KR0117045Y1 - Generator for absorption type air-conditioner - Google Patents

Generator for absorption type air-conditioner

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Publication number
KR0117045Y1
KR0117045Y1 KR2019940011020U KR19940011020U KR0117045Y1 KR 0117045 Y1 KR0117045 Y1 KR 0117045Y1 KR 2019940011020 U KR2019940011020 U KR 2019940011020U KR 19940011020 U KR19940011020 U KR 19940011020U KR 0117045 Y1 KR0117045 Y1 KR 0117045Y1
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KR
South Korea
Prior art keywords
solution
generator
refrigerant
supplied
rare
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KR2019940011020U
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Korean (ko)
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KR950033926U (en
Inventor
이승갑
김봉인
은석현
Original Assignee
김광호
삼성전자 주식회사
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Priority to KR2019940011020U priority Critical patent/KR0117045Y1/en
Publication of KR950033926U publication Critical patent/KR950033926U/en
Application granted granted Critical
Publication of KR0117045Y1 publication Critical patent/KR0117045Y1/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
    • 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
    • F25B41/00Fluid-circulation arrangements
    • F25B41/40Fluid line arrangements
    • 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
    • F25B2315/001Crystallization prevention
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/04Refrigeration circuit bypassing means
    • 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
    • F25B2500/22Preventing, detecting or repairing leaks of refrigeration fluids
    • F25B2500/221Preventing leaks from developing
    • 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

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

본 고안은 희용액을 농용액과 냉매증기로 분리시키는 흡수식 냉난방기의 발생기에 관한 것으로써, 냉매증기관(70)에 용액이 함유되지 않은 냉매증기가 공급되도록 상부저장조(13)와 하부저장조(12) 사이에 용액을 바이패스시키는 바이패스수단(20)이 배설된 것을 특징으로 한다. 이와같이 구성된 본 고안은 냉매증기관에 냉매증기만이 공급되어 시스템의 안전성을 보다 향상시킬 수 있는 것은 물론이고, 시스템의 정지시에 농용액의 결정석출현상이 방지되어 냉난방의 효율을 보다 향상시킬 수 있다는 효과가 있다.The present invention relates to a generator of an absorption type air conditioner that separates a rare solution into a concentrated solution and a refrigerant vapor. The upper storage tank (13) and the lower storage tank (12) are supplied with a refrigerant vapor containing no solution to the refrigerant vapor engine (70). Bypass means for bypassing the solution 20 is characterized in that it is disposed. The present invention configured as described above can not only improve the safety of the system by supplying the refrigerant steam to the refrigerant steam engine but also improve the efficiency of cooling and heating by preventing the precipitation of crystallization of the farm solution when the system is stopped. It works.

Description

흡수식 냉난방기의 발생기Generator of absorption air conditioner

제1도는 종래예에 적용되는 흡수식 냉난방기의 발생기의 내부구조를 개략적으로 도시한 내부구조도.1 is an internal structure diagram schematically showing an internal structure of a generator of an absorption type air conditioner applied to a conventional example.

제2도는 본 고안에 적용되는 흡수식 냉난방기의 구성을 개략적으로 도시한 구성도.Figure 2 is a schematic diagram showing the configuration of an absorption type air conditioner applied to the present invention.

제3도는 본 고안에 적용되는 발생기의 내부구조를 개략적으로 도시한 내부구조도.Figure 3 is an internal structure diagram schematically showing the internal structure of the generator applied to the present invention.

제4도는 제3도의 A-A부분을 절결하여 그 평면을 개략적으로 도시한 평면도.FIG. 4 is a plan view schematically illustrating the plane of the A-A section of FIG.

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

10:발생기11:열발생수단10: generator 11: heat generating means

12:하부저장조13:상부저장조12: lower reservoir 13: upper reservoir

14:양액관15:기액분리수단14: nutrient solution pipe 15: gas-liquid separation means

20:바이패스수단30;배기수단20: bypass means 30; exhaust means

31:배기 가스조절부재32:배기통로31: exhaust gas regulating member 32: exhaust passage

33:팬부재40:응축기33: fan member 40: condenser

50:증발기60:흡수기50: evaporator 60: absorber

70:냉매증기관80:농용액관70: refrigerant increase engine 80: agricultural liquid pipe

90:희용액관90: solution tube

본 고안은 리튬브로마이드수용액(Lithium Bromide Solution)을 이용하여 냉난방을 출력시키는 흡수식 냉난방기에 있어서 희용액을 농용액과 냉매증기로 분리시키는 흡수식 냉난방기의 발생기에 관한 것으로써, 특히 용액이 응축기로 유출되는 것을 방지하여 시스템의 안전성을 확보함과 동시에 시스템의 정지시 농용액의 결정석출을 방지할 수 있는 흡수식 냉난방기의 발생기에 관한 것이다.The present invention relates to a generator of an absorption type air conditioner that separates a rare solution into a concentrated solution and a refrigerant vapor in an absorption type air conditioner that outputs cooling and heating by using a lithium bromide solution. The present invention relates to a generator of an absorption type air conditioner which can prevent the crystal precipitation of agricultural liquids when the system is stopped while at the same time ensuring the safety of the system.

일반적으로 리튬브로마이드수용액(Lithium Bromide Solution)을 이용하여서 냉난방을 출력시키는 흡수식 냉난방기는 여러가지 형태로 다양하게 제안되어 있다.In general, absorption type air conditioners for outputting heating and cooling by using lithium bromide solution have been proposed in various forms.

이러한 종래의 흡수식 냉난방기는 희용액을 농용액과 냉매증기로 분리시키는 발생기와, 상기 발생기에서 분리된 냉매증기를 응축시키는 응축기와, 상기 응축기에서 응축된 냉매액을 증발시키는 증발기와, 상기 증발기에서 증발된 냉매증기가 상기 발생기에서 분리된 농용액에 흡수되도록 하여서 희용액으로 변환시키는 흡수기로 이루어져서 냉난방의 출력을 발생시킨다.The conventional absorption type air conditioner includes a generator for separating a rare solution into a concentrated solution and a refrigerant vapor, a condenser for condensing the refrigerant vapor separated from the generator, an evaporator for evaporating the refrigerant liquid condensed in the condenser, and an evaporator in the evaporator. The refrigerant vapor thus obtained is absorbed by the concentrated solution separated from the generator, and is converted into a rare solution to generate an output of cooling and heating.

또, 이와 같이 희용액을 농용액과 냉매증기로 분리시키는 종래의 흡수식 냉난방기의 발생기는, 제1도에 도시한 바와같이 흡수기에서 변환된 희용액의 흐름을 가이드하는 희용액관(2)과, 상기 희용액관(2)을 통과한 희용액이 저장되는 하부저장조(3)와, 상기 하부저장조(3)에 저장된 희용액이 충만되며 양단이 개방되고 외주에 다수의 전열핀(71)이 배설된 다수의 양액관(7)과, 상기 양액관(7)에 충만된 희용액이 가열되도록 열을 발생시키는 열발생수단(1)과, 상기 열발생수단(1)으로부터 발생되는 열에 의해 가열된 희용액을 농용액과 냉매증기로 분리시키는 기액분리기(6)와, 상기 기액분리기(6)가 배설되며 상기 기액분리기(6)에 의해 분리된 냉매증기가 응축기로 공급되도록 냉매증기의 흐름을 가이드하는 냉매증기관(9)이 배설됨과 동시에 상기 기액분리기(6)에서 분리된 농용액이 흡수기로 공급되도록 농용액의 흐름을 가이드하는 농용액관(8)이 배설된 상부저장조(5)로 이루어진다.In addition, the generator of the conventional absorption type air conditioner that separates the rare solution into the concentrated solution and the refrigerant vapor includes a rare solution tube (2) for guiding the flow of the rare solution converted in the absorber as shown in FIG. The lower storage tank (3) storing the rare solution passed through the rare solution tube (2) is filled with the rare solution stored in the lower storage tank (3), both ends are open, and a plurality of heat transfer fins (71) are disposed on the outer circumference. A plurality of nutrient solution tubes (7), heat generating means (1) for generating heat to heat the rare solution filled in the nutrient solution tube (7), and heated by heat generated from the heat generating means (1) The gas-liquid separator 6 which separates the rare solution into the concentrated solution and the refrigerant vapor, and the gas-liquid separator 6 are disposed, and guide the flow of the refrigerant vapor so that the refrigerant vapor separated by the gas-liquid separator 6 is supplied to the condenser. At the same time the refrigerant vapor pipe (9) is disposed and the gas-liquid separator ( It consists of an upper reservoir (5) in which the agricultural liquid pipe (8) for guiding the flow of the agricultural liquid so that the agricultural liquid separated in 6) is supplied to the absorber.

또, 상기 튜브부재(7)의 하부는 상기 하부저장조(3)에 고착된 하부홀더(31)에 의해서 지지되고, 상기 튜브부재(7)의 상부는 상기 상부저장조(4)에 고착된 상부홀더(41)에 의해 지지된다.In addition, a lower portion of the tube member 7 is supported by a lower holder 31 fixed to the lower reservoir 3, and an upper portion of the tube member 7 is fixed to the upper reservoir 4. It is supported by 41.

또한, 상기 튜브부재(7)의 상단부는 상기 상부홀더(41)의 상면보다 상부로 돌출되어 있다.In addition, the upper end of the tube member 7 protrudes upward from the upper surface of the upper holder 41.

이와 같은, 종래의 흡수식 냉난방기의 발생기는, 흡수기에서 변환된 희용액이 상기 희용액관(2)을 통해서 상기 하부저장조(3)로 공급되고, 상기 하부저장조(3)에 희용액이 계속적으로 공급되면 다수의 상기 양액관(7)의 내부에 희용액이 충만되며, 상기 양액관(7)의 내부에 공급된 희용액은 상기 열발생수단(1)에서 발생되는 열에 의해서 가열된다.In the generator of the conventional absorption type air conditioner, the rare solution converted in the absorber is supplied to the lower reservoir 3 through the rare solution tube 2, and the rare solution is continuously supplied to the lower reservoir 3. Then, the rare solution is filled in the plurality of nutrient solution tubes 7, and the rare solution supplied to the nutrient solution tube 7 is heated by the heat generated by the heat generating means 1.

또, 상기 양액관(7)에 공급된 희용액은 상기 열발생수단(1)에서 발생되는 열에 의해서 가열되어 농용액과 냉매증기 상태로 분리된다.In addition, the rare solution supplied to the nutrient solution tube 7 is heated by heat generated by the heat generating means 1 to be separated into a concentrated solution and a refrigerant vapor state.

즉, 상기 열발생수단(1)의 열에 의해서 상부저장조(4)로 이동한 냉매증기는 상기 상부저장조(5)에 배설된 냉매증기관(9)에 가이드되어서 응축기로 공급되고, 농용액은 상기 상부저장조(5)에 배설된 농용액관(8)에 가이드되어서 흡수기로 공급된다.That is, the refrigerant vapor moved to the upper storage tank (4) by the heat of the heat generating means (1) is guided to the refrigerant steam pipe (9) disposed in the upper storage tank (5) is supplied to the condenser, the agricultural solution is the upper portion It is guided to the agricultural liquid pipe 8 arrange | positioned at the storage tank 5, and is supplied to an absorber.

이때, 상기 열발생수단(1)에서 과다한 열이 발생되면 상기 양액관(7)을 통해 상부저장조(5)로 과다한 양의 용액이 공급되며 상기 상부저장조(5)에 배설된 냉매증기관(9)을 통해 응축기로 공급되었다.At this time, when excessive heat is generated in the heat generating means (1), the excess amount of solution is supplied to the upper reservoir (5) through the nutrient solution pipe (7) and the refrigerant increasing pipe (9) disposed in the upper reservoir (5) Through a condenser.

즉, 종래의 발생기는 용액의 일부가 상기 냉매증기관(9)을 거쳐서 응축기로 공급되어 시스템의 효율을 저하시키는 등의 안전성을 저하시켰다.That is, in the conventional generator, a part of the solution is supplied to the condenser through the refrigerant vapor condenser 9 to deteriorate safety such as lowering the efficiency of the system.

또, 종래의 발생기는 동작이 정지될경우 희용액으로부터 분리된 농용액의 일부가 상기 상부홀더(41)에 잔류되게 되고, 상기 상부홀더(41)에 잔류된 농용액이 결정으로 석출되어 농용액의 농도가 짙게되므로써 흡수기에서 보다 많은 냉매증기가 흡수되지 못해 흡수효율의 저하 등으로 냉난방의 효율이 저하되었다.In addition, in the conventional generator, when the operation is stopped, a part of the farm solution separated from the rare solution is left in the upper holder 41, and the farm solution remaining in the upper holder 41 is precipitated as a crystal, and the farm solution. As the concentration of was increased, the refrigerant vapor was not absorbed more by the absorber, and the efficiency of cooling and heating was lowered due to the decrease in absorption efficiency.

즉, 종래의 흡수식 냉난방기 발생기는 용액의 일부가 응축기로 공급되어 시스템의 안전성을 저하시키는 것은 물론, 시스템의 가동이 정지될 경우 농용액이 결정으로 석출되어 냉난방의 효율을 저하시킨다는 등의 여러가지 문제점들이 있었다.That is, in the conventional absorption type air conditioner generator, a portion of the solution is supplied to the condenser to reduce the safety of the system, and when the system is stopped, the farm solution precipitates as crystals, which lowers the efficiency of heating and cooling. there was.

본 고안은 상술한 여러가지 문제점들을 감안해서 이루어진 것으로써, 본 고안의 목적은 응축기로 냉매증기만이 공급되도록 하여 시스템의 안전성을 향상시킴과 동시에, 농용액의 결정석출현상을 방지하여 냉난방의 효율을 보다 향상시킬 수 있는 흡수식 냉난방기의 발생기를 제공하는데 있다.The present invention has been made in view of the above-mentioned problems, and an object of the present invention is to improve the safety of the system by supplying only the refrigerant vapor to the condenser, and to prevent crystal precipitation of agricultural solutions, thereby improving the efficiency of heating and cooling. It is to provide a generator of the absorption air conditioner that can be further improved.

이와 같은 목적을 달성하기 위하여 본 고안에 의한 흡수식 냉난방기의 발생기는, 희용액관이 배설된 하부저장조와, 상기 하부저장조에 배설된 희용액관을 통해서 희용액이 공급되는 양액관과, 상기 양액관에 공급된 희용액을 냉매증기와 농용액으로 분리시키기 위해서 열을 발생시키는 열발생수단과, 상기 열발생수단으로부터 발생된 열에 의해서 분리된 냉매증기의 흐름을 가이드하는 냉매증기관 및 농용액의 흐름을 가이드하는 농용액관이 배설된 상부저장조로 이루어진 흡수식 냉난방기의 발생기에 있어서, 상기 냉매증기관으로 용액이 함유되지 않은 냉매증기가 공급되도록 상기 상부저장조와 상기 하부저장조 사이에 용액을 바이패스시키는 바이패스수단이 배설된 것을 특징으로 한다.In order to achieve the above object, the generator of the absorption type air conditioner according to the present invention includes: a nutrient solution pipe in which a rare solution is supplied through a lower storage tank in which a rare solution pipe is disposed, and a rare solution tube disposed in the lower storage tank, and the nutrient solution tube The heat generating means for generating heat to separate the rare solution supplied to the refrigerant vapor and the concentrated solution, and the flow of the refrigerant vapor engine and the agricultural liquid for guiding the flow of the refrigerant vapor separated by the heat generated from the heat generating means. In the generator of the absorption type air conditioner consisting of an upper storage tank to guide the agricultural liquid pipe to guide, the bypass means for bypassing the solution between the upper reservoir and the lower reservoir so that the refrigerant vapor containing no solution is supplied to the refrigerant steam pipe. It is characterized by the excretion.

이와 같은 본 고안에 의한 흡수식 냉난방기의 발생기에 의하면, 상부저장조와 하부저장조 사이에 용액을 바이패스시키는 바이패스수단이 배설되므로써 냉매증기관으로 냉매증기만이 공급되어 시스템의 안전성을 보다 향상시킬 수 있는 것이다.According to the generator of the absorption type air conditioner according to the present invention, the bypass means for bypassing the solution is disposed between the upper reservoir and the lower reservoir, so that only the refrigerant vapor is supplied to the refrigerant steam engine, thereby improving the safety of the system. .

이하, 본 고안에 의한 흡수식 냉난방기의 발생기의 일실시예를 첨부 도면을 참조하여 상세하게 설명한다.Hereinafter, an embodiment of a generator of an absorption type air conditioner according to the present invention will be described in detail with reference to the accompanying drawings.

제2도는 본 고안에 적용되는 흡수식 냉난방기의 구성을 개략적으로 도시한 구성도이고, 제3도는 본 고안에 적용되는 발생기의 내부구조를 개략적으로 도시한 내부구조도이며, 제4도는 제3도의 A-A부분을 절결하여 그 평면을 개략적으로 도시한 평면도이다.Figure 2 is a schematic diagram showing the configuration of the absorption type air conditioner applied to the present invention, Figure 3 is an internal structure diagram schematically showing the internal structure of the generator applied to the present invention, Figure 4 is a part AA of Figure 3 Is a plan view schematically showing the plane by cutting out.

제2도 내지 제4도에 있어서, (10)은 발생기로써, 흡수기(60)에서 변환된 희용액을 농용액과 냉매증기를 분리시켜서 농용액은 상기 흡수기(60)에 공급하고 냉매증기는 응축기(40)로 공급한다.In FIGS. 2 to 4, reference numeral 10 denotes a generator in which the rare solution converted in the absorber 60 is separated from the concentrated solution and the refrigerant vapor so that the concentrated solution is supplied to the absorber 60 and the refrigerant vapor is a condenser. Supply to 40.

또, 상기 발생기(10)는, 상기 흡수기(60)에서 변환된 희용액의 흐름을 가이드하는 희용액관(90)과, 상기 희용액관(90)을 통과한 희용액이 저장되도록 공간을 형성시키는 하부저장조(12)와, 상기 하부저장조(12)에 저장된 희용액이 충만되며 양단이 개방되고 외주에 다수의 전열핀(141)이 배설된 다수의 양액관(14)과, 상기 양액관(14)에 충만된 희용액이 가열되도록 열을 발생시키는 열발생수단(11)과, 상기 열발생수단(11)으로 부터 발생되는 열에 의해서 희용액을 농용액과 냉매증기로 분리시키는 기액분리수단(15)과, 상기 기액분리수단(15)이 배설되며 상기 기액분리수단(15)에 의해 분리된 냉매증기가 상기 응축기(40)로 공급되도록 냉매증기의 흐름을 가이드하는 냉매증기관(70)이 배설됨과 동시에 상기 기액분리수단(15)에 의해서 분리된 농용액이 상기 흡수기(60)로 공급되도록 농용액의 흐름을 가이드하는 농용액관(80)이 배설된 상부저장조(13)로 이루어진다.In addition, the generator 10 forms a space such that a rare solution tube 90 that guides the flow of the rare solution converted by the absorber 60 and a rare solution that has passed through the rare solution tube 90 are stored. And a plurality of nutrient solution tubes 14 filled with a lower storage tank 12, a rare solution stored in the lower storage tank 12, both ends of which are open, and a plurality of heat transfer fins 141 disposed on an outer circumference thereof. Heat generating means 11 for generating heat so that the rare solution filled in 14 is heated, and gas-liquid separation means for separating the rare solution into a concentrated solution and a refrigerant vapor by heat generated from the heat generating means 11 ( 15) and a refrigerant vapor pipe 70 for guiding the flow of refrigerant vapor so that the gas-liquid separation means 15 is disposed and the refrigerant vapor separated by the gas-liquid separation means 15 is supplied to the condenser 40. At the same time the concentrated solution separated by the gas-liquid separation means 15 is the absorber (60) Supplied to the upper reservoir comprises a 13 perch solution pipe 80 for guiding the flow of the discharged solution is sea bass.

또한, 상기 상부저장조(13)와 상기 하부저장조(12) 사이에는, 상기 열발생수단(11)으로부터 과다한 열이 발생되거나 혹은, 상기 양액관(14)에 과다한 희용액이 충만될 경우 등과 같이 상기 상부저장조(13)에 용액이 과다하게 존재할 경우에 상기 상부저장조(13)의 용액이 상기 냉매증기관(70)을 통해 상기 응축기(40)로 공급되지 않도록 용액을 바이패스시키는 바이패스수단(20)이 배설되어 있다.In addition, between the upper reservoir 13 and the lower reservoir 12, such as when excessive heat is generated from the heat generating means 11, or when the excess solution is filled in the nutrient solution tube 14, such as Bypass means 20 for bypassing the solution so that the solution of the upper reservoir 13 is not supplied to the condenser 40 through the refrigerant inlet pipe 70 when the solution is excessively present in the upper reservoir 13. This is excreted.

즉, 상기 상부저장조(13)와 상기 하부저장조(12) 사이에는 바이패스수단(20)이 배설되어서 용액을 상기 하부저장조(12)로 바이패스시키므로써, 냉매증기만이 상기 냉매증기관(70)을 통해 상기 응축기(40)로 공급되는 것이다.That is, the bypass means 20 is disposed between the upper reservoir 13 and the lower reservoir 12 to bypass the solution to the lower reservoir 12, so that only the refrigerant steam is the refrigerant vapor engine 70. It is supplied to the condenser 40 through.

또, 상기 양액관(14)의 하부는 상기 하부저장조(12)에 고착된 하부홀더(121)에 의해서 지지되고, 상기 양액관(14)의 상부는 상기 상부저장조(13)에 고착된 상부홀더(131)에 의해 지지되어있다.In addition, a lower portion of the nutrient solution tube 14 is supported by a lower holder 121 fixed to the lower reservoir 12, and an upper portion of the nutrient solution tube 14 is fixed to the upper reservoir 13. 131 is supported by.

또한, 상기 양액관(14)의 상단부는 상기 상부홀더(131)의 상면보다도 돌설되어 있으며, 다수개의 상기 양액관(14)중의 일부 양액관(14)의 상단부는 상기 발생기(10)가 정지될 경우 농용액의 잔류를 방지하기 위하여 상기 상부홀더(131)와 동일한 높이에 지지되어 있다.In addition, the upper end of the nutrient solution tube 14 is more protruding than the upper surface of the upper holder 131, the upper end of some of the nutrient solution tube 14 of the plurality of nutrient solution tube 14 is the generator 10 is stopped In this case, it is supported at the same height as the upper holder 131 to prevent the remaining of the agricultural solution.

즉, 상기 양액관(14)의 일부는 시스템의 정지시 상기 상부홀더(131)의 상면에 농용액의 잔류를 방지하도록 상기 상부홀더(14)와 동일한 높이로 지지되어서 농용액의 결정석출현상을 방지한다.That is, a part of the nutrient solution tube 14 is supported at the same height as the upper holder 14 to prevent the remaining of the agricultural solution on the upper surface of the upper holder 131 when the system is stopped to prevent crystallization of the agricultural solution. prevent.

한편, 상기 발생기(10)에는 상기 열발생수단(11)의 연소에 의해서 발생되는 가스를 배기시키는 배기수단(30)이 장착된다.On the other hand, the generator 10 is equipped with an exhaust means 30 for exhausting the gas generated by the combustion of the heat generating means (11).

즉, 상기 배기수단(30)은 상기 열발생수단(11)의 연소에 의해서 발생되는 가스의 흐름을 가이드하는 배기통로(32)와, 상기 배기통로(32)로 가이드되는 가스의 양을 제어하는 가스조절부재(31)와, 상기 배기통로(32)로 가이드되는 가스가 외부로 토출되도록 흡인력을 발생시키는 팬부재(33)로 이루어져서, 상기 열발생수단(11)의 연소에 의해서 발생되는 가스를 외부로 방출시킨다.That is, the exhaust means 30 controls the exhaust passage 32 for guiding the flow of gas generated by the combustion of the heat generating means 11 and the amount of gas guided to the exhaust passage 32. Gas control member 31 and the fan member 33 for generating a suction force so that the gas guided to the exhaust passage 32 is discharged to the outside, the gas generated by the combustion of the heat generating means 11 Release to the outside.

한편, 도면에서 미설명 부호(50)은 증발기로써, 상기 응축기(40)에서 응축된 냉매액을 증발시킨다.In the drawing, reference numeral 50 denotes an evaporator, which evaporates the refrigerant liquid condensed in the condenser 40.

다음에, 상기와 같이 구성된 본 고안에 의한 흡수식 냉난방기의 증발기의 작용효과를 설명한다.Next, the effect of the evaporator of the absorption type air conditioner according to the present invention configured as described above will be described.

먼저, 시스템이 가동되면 상기 흡수기(60)에서는 냉매증기가 농용액에 흡수되어 희용액으로 변환되고, 상기 흡수기(60)에서 변환된 희용액은 상기 희용액관(90)에 가이드되어 상기 발생기(10)의 하부저장조(12)로 공급된다.First, when the system is operated, the refrigerant vapor is absorbed into the concentrated solution in the absorber 60 and converted into the rare solution. The rare solution converted by the absorber 60 is guided to the rare solution tube 90 to generate the generator ( 10 is supplied to the lower reservoir (12).

또, 상기 하부저장조(12)로 희용액이 계속적으로 공급되면 상기 양액관(14)의 내부에 희용액이 공급되고, 도시되지 않은 제어수단의 제어신호에 의해서 상기 열발생수단(11)으로부터 열이 발생된다.In addition, when the rare solution is continuously supplied to the lower reservoir 12, the rare solution is supplied into the nutrient solution tube 14, and heat is generated from the heat generating means 11 by a control signal of a control means (not shown). Is generated.

또한, 상기 열발생수단(11)의 열에 의해서 상기 양액관(14)에 공급된 희용액은 가열되고, 이 가열된 희용액은 상기 상부저장조(13)에 배설된 상기 기액분리수단(15)에 의해서 농용액과 냉매증기로 분리된다.In addition, the rare solution supplied to the nutrient solution tube 14 is heated by the heat of the heat generating means 11, and the heated rare solution is supplied to the gas-liquid separation means 15 disposed in the upper reservoir 13. It is separated into the concentrated solution and the refrigerant vapor.

이때, 상기 상부저장조(13)로 과다한 양의 용액이 공급될 경우에는, 농용액관(8)을 통해 흡수기로 보내어지고, 나머지 용액은 상기 상부저장조(13)와 하부저장조(12)에 삽입된 바이패스수단(20)에 가이드되어서 상기 하부저장조(12)로 바이패스된다.In this case, when an excessive amount of the solution is supplied to the upper reservoir 13, it is sent to the absorber through the concentrated liquid tube 8, the remaining solution is inserted into the upper reservoir 13 and the lower reservoir 12 Guided by the bypass means 20 is bypassed to the lower reservoir (12).

즉, 상기 기액분리수단(15)에 의해서 분리된 냉매증기는 상기 상부저장조(13)에 배설된 상기 냉매증기관(70)에 가이드되어서 상기 응축기(40)로 공급되고, 농용액은 상기 상부저장조(13)에 배설된 상기 농용액관(80)에 가이드되어서 상기 흡수기(60)로 공급됨과 동시에, 과다하게 상기 상부저장조(13)에 공급된 용액은 상기 바이패스수단(20)에 가이드되어서 상기 하부저장조(12)로 바이패스된다.That is, the refrigerant vapor separated by the gas-liquid separation means 15 is guided to the refrigerant steam pipe 70 disposed in the upper storage tank 13 to be supplied to the condenser 40, and the agricultural liquid is supplied to the upper storage tank ( The solution supplied to the absorber 60 while being guided to the agricultural liquid pipe 80 disposed at 13) and excessively supplied to the upper reservoir 13 is guided to the bypass means 20 to the lower portion. Bypass into the reservoir (12).

또, 상기 응축기(40)로 공급된 냉매증기는 응축되어 냉매액으로 변환되고, 상기 응축기(40)에서 변환된 냉매액은 상기 증발기(50)에서 증발되어 흡수기(60)에서 희용액으로 변환되고, 상기 흡수기(60)에서 변환된 희용액은 상기 희용액관(90)을 통해서 상기 발생기(10)로 공급되어 순환된다.In addition, the refrigerant vapor supplied to the condenser 40 is condensed and converted into a refrigerant liquid, and the refrigerant liquid converted by the condenser 40 is evaporated in the evaporator 50 and converted into a rare solution in the absorber 60. The rare solution converted by the absorber 60 is supplied to the generator 10 through the rare solution tube 90 and circulated.

즉, 상기 바이패스수단(20)은 상기 상부저장조(13)에 과다한 양의 용액이 공급될 경우에 용액을 상기 하부저장조(12)로 바이패스시키므로써, 상기 응축기(40)에는 용액이 함유되지 않은 냉매증기만이 공급되어 원활한 응축작용이 일어나 시스템을 안정화됨은 물론, 냉난방 효율을 보다 향상되는 것이다.That is, the bypass means 20 bypasses the solution to the lower reservoir 12 when an excessive amount of the solution is supplied to the upper reservoir 13 so that the condenser 40 does not contain the solution. Not only refrigerant vapor is supplied, so that smooth condensation occurs to stabilize the system, as well as to improve the heating and cooling efficiency.

한편, 시스템의 가동이 정지될 경우에는 상기 튜브부재(14)의 일부가 상기 상부홀더(131)의 상면과 동일한 높이로 위치되어 상기 상부홀더(131)의 상면에는 농용액이 잔류되지 않게된다.On the other hand, when the operation of the system is stopped, a portion of the tube member 14 is positioned at the same height as the upper surface of the upper holder 131 so that the agricultural solution does not remain on the upper surface of the upper holder 131.

즉, 시스템의 정지시에는 상기 상부홀더(131)에 잔류된 농용액이 상기 양액관(14)을 통해서 상기 하부저장조(12)로 흘러내려 상기 하부저장조(12)에 저장된 희용액에 희석되게 된다.That is, when the system is stopped, the agricultural solution remaining in the upper holder 131 flows into the lower reservoir 12 through the nutrient solution tube 14 to be diluted in the rare solution stored in the lower reservoir 12. .

이로 인해서, 농용액의 결정석출현상이 방지되고, 농용액의 결정석출의 방지로 인해서 냉난방의 효율을 보다 향상시켜 품질을 보다 고급화시킬 수 있는 것이다.As a result, the crystal precipitation phenomenon of the agricultural solution is prevented, and the crystallization of the agricultural solution is prevented, thereby improving the efficiency of cooling and heating, thereby improving the quality.

앞에서 설명한 바와 같이, 본 고안에 의한 흡수식 냉난방기의 발생기에 의하면, 상부저장조와 하부저장조 사이에 용액을 바이패스시키는 바이패스수단이 배설되어 있으므로, 냉매증기관에는 냉매증기만이 공급되어 시스템의 안전성을 보다 향상시킬 수 있는 것은 물론이고, 시스템의 정지시에 농용액의 결정석출현상이 방지되어 냉난방의 효율을 보다 향상시킬 수 있다는 매우 실용적인 효과가 있는 것이다.As described above, according to the generator of the absorption type air conditioner according to the present invention, since a bypass means for bypassing the solution is provided between the upper reservoir and the lower reservoir, only the refrigerant steam is supplied to the refrigerant steam engine, thereby improving the safety of the system. Of course, there is a very practical effect that it is possible to improve the efficiency of cooling and heating, as well as to prevent the precipitation of crystallization of the concentrated solution at the time of stopping the system.

Claims (2)

희용액관(90)이 배설된 하부저장조(12)와, 상기 하부저장조(12)에 배설된 희용액관(90)을 통해서 희용액이 공급되는 양액관(14)과, 상기 양액관(14)에 공급된 희용액을 냉매증기와 농용액으로 분리시키기 위해서 열을 발생시키는 열발생수단(11)과, 상기 열발생수단(11)으로부터 발생된 열에 의해서 분리된 냉매증기의 흐름을 가이드하는 냉매증기관(70) 및 농용액의 흐름을 가이드하는 농용액관(80)이 배설된 상부저장조(13)로 이루어진 흡수식 냉난방기의 발생기에 있어서, 상기 냉매증기관(70)에 용액이 함유되지 않은 냉매증기가 공급되도록 상기 상부저장조(13)와 상기 하부저장조(12) 사이에 용액을 바이패스시키는 바이패스수단(20)이 배설된 것을 특징으로 하는 흡수식 냉난방기의 발생기.A lower storage tank 12 in which the rare liquid pipe 90 is disposed, a nutrient solution tube 14 through which the rare solution is supplied through the rare solution tube 90 disposed in the lower storage tank 12, and the nutrient solution tube 14 The heat generating means 11 for generating heat to separate the rare solution supplied to the refrigerant into the concentrated solution and the refrigerant, and the refrigerant guiding the flow of the refrigerant vapor separated by the heat generated from the heat generating means (11) In the generator of the absorption type air conditioner composed of a steam pipe (70) and an upper reservoir (13) provided with a farm liquid pipe (80) for guiding the flow of the farm liquid, the refrigerant vapor containing no solution in the refrigerant steam pipe (70) Generator of the absorption type air conditioner, characterized in that the bypass means for bypassing the solution is disposed between the upper reservoir (13) and the lower reservoir (12) to be supplied. 제1항에 있어서, 상기 양액관(14)의 일부는 시스템의 정지시 상부홀더(131)의 상면에 농용액의 잔류를 방지하도록 상부홀더(131)와 동일한 높이로 위치되는 것을 특징으로 하는 흡수식 냉난방기의 발생기.2. The absorption type according to claim 1, wherein a part of the nutrient solution tube 14 is positioned at the same height as the upper holder 131 so as to prevent the residual liquid from remaining on the upper surface of the upper holder 131 when the system is stopped. Generator of air conditioners.
KR2019940011020U 1994-05-17 1994-05-17 Generator for absorption type air-conditioner KR0117045Y1 (en)

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KR0117045Y1 true KR0117045Y1 (en) 1998-06-15

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