KR200323227Y1 - A absorption solution refining filter unified cool-hot water supply implement - Google Patents

A absorption solution refining filter unified cool-hot water supply implement Download PDF

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KR200323227Y1
KR200323227Y1 KR20-2003-0012007U KR20030012007U KR200323227Y1 KR 200323227 Y1 KR200323227 Y1 KR 200323227Y1 KR 20030012007 U KR20030012007 U KR 20030012007U KR 200323227 Y1 KR200323227 Y1 KR 200323227Y1
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solution
vacuum valve
filter
hot water
absorber
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KR20-2003-0012007U
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Korean (ko)
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양우석
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(주)비룡
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    • 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
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/003Filters
    • 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
    • F25B41/20Disposition of valves, e.g. of on-off valves or flow control valves

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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)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Materials Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

흡수용액의 정제필터와 냉,온수기를 일체화시켜 장시간 운전으로 인한 진공 누수로 발생되는 용액오염 문제를 없애도록 한 흡수용액 정제여과기 일체형 냉,온수기에 관한 것으로, 흡수기(1)내의 흡수액이 용액펌프(2)와 진공밸브(7)를 통해 유입되는 배관(11)을 가지고 있는 여과용기(9)에는 내부측 상부에 격판(19)을 두고 평균공경 0.1마이크로미터의 미세 다공막으로 형성된 중공사형 외압식 여과기가 격판(19)상부로 개구부(18)를 가지고 여러개가 밀폐배열 형성됨과 아울러 여과용기(9) 상부로는 진공밸브(8)를 가지는 질소가스 또는 수도수를 유입하는 역세배관(15)과 흡수기로 보내는 진공밸브(12)를 가지는 토출배관(16)으로 구성되고 여과용기(9) 하부로는 진공밸브(10)를 가지는 철 및 구리의 산화물 등의 찌꺼기를 역세하기 위한 배출배관(17)으로 구성된다.Absorption solution purification filter integrated cold and hot water unit to eliminate the problem of solution contamination caused by vacuum leakage due to long time operation by integrating the filter and the cold and hot water of the absorbent solution, the absorber in the absorber (1) is a solution pump ( 2) and the filtration vessel (9) having a pipe (11) flowing through the vacuum valve (7) has a diaphragm (19) with a diaphragm (19) on top of the inner side formed of a microporous membrane having an average pore diameter of 0.1 micrometer The filter has an opening 18 above the diaphragm 19 and a plurality of hermetic arrays are formed, and the back washing pipe 15 for introducing nitrogen gas or tap water having a vacuum valve 8 above the filter container 9 and A discharge pipe (17) composed of a discharge pipe (16) having a vacuum valve (12) sent to the absorber and having a vacuum valve (10) below the filter container (9) for backwashing debris such as iron and copper oxides. Consisting of .

Description

흡수용액 정제여과기 일체형 냉,온수기{A absorption solution refining filter unified cool-hot water supply implement}Absorption solution refining filter unified cool-hot water supply implement

본 고안은 리튬브로마이드를 흡수액으로 사용하고 있는 냉,온수기에서 흡수용액의 정제필터와 냉,온수기를 일체화시켜 장시간 운전으로 인한 진공 누수로 발생되는 용액오염 문제를 없애도록 한 흡수용액 정제여과기 일체형 냉,온수기에 관한 것이다.The present invention integrates the refining filter of the absorbing solution and the cold and hot water in the cold and hot water machine using lithium bromide as the absorbing liquid to eliminate the solution contamination problem caused by vacuum leakage due to long time operation. It is about a water heater.

흡수식 냉,온수기는 국내에서 년간 1500여대가 보급되고 있으나 용액오염으로 인한 기계의 성능저하와 기기의 수명 단축 및 여러 가지 문제가 있는 실정이다.Absorption cold and hot water heaters have been widely distributed in Korea for 1,500 years.

따라서 이러한 문제를 없애기 위하여서는 용액을 냉,온수기장치 내에서 자체 정제여과 할 수 있는 장치가 어느 때보다도 필요하다고 할 수 있다.Therefore, in order to eliminate this problem, it can be said that a device that can purify the solution itself in the cold and hot water device is more necessary than ever.

이러한 흡수액 정제여과기 일체형 냉,온수기의 구성을 살펴보면 용액의 흐름방식에 따라 직렬흐름, 리버스흐름 및 직,병렬 병용 흐름방식 등으로 구분되며 국내에서는 직렬흐름방식과 병렬흐름방식이 주로 사용되고 있다.Looking at the structure of the absorption liquid filter filter integrated cold, water heaters are divided into a series flow, reverse flow and series, parallel combined flow method according to the flow of the solution, and the serial flow and parallel flow method is mainly used in Korea.

도 1은 본 고안이 적용된 직렬흐름방식의 흡수식 냉,온수기를 나타내고 있으며, 도시된 바와 같이 흡수기(1)에서 나온 묽은 용액은 용액펌프(2)에 의해 저온 열교환기(3)와 고온열교환기(4)를 거처 고온재생기(5)로 들어간다. 여기서 묽은 용액은 냉매를 발생시킨후 농도가 진해져서 중간용액이 되어 고온열교환기(4)에서 저온의 묽은 용액과 열교환된다. 그 후 저온재생기(6)에서는 다시 고온재생기(5)에서 발생된 고온의 냉매증기에 의해 가열되어 냉매를 발생시킨후 더욱 농도가 진한 용액 상태가 되어 저온열교환기(3)를 거쳐 흡수기(1)로 되돌아온다.1 shows an absorption cold and hot water heater of a series flow method to which the present invention is applied, and as shown, the dilute solution from the absorber 1 is connected to a low temperature heat exchanger 3 and a high temperature heat exchanger by a solution pump 2. 4) to enter the high temperature regenerator (5). Here, the diluted solution becomes a medium solution by increasing the concentration after generating the refrigerant, and heat-exchanges with the diluted solution of low temperature in the high temperature heat exchanger (4). Thereafter, the low temperature regenerator 6 is heated again by the high temperature refrigerant vapor generated in the high temperature regenerator 5 to generate the refrigerant, and then to a deeper solution state. The absorber 1 passes through the low temperature heat exchanger 3. Return to

도 2는 본 고안이 적용된 병렬흐름방식의 흡수식 냉,온수기를 나타내고 있으며, 도시된 바와 같이 흡수기(1)에서 나온 묽은 용액은 용액펌프(2)에 의해 저온열교환기(3)를 거쳐 일부용액은 고온열교환기(4)를 통해 고온재생기(5)로 보내지고 또 다른 일부용액은 직접 저온재생기(6)로 유입돼서 각각 냉매를 발생시킨후 진한용액과 중간용액으로 되어 진한 용액은 고온 열교환기(4)를 통하고, 또한 저온재생기(6)에서의 중간용액은 직접 저온열교환기(3)로 와서 묽은 용액과 열교환한 후 흡수기(1)로 되돌아온다2 shows a parallel flow type absorption cold and hot water heater to which the present invention is applied, and as shown, a dilute solution from the absorber 1 is passed through a low temperature heat exchanger 3 by a solution pump 2, It is sent to the high temperature regenerator (5) through the high temperature heat exchanger (4) and another part of the solution is introduced directly to the low temperature regenerator (6) to generate a refrigerant, respectively, and the thick solution and the intermediate solution into a thick solution is a high temperature heat exchanger ( 4), and the intermediate solution in the low temperature regenerator (6) comes directly to the low temperature heat exchanger (3), heat exchanges with the dilute solution, and then returns to the absorber (1).

이상의 흐름에서 흡수제로 사용되는 리튬브로마이드(LiBr) 용액은 액체상태로 존재하며 냉매(H2O)는 액체 및 기체상태로 흡수식 냉온수기 장치내에서 공존하고 있다. 흡수액내의 증기압이 기체상태의 증기압보다 낮을 경우 경계면에서 흡수현상이 일어나게 된다. 흡수현상에서 발생된 열은 온도구배를 형성시켜 열전달이 일어난다.In the above flow, the lithium bromide (LiBr) solution used as the absorbent exists in the liquid state, and the refrigerant (H 2 O) coexists in the absorption type cold and hot water device in the liquid and gaseous state. If the vapor pressure in the absorbent liquid is lower than the vapor pressure in the gaseous state, absorption occurs at the interface. Heat generated in the absorption phenomenon forms a temperature gradient, causing heat transfer.

흡수액으로 사용되는 리튬브로마이드(LiBr) 용액은 식염수와 유사한 화학적 성질을 가지고 있어 금속에 대한 부식이 아주 민감하여 이에 대한 관리가 아주 중요하다.Lithium bromide (LiBr) solution used as absorbent liquid has chemical properties similar to that of saline solution, so it is very sensitive to metal corrosion and management is very important.

냉,온수기가 진공상태로 흡수액과 냉매가 순환되면서 장치를 구성하고 있는 순환경로에서 철과 구리재질과 접촉하면서 철 및 구리산화물이 발생하게 된다.Iron and copper oxides are generated as the cold and hot water come into contact with iron and copper materials in a circulation path constituting the device as the absorbent liquid and the refrigerant circulate in a vacuum state.

이같이 발생된 산화물을 제거하지 않으면 차츰 농도가 높아지게 되고 그로 인하여 순환경로에 스케일 형성과 펌프에 동부착현상 등 여러가지 문제를 야기시킨다.Failure to remove these oxides will lead to higher concentrations, which can lead to problems such as scale formation in the circulation paths and eastern phenomena in the pumps.

냉,온수기의 적절한 운전을 위해서는 수년마다 흡수액의 교체나 약품정제를 하여야만 하게 되는데, 이때 진공상태의 기계내부로부터 액을 뽑아내기 위하여 일시적으로 질소가스를 사용하여 기계내부를 대기압 이상으로 하여 흡수액을 뽑아내어 회수, 수송, 화학처리반송, 진공유지 등과 같은 많은 공정을 거쳐야만 한다.For proper operation of cold and water heaters, it is necessary to replace absorbents or purify chemicals every few years. At this time, to extract the liquid from the inside of the machine under vacuum, the absorbent liquid is drawn out above the atmospheric pressure using nitrogen gas temporarily. It has to go through many processes such as recovery, transportation, chemical transfer and vacuum maintenance.

또한 냉,온수기를 재 가동할 때까지는 여러날이 소요되고 많은 노동력과 비용이 과다하게 지출되는 문제를 가지고 있다.In addition, it takes many days to restart the cold and hot water heaters, and a lot of labor and costs are excessively spent.

만일, 흡수액 교체나 약품정제 등의 처리를 하지 않으면 기계의 효율 저하로 인하 에너지 비용 증가와 기계 수명단축 등의 문제를 낳게 된다.If the absorbent solution is not replaced or the chemical refining is not performed, the efficiency of the machine may be lowered, resulting in an increase in energy cost and shortening of the machine life.

따라서 본 고안은 흡수용액 정제장치를 냉,온수기를 제작하는 시점에서 부착하는 일체식으로 냉,온수기를 제작하므로서 시운전 초기부터 기밀상태가 유지되면서 운전이 가능토록 하여 상기와 같은 제반 문제점을 해결함에 있다.Therefore, the present invention solves the above-mentioned problems by allowing the operation of the absorption solution refining device to be attached at the time of manufacturing the cold and hot water heaters, while maintaining the airtight state from the beginning of the trial run. .

상기의 목적을 달성하기 위한 본 고안의 구체적인 수단은, 흡수기내의 액이 용액펌프(2)와 진공밸브(7)를 통해 일부용액이 여과기 내로 들어오고 미세기공을 가지고 있는 특수재질의 외압식의 중공사막을 통과하면서 여과된 흡수용액이 진공밸브(12)를 통해 흡수기도 들어가고 아울러 역세용 질소가스 및 수도수용 역세관으로부터 역세된 용액을 회수처리하는 배관을 가지고 있는 여과용기로서 흡수액을 여과 정제 가능토록 하여서 이루어진다.Specific means of the present invention for achieving the above object, the liquid in the absorber through the solution pump (2) and the vacuum valve (7) some of the solution enters the filter and has a special material of the external pressure type The absorbent solution filtered while passing through the hollow fiber membrane enters the absorber through the vacuum valve 12, and also has a pipe for recovering the backwashed solution from the backwashing nitrogen gas and the water backwashing tube. It is done by doing so.

도 1은 본 고안이 적용된 직렬 흐름방식의 흡수식 냉,온수기의 구성도.1 is a configuration of the absorption type cold, water heater of the series flow method to which the present invention is applied.

도 2는 본 고안이 적용된 병렬 흐름방식의 흡수식 냉,온수기의 수성도.Figure 2 is an aqueous diagram of the absorption type cold, water heater of the parallel flow method to which the present invention is applied.

도 3은 본 고안에 적용되는 흡수용액 정체여과기의 구성도.Figure 3 is a block diagram of an absorption solution stabilizing filter applied to the present invention.

<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>

1 : 흡수기1: absorber

2 : 용액 펌프2: solution pump

9 : 여과용기9: filtration vessel

8,10,12 : 진공밸브8,10,12: vacuum valve

16 : 토출배관16 discharge pipe

17 : 배출배관17: discharge piping

18 : 개구부18: opening

19 : 격판19: diaphragm

이하, 첨부된 도면을 참조하여 본 고안의 바람직한 실시예를 상세히 설명한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도 3은 본 고안에 적용되는 흡수용액 정체여과기의 구성도이고, 도 3의 흡수용액 정체여과기가 적용된 예가 도 1,2에 도시되어 있다.3 is a configuration diagram of the absorbent solution static filter applied to the present invention, an example in which the absorbent solution static filter of FIG. 3 is illustrated in FIGS. 1 and 2.

도 1,2와 같이 흡수식 냉동기 및 냉,온수기에 여과정제장치를 일체형으로 부설함에 있어서, 본 고안은 흡수기(1)내의 용액이 용액펌프(2)와 진공밸브(7)를 통하여 유입되는 유입관(11)을 가지는 여과용기(9) 내부에는 상부에 격판(19)을 두고 평균공경 0.1마이크로미터의 미세다공막을 형성한 중공사형 고분자 필터(20)가 격판(19)상부로 개구부(18)를 가지고 여러개가 밀폐배열이 형성됨과 아울러 여과용기(9) 상부로 세정용 질소가스 및 수도수의 유입용 역세관로(15)를 구비하여 흡수기(1)로 보내지는 토출관(16)을 가짐과 동시에 여과용기(9) 하부로는 걸러진 찌꺼기를 배출하기 위한 배출관(17)을 가지며, 이 배출관(17)에는 배출량을 조정하는 진공밸브(10)를 가진다.1 and 2, the present invention provides an inlet tube through which the solution in the absorber 1 is introduced through the solution pump 2 and the vacuum valve 7 as shown in FIG. The hollow fiber-type polymer filter 20 having the diaphragm 19 at the top and the microporous membrane having an average pore diameter of 0.1 micrometer is formed inside the filtration container 9 having the opening 11. And a plurality of hermetic arrays are formed, and a discharge tube 16 which is sent to the absorber 1 is provided with a back washing pipe 15 for the inflow of nitrogen gas and tap water for washing in the upper part of the filtration vessel 9. At the same time, the lower part of the filtration vessel 9 has a discharge pipe 17 for discharging the filtered debris, and the discharge pipe 17 has a vacuum valve 10 for adjusting the discharge amount.

이상과 같이 구성된 본 고안의 작동상태를 보면 기계의 운전중에 유입된 미량의 산소가 리튬브로마이드 용액과 부식억제제 등과 반응하여 발생된 철 및 구리의 이온 및 산화물의 찌꺼기가 냉온수기 장치내에서 서서히 축적되거나 스케일이 형성되면서 기계의 성능 저하로 발전하거나 고장으로 진행되게 된다.According to the operating state of the present invention configured as described above, traces of iron and copper ions and oxides generated by reacting a small amount of oxygen introduced during operation of the machine with lithium bromide solution and corrosion inhibitor are gradually accumulated or scaled in the cold / hot water apparatus. As it is formed, the power generation of the machine is degraded or progressed to failure.

이때 진공밸브(7)를 통해 유입배관(11)으로 오염된 흡수액이 유입되어 고분자 필터(20)에서 철 및 구리산화물이 여과된다. 고분자 필터(20)에서 정제된 흡수액만이 중공사 내부에서 상부개구부(18)를 통해 유입되고 여과용기(9) 상부측으로 보내어져 진공밸브(12)를 가진 토출배관(16)을 통해 다시 흡수기로 보내지므로서 정제된 용액으로 사용되게 된다.At this time, the contaminated absorbent liquid is introduced into the inlet pipe 11 through the vacuum valve 7 to filter iron and copper oxides from the polymer filter 20. Only the absorbent liquid purified from the polymer filter 20 flows through the upper opening 18 from the inside of the hollow fiber and is sent to the upper side of the filtration vessel 9 to the absorber through the discharge pipe 16 having the vacuum valve 12. As it is sent, it is used as a purified solution.

이때 중공사형 필터(20)를 사용함에 따라 중공사외부에는 철,동산화물 등의찌꺼기가 축적되어 있는 상태이므로 이를 제거하기 위하여 주기적으로 유입배관(11)과 토출배관(16)을 막고 역세배관(15)을 통하여 질소가스 또는 수도수를 공급하므로서 여과용기(9) 상부를 거처 격벽(19) 상부로부터 중공사형 고분자 필터(20)의 개구부(18)를 통해 유입되어 필터(20) 외부에 축적된 철,동산화물 등의 찌꺼기가 분리되며 이를 배출배관(17)을 통하여 배출시킴으로서 기계외부로 완전히 분리한다. 이 과정에서도 운전중 절대로 공기가 유입되어서는 아니된다.At this time, as the hollow fiber filter 20 is used, wastes such as iron and copper oxide are accumulated in the outside of the hollow fiber, so that the inlet pipe 11 and the discharge pipe 16 are periodically blocked in order to remove them. 15) is supplied through the opening 18 of the hollow fiber-type polymer filter 20 through the upper portion of the partition 19 through the upper portion of the filtration vessel (9) by supplying nitrogen gas or tap water through the filter 20 is accumulated outside the filter 20 Debris, such as iron and copper oxide, is separated and discharged through the discharge pipe 17 to be completely separated outside the machine. In this process, no air should be introduced during operation.

따라서 흡수액이 순환되는 배관(11,15,16,17)과 진공밸브(7,8,10,12)의 연결은 완전히 용접으로 밀폐해야 하고 여과기 여과용기(9)의 플랜지(21)부분에는 완전밀폐가 될 수 있도록 하고 고온에서도 견딜 수 있는 가스켓(22)을 사용함이 바람직하다.Therefore, the connection between the pipes (11, 15, 16, 17) and the vacuum valves (7, 8, 10, 12) through which the absorbent liquid is circulated must be completely sealed by welding, and the flange (21) of the filter filtration vessel (9) is completely closed. It is preferable to use a gasket 22 that can be sealed and can withstand high temperatures.

상술한 바와 같이 본 고안은 종래에 냉동기 및 냉온수기의 가동을 중지하면서 흡수액을 분리하여 별도의 정제과정을 거치면서 문제되는 진공파괴와 정제에 따른 많은 시간과 비용을 여과정제장치를 직접 일체형으로 부착하므로써 흡수용액 오염을 방지할 수 있고 장시간동안 운전할 수 있으며, 에너지를 13% 이상 절약할 수 있음이 확인되었고 기계의 수명이 연장된다.As described above, the present invention is conventionally made by directly attaching the filtration and purification device to the vacuum purification and refining process. It has been found that it can prevent the contamination of absorbent solution, can operate for a long time, save more than 13% of energy, and extend the life of the machine.

Claims (1)

흡수식 냉,온수기에 흡수용액의 여과정제장치를 부설함에 있어 흡수기(1)내의 흡수액이 용액펌프(2)와 진공밸브(7)를 통해 유입되는 배관(11)을 가지고 있는 여과용기(9)에는 내부측 상부에 격판(19)을 두고 평균공경 0.1마이크로미터의 미세 다공막으로 형성된 중공사형 외압식 여과기가 격판(19)상부로 개구부(18)를 가지고 여러개가 밀폐배열 형성됨과 아울러 여과용기(9) 상부로는 진공밸브(8)를 가지는 질소가스 또는 수도수를 유입하는 역세배관(15)과 흡수기로 보내는 진공밸브(12)를 가지는 토출배관(16)으로 구성되고 여과용기(9) 하부로는 진공밸브(10)를 가지는 철 및 구리의 산화물 등의 찌꺼기를 역세하기 위한 배출배관(17)으로 구성되어 있는 것을 특징으로 하는 흡수용액 정제여과기 일체형 냉,온수기.In the installation of the filtration and purification device for the absorbing solution in the absorption type cold and hot water, the filtration vessel (9) having the pipe (11) through which the absorbent liquid in the absorber (1) flows through the solution pump (2) and the vacuum valve (7). Hollow fiber type external pressure filter having a diaphragm 19 having an average pore diameter of 0.1 micrometer and having an opening 18 above the diaphragm 19 has a plurality of hermetic arrays and a plurality of filter vessels. The upper part is composed of a backwash pipe 15 for introducing nitrogen gas or tap water having a vacuum valve 8 and a discharge pipe 16 having a vacuum valve 12 which is sent to the absorber. The cold and hot water absorber integrated filter, characterized in that the exhaust pipe 17 for backwashing the residue of iron and copper oxide having a vacuum valve (10).
KR20-2003-0012007U 2003-04-18 2003-04-18 A absorption solution refining filter unified cool-hot water supply implement KR200323227Y1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100841655B1 (en) * 2007-09-18 2008-06-26 주식회사신우이엔지 Chiller heater with refining apparatus of absorption liquids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100841655B1 (en) * 2007-09-18 2008-06-26 주식회사신우이엔지 Chiller heater with refining apparatus of absorption liquids

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