)내의 희용액을 희용액공급펌프(36)의 작동에 따라 용액열교환기(30)에서 열교환시킨후 상기 발생기(20)로 공급하는 희용액관(37)이 각각 접속되어 있다.On the other hand, the generator 20 and the absorber 29 is connected to the agricultural liquid pipe 35 so that the concentrated solution generated in the generator 20 is heat-exchanged in the solution heat exchanger 30 and then introduced into the absorber 29. At the same time, the rare liquid pipes 37 for supplying the rare solution in the absorber 29 to the generator 20 after heat exchange in the solution heat exchanger 30 in accordance with the operation of the rare solution supply pump 36 are connected. .

다음에 이와같이 구성된 본 고안에 따른 흡수식 냉난방기에 대한 작용 및 효과를 설명한다.Next will be described the action and effect on the absorption type air conditioner according to the present invention configured as described above.

먼저, 버너(20a)에서 가해지는 연소열에 의해 발생기(20)내의 용액이 가열되면 고온의 냉매증기와 농용액이 발생되고, 상기 발생기(20)에서 발생된 냉매증기는 냉매증기관(21)을 통하여 열교환기(22)의 응축기(22a)에서 응축된후 팽창밸브(23)에서 충분한 감압이 이루어져 증발기(24)로 보내진다.First, when the solution in the generator 20 is heated by the combustion heat applied by the burner 20a, a high temperature refrigerant vapor and a concentrated solution are generated, and the refrigerant vapor generated in the generator 20 is passed through the refrigerant vapor engine 21. After condensation in the condenser 22a of the heat exchanger 22, a sufficient pressure reduction is performed in the expansion valve 23 and sent to the evaporator 24.

그리고, 상기 증발기(24)내로 보내진 냉매는 냉매순환펌프(25)의 작동에 따라 순환되면서 증발이 이루어지면 냉수관(27)내의 냉수가 냉가되면서 실내기(26)에서는 냉방이 이루어지게 되는 것이다.In addition, when the refrigerant sent into the evaporator 24 is circulated according to the operation of the refrigerant circulation pump 25 and evaporation is performed, cooling is performed in the indoor unit 26 while the cold water in the cold water pipe 27 cools.

한편, 상기 발생기(20)내에서 발생된 고온의 농용액은 농용액관(35)을 통하여 흡수기(29)내로 유입되는데, 이때 상기 농용액관(35)을 통하여 유통되는 농용액은 용액열교환기(30)에서 희용액과 열교환이 이루어진후 흡수기(29)내로 유입되어 진다.On the other hand, the hot agricultural solution generated in the generator 20 is introduced into the absorber 29 through the agricultural liquid pipe 35, wherein the agricultural liquid circulated through the agricultural liquid pipe 35 is a solution heat exchanger In 30, after the heat exchange with the rare solution is introduced into the absorber (29).

그리고, 상기 흡수기(29)내로 유입된 농용액은 농용액순환펌프(31)의 작동에 따라 순환되면서 분사됨과 동시에 증발기(24)내에서 증발되어 분리판(28)을 통하여 유입된 냉매를 흡수하게되며, 이때 상기 증발기(24)에서 유입된 냉매를 흡수함에 따라 발생된 흡수열은 냉각수관(33)내로 순환되는 냉각수에 의해 냉각된후 희용액공급펌프(36)의 작동에 따라 희용액관(37)을 통하여 유통되어 용액열교환기(30)에서 농용액과 열교환된후 발생기(20)내로 공급되어 진다.In addition, the agricultural liquid introduced into the absorber 29 is circulated in accordance with the operation of the agricultural liquid circulation pump 31 and is sprayed while being evaporated in the evaporator 24 to absorb the refrigerant introduced through the separator 28. At this time, the absorption heat generated by absorbing the refrigerant introduced from the evaporator 24 is cooled by the cooling water circulated into the cooling water pipe 33 and then the rare water pipe (operation of the rare liquid supply pump 36). It is distributed through 37) and is heat-exchanged with the concentrated solution in the solution heat exchanger 30 and then supplied into the generator 20.

한편, 상기 흡수기(29)내에서 발생된 흡수열을 냉각시킨 냉각수는 냉각수순환펌프(32)의 작동에 따라 냉각수관(33)을 통하여 유통되어 열교환기(22), 즉 간냉기(22b)내로 유입되고, 상기 간냉기(22b)내에서는 냉각팬(34)의 작동에 따라 생성된 공기에 의해 냉각된후 다시 흡수기(29)내로 공급되는 작용을 반복적으로 행하게 되는 것이다.On the other hand, the cooling water cooling the absorption heat generated in the absorber 29 is distributed through the cooling water pipe 33 in accordance with the operation of the cooling water circulation pump 32 and into the heat exchanger 22, that is, intercooler 22b. In the intercooler 22b, the air is cooled by the air generated by the operation of the cooling fan 34 and then supplied to the absorber 29 again.

이때, 상기 냉각팬(34)의 작동에 따라 생성된 냉각공기는 간냉기(22b)내로 순환되는 냉각수를 냉각시킴과 동시에 냉매의 응축에 따라 응축열이 방열되는 응축기(22a)를 냉각시키게 됨으로써 냉각효율이 향상되는 것이다.At this time, the cooling air generated by the operation of the cooling fan 34 cools the cooling water circulated into the intercooler 22b and at the same time cools the condenser 22a in which the heat of condensation is radiated according to the condensation of the refrigerant. This is to be improved.

상술한 바와같이 본 고안에 따른 흡수식 냉난방기에 의하면, 응축기내에서 냉매의 응축에 따른 응축열 및 흡수기내에서 용액이 냉매를 흡수할때 발생되는 흡수열을 냉각시킨 냉각수를 하나의 열교환기에서 냉각시킴으로써 설비전체를 소형화할 수 있고, 특히 냉각수가 반복적으로 순환됨으로써 냉각수를 보충할 필요가 없으므로 관리가 용이하게 될 뿐만 아니라 냉각효율이 향상되는 등의 탁월한 이점을 갖는 것이다.As described above, according to the absorption type air conditioner according to the present invention, an apparatus is provided by cooling a condenser heat resulting from condensation of a refrigerant in a condenser and a cooling water cooling the absorption heat generated when a solution absorbs the refrigerant in the absorber in one heat exchanger. Since the whole can be downsized, in particular, since the coolant is repeatedly circulated, there is no need to replenish the coolant, thereby facilitating management and improving the cooling efficiency.

Claims (1)

적어도 연소실에 의해 가열을 행하는 발생기, 응축기, 증발기, 용액열교환기 및 흡수기를 갖춘 흡수식 냉난방기에 있어서, 상기 발생기(20)에서 발생된 냉매를 공급받아 응축시키는 응축기(22a)와, 상기 흡입기(29)내로 냉각수를 순환시키는 냉각수관(33)이 접속된 간냉기(22b)와, 상기 응축기(22a) 및 간냉기(22b)로 냉각공기를 공급하여 상기 응축기(22a)내에서 냉매의 응축에 따라 발생된 응축열과 상기 흡수기(29)내에서 냉매의 흡수에 따라 발생된 흡수열을 동시 냉각시키는 냉각팬(34)으로 이루어진 하나의 열교환기(22)를 포함을 특징으로 하는 흡수식 냉난방기.In an absorption type air conditioner having at least a generator, a condenser, an evaporator, a solution heat exchanger, and an absorber for heating by a combustion chamber, a condenser (22a) for receiving and condensing the refrigerant generated in the generator (20), and the inhaler (29) The intercooler 22b to which the coolant pipe 33 circulates the coolant is connected, and the cooling air is supplied to the condenser 22a and the intercooler 22b to generate coolant condensation in the condenser 22a. And a heat exchanger (22) comprising a cooling fan (34) for simultaneously cooling the condensed heat and the absorption heat generated by the absorption of the refrigerant in the absorber (29).
KR2019950001486U 1995-01-28 1995-01-28 Absorptive type airconditioner KR0136205Y1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR2019950001486U KR0136205Y1 (en) 1995-01-28 1995-01-28 Absorptive type airconditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR2019950001486U KR0136205Y1 (en) 1995-01-28 1995-01-28 Absorptive type airconditioner

Publications (2)

Publication Number Publication Date
KR960027565U KR960027565U (en) 1996-08-17
KR0136205Y1 true KR0136205Y1 (en) 1999-03-20

Family

ID=19407355

Family Applications (1)

Application Number Title Priority Date Filing Date
KR2019950001486U KR0136205Y1 (en) 1995-01-28 1995-01-28 Absorptive type airconditioner

Country Status (1)

Country Link
KR (1) KR0136205Y1 (en)

Also Published As

Publication number Publication date
KR960027565U (en) 1996-08-17

Similar Documents

Publication Publication Date Title
US4439999A (en) Absorption type refrigeration system
EP0470432B1 (en) Absorption apparatus for cooling a fluid
KR0136205Y1 (en) Absorptive type airconditioner
KR101699905B1 (en) Absorption chiller system having fuel cell
JPH09159300A (en) Air cooling absorption heat pump chiller using ammonia-water absorption cycle
CN210814603U (en) Energy-saving white-removing system for hot and wet flue gas
KR200230604Y1 (en) Absorption Cooler Using Solar Heat
JP4100462B2 (en) Heat utilization system
JPH05280825A (en) Absorption heat pump
JPH0854156A (en) Cooling and heating device utilizing exhaust heat of engine and operating method thereof
KR0177714B1 (en) Gax cycle absorptive refrigerator
KR0137580Y1 (en) Cooling apparatus of liquid refrigerator absorptive airconditioner
JP3145215B2 (en) Evaporation and absorption device in absorption refrigerator
JPS61167429A (en) Regenerating method of liquid moisture-absorbent in air-conditioning equipment
JPS5849872A (en) Heat pump device
KR200288627Y1 (en) a device of cooling and heating water to suction method for high degree of efficiency
KR0139349Y1 (en) Circulation of condensed water of evaporator for absorption type refrigerator
JPS5944498B2 (en) Exhaust heat utilization equipment
KR200276965Y1 (en) Evaporative air conditioner
KR0177715B1 (en) Hot water supplying absorptive type refrigerator
JPS5924134A (en) Calorimeter for air conditioner
KR0139287Y1 (en) Absorptive type airconditioner
JPS6446541A (en) Two-phase flow refrigerant circulation type air-conditioning system
JP3311926B2 (en) Absorption air conditioner
JPS6024894B2 (en) Absorption heat pump device

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
REGI Registration of establishment
FPAY Annual fee payment

Payment date: 20051028

Year of fee payment: 8

LAPS Lapse due to unpaid annual fee