JPH0566479U - Absorption refrigerator - Google Patents
Absorption refrigeratorInfo
- Publication number
- JPH0566479U JPH0566479U JP1248592U JP1248592U JPH0566479U JP H0566479 U JPH0566479 U JP H0566479U JP 1248592 U JP1248592 U JP 1248592U JP 1248592 U JP1248592 U JP 1248592U JP H0566479 U JPH0566479 U JP H0566479U
- Authority
- JP
- Japan
- Prior art keywords
- storage tank
- refrigerant
- refrigerant storage
- gas storage
- condensable gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
(57)【要約】
【目的】 冷媒貯蔵タンクを用いた吸収冷凍機におい
て、保冷材を使用することなく、運転停止時に冷媒貯蔵
タンクが結露して周囲を水浸しにするのを防止する。
【構成】 冷媒貯蔵タンクを不凝縮ガス貯蔵タンク内に
設けた。
【効果】 不凝縮ガス貯蔵タンク内部の真空断熱効果に
より、保冷材が不要となるので、機器の小型化を図るこ
とができる。
(57) [Abstract] [Purpose] In an absorption chiller using a refrigerant storage tank, without using a heat insulating material, it is possible to prevent the refrigerant storage tank from being condensed and submerged when the operation is stopped. [Structure] A refrigerant storage tank is provided in the non-condensable gas storage tank. [Effect] Since a heat insulating material is unnecessary due to the vacuum heat insulating effect inside the non-condensable gas storage tank, the device can be downsized.
Description
【0001】[0001]
本考案は吸収冷凍機の冷媒貯蔵タンクに関するものである。 The present invention relates to a refrigerant storage tank of an absorption refrigerator.
【0002】[0002]
蒸発器の冷媒溜と冷媒ポンプを省略した小型吸収冷凍機においては、それに代 わるものとして、図2に示すように、凝縮器7から蒸発室8に至る冷媒経路に冷 媒貯蔵タンク13とバルブ14とを備え、溶液の濃度が高くなり過ぎた時、ある いは運転終了時に、冷媒貯蔵タンク13に溜っている冷媒液(水)を放出するこ とによって濃度を調整し、結晶の発生を防止している。 As an alternative to the small-sized absorption refrigerator without the refrigerant reservoir and the refrigerant pump of the evaporator, as shown in FIG. 2, the refrigerant storage tank 13 and the valve are provided in the refrigerant path from the condenser 7 to the evaporation chamber 8. 14 is provided, the concentration of the solution is adjusted by releasing the refrigerant liquid (water) accumulated in the refrigerant storage tank 13 when the concentration of the solution becomes too high, or at the end of the operation, to prevent the generation of crystals. To prevent.
【0003】 同図において、1は室内冷房ユニット等に冷水を循環させる負荷配管、2は屋 外クーリングタワー等から冷却水を導入する冷却水配管であり、バーナ3の加熱 により高温再生器4で発生する冷媒蒸気(水蒸気)と吸収剤(リチウム塩類)の 中濃度溶液とが気液分離器5で分離し、冷媒蒸気は低温再生器6の加熱管を通っ て溶液を加熱したのち、溶液から放出された冷媒蒸気と共に凝縮器7で冷却され て冷媒液(水)に戻り、更に蒸発器8の管束上に散布されて、負荷回路1の冷水 を自身が蒸発することによって冷却し、吸収器9で凝縮すると共に溶液に吸収さ れる。一方、中濃度溶液は気液分離器5から高温熱交換器10を通って低温再生 器6へ送られ、上記冷媒蒸気による加熱で高濃度に濃縮されたのち、更に低温熱 交換器11を通って吸収器9へ送られ、蒸発器8からの冷媒蒸気を吸収して稀溶 液となる。この稀溶液は、溶液ポンプ12によって、低温熱交換器11及び高温 熱交換器10で加熱されながら、高温再生器4へ圧送される。In the figure, 1 is a load pipe for circulating cold water to an indoor cooling unit or the like, and 2 is a cooling water pipe for introducing cooling water from an outdoor cooling tower or the like, which is generated in a high temperature regenerator 4 by heating a burner 3. The refrigerant vapor (water vapor) and the medium concentration solution of the absorbent (lithium salts) are separated in the gas-liquid separator 5, and the refrigerant vapor is heated through the heating pipe of the low temperature regenerator 6 and then released from the solution. It is cooled in the condenser 7 together with the generated refrigerant vapor and returned to the refrigerant liquid (water), and is further sprayed on the tube bundle of the evaporator 8 to cool the cold water in the load circuit 1 by itself evaporating and cooling the cold water in the absorber 9 Condenses at the same time and is absorbed by the solution. On the other hand, the medium-concentration solution is sent from the gas-liquid separator 5 to the low-temperature regenerator 6 through the high-temperature heat exchanger 10, concentrated to a high concentration by the above-mentioned refrigerant vapor, and then further passed through the low-temperature heat exchanger 11. Is sent to the absorber 9 and absorbs the refrigerant vapor from the evaporator 8 to become a dilute solution. The diluted solution is pressure-fed to the high temperature regenerator 4 while being heated by the low temperature heat exchanger 11 and the high temperature heat exchanger 10 by the solution pump 12.
【0004】[0004]
上記の構成において、運転時に低温のため保冷を必要とするのは5℃程度まで 温度の下がる蒸発器8であるが、冷凍機の運転を停止した時には、高温再生器4 における冷媒蒸気の発生が停止して凝縮器7内の圧力が低下し、また冷却水が停 止するので、凝縮器7から冷媒貯蔵タンク13への冷媒液の供給も停止する。更 に凝縮器7と蒸発器8の圧力差がなくなるために、蒸発器8への冷媒液の供給も 停止し、そのため冷媒貯蔵タンク13は、冷媒液を貯蔵したまま圧力が低下する ことになって、冷媒貯蔵タンク13内で冷媒液の蒸発が起こり、その気化熱が奪 われるために、冷媒貯蔵タンク13の温度が低下する。 In the above-mentioned configuration, it is the evaporator 8 that needs to be kept cool due to the low temperature during operation, but the temperature of the evaporator 8 drops to about 5 ° C. However, when the operation of the refrigerator is stopped, the generation of refrigerant vapor in the high temperature regenerator 4 occurs. The supply of the refrigerant liquid from the condenser 7 to the refrigerant storage tank 13 is also stopped because the pressure in the condenser 7 is lowered and the cooling water is stopped. Furthermore, since the pressure difference between the condenser 7 and the evaporator 8 disappears, the supply of the refrigerant liquid to the evaporator 8 is also stopped, so that the pressure in the refrigerant storage tank 13 decreases while the refrigerant liquid is stored. As a result, the refrigerant liquid evaporates in the refrigerant storage tank 13 and the heat of vaporization is removed, so that the temperature of the refrigerant storage tank 13 decreases.
【0005】 その結果、運転停止時には冷媒貯蔵タンク13の表面に結露して、機械内が水 浸しになるので、これを防止するためにタンク13の外壁を断熱材で保冷する必 要があり、小型化の要請に反するという問題があった。本考案は、かかる問題点 を解消することを目的とするものである。As a result, when the operation is stopped, dew condensation is formed on the surface of the refrigerant storage tank 13 and the inside of the machine is submerged. Therefore, in order to prevent this, it is necessary to cool the outer wall of the tank 13 with a heat insulating material. There was a problem that it was against the demand for miniaturization. The present invention aims to solve such problems.
【0006】[0006]
本考案は、図1に示すように、凝縮器7から蒸発器8までの冷媒経路に、冷媒 液を一時的に貯蔵する冷媒貯蔵タンク13を備えて、溶液の濃度調整を行うよう にした吸収冷凍機において、この冷媒貯蔵タンク13を不凝縮ガス貯蔵タンク1 5内に設けたものである。 As shown in FIG. 1, the present invention is provided with a refrigerant storage tank 13 for temporarily storing a refrigerant liquid in a refrigerant path from a condenser 7 to an evaporator 8 to adjust the concentration of a solution. In the refrigerator, the refrigerant storage tank 13 is provided in the non-condensable gas storage tank 15.
【0007】[0007]
不凝縮ガス貯蔵タンク15は、保冷は施されていないけれども、内部が真空状 態であるために、不凝縮ガス貯蔵タンク15内に設けられている冷媒貯蔵タンク 13に対しては断熱材と同等に作用する。従って不凝縮ガス貯蔵タンク15の容 積はその分だけ大きくする必要があるが、冷媒貯蔵タンク13を保冷するための 断熱材が不要となって、全体として機器の小型化とコスト低減を図ることができ る上に、タンク数が減少するのでレイアウトも容易になる。 Although the non-condensable gas storage tank 15 is not kept cold, the inside of the non-condensable gas storage tank 15 is in a vacuum state. Act on. Therefore, the volume of the non-condensable gas storage tank 15 needs to be increased by that amount, but the heat insulating material for keeping the refrigerant storage tank 13 cool is not necessary, and the overall size of the device and cost reduction can be achieved. In addition, the number of tanks is reduced and the layout is easier.
【0008】[0008]
図1は本考案の一実施例を示すもので、図2の従来例と異なるところは、冷媒 貯蔵タンク13を不凝縮ガス貯蔵タンク15内に設けた点にある。冷媒貯蔵タン ク13は、凝縮器7で凝縮して蒸発器8に供給される冷媒液を一時的に貯蔵し、 バルブ14等による貯蔵冷媒液量の調節によって、吸収溶液の冷媒含有量を制御 し、それによって運転停止時や冷却水の温度低下時における溶液の晶析を防止す るものであり、通常凝縮器7の近傍に設けられる。一方、不凝縮ガス貯蔵タンク 15は、バルブ類から侵入する空気や腐食防止剤の作用により冷凍機内で発生す る水素ガスなどの不凝縮ガスを集積しておき、一定量に達すると機外に排出する ためのもので、抽気の便宜のため機械本体の上方に設けられるものである。 FIG. 1 shows an embodiment of the present invention, and is different from the conventional example of FIG. 2 in that a refrigerant storage tank 13 is provided in a noncondensable gas storage tank 15. The refrigerant storage tank 13 temporarily stores the refrigerant liquid condensed in the condenser 7 and supplied to the evaporator 8, and controls the refrigerant content of the absorbing solution by adjusting the amount of the refrigerant liquid stored by the valve 14 or the like. However, this prevents crystallization of the solution when the operation is stopped or the temperature of the cooling water is lowered, and is usually provided in the vicinity of the condenser 7. On the other hand, the non-condensable gas storage tank 15 accumulates non-condensable gases such as hydrogen gas generated in the refrigerator due to the action of the air invading from the valves and the action of the corrosion inhibitor, and the non-condensable gas storage tank 15 is removed from the machine when it reaches a certain amount. It is for discharging and is provided above the machine body for convenience of air extraction.
【0009】 冷媒貯蔵タンク13は、その外壁面と不凝縮ガス貯蔵タンク15の内壁面との 間に間隙を設けて、配管の継手によって不凝縮ガス貯蔵タンク15の壁面に固定 されており、従って運転停止時に内部の冷媒の蒸発により冷媒貯蔵タンク13内 の温度が低下した時にも、不凝縮ガス貯蔵タンク15からの熱伝導は殆どなく、 従って不凝縮ガス貯蔵タンク15の外壁面にも結露する虞はない。The refrigerant storage tank 13 is fixed to the wall surface of the noncondensable gas storage tank 15 by a pipe joint with a gap provided between the outer wall surface thereof and the inner wall surface of the noncondensable gas storage tank 15. Even when the temperature inside the refrigerant storage tank 13 decreases due to the evaporation of the refrigerant inside when the operation is stopped, there is almost no heat conduction from the noncondensable gas storage tank 15, and therefore dew condensation also forms on the outer wall surface of the noncondensable gas storage tank 15. There is no fear.
【0010】[0010]
本考案は上述のように、冷媒貯蔵タンクを不凝縮ガス貯蔵タンク内に設けると いう極めて簡単な構成により、不凝縮ガス貯蔵タンクが冷媒貯蔵タンクの断熱の 役割を果たし、運転停止後に冷媒貯蔵タンクの外壁面の結露によって機械内部を 水浸しにする虞がなく、冷媒貯蔵タンクを保冷するための断熱材が不要となるの で、全体として機器の小型化と低コスト化が図れる上に、要素数の減少によりレ イアウトが容易になるという利点がある。 As described above, the present invention has an extremely simple structure in which the refrigerant storage tank is provided in the non-condensable gas storage tank, and the non-condensable gas storage tank plays a heat insulating function for the refrigerant storage tank. Since there is no risk of water inside the machine being contaminated by dew condensation on the outer wall surface of the machine, there is no need for a heat insulating material to keep the refrigerant storage tank cool, so the overall size and cost of the equipment can be reduced and the number of elements can be reduced. There is an advantage that layout can be facilitated by reducing
【図1】本考案の一実施例の概略系統図。FIG. 1 is a schematic system diagram of an embodiment of the present invention.
【図2】従来例の概略系統図。FIG. 2 is a schematic system diagram of a conventional example.
1 負荷配管 2 冷却水配管 3 バーナ 4 高温再生器 5 分離器 6 低温再生器 7 凝縮器 8 蒸発器 9 吸収器 13 冷媒貯蔵タンク 14 バルブ 15 不凝縮ガス貯蔵タンク 1 Load piping 2 Cooling water piping 3 Burner 4 High temperature regenerator 5 Separator 6 Low temperature regenerator 7 Condenser 8 Evaporator 9 Absorber 13 Refrigerant storage tank 14 Valve 15 Non-condensable gas storage tank
Claims (1)
媒液を一時的に貯蔵する冷媒貯蔵タンクを備えて、溶液
の濃度調整を行うようにした吸収冷凍機において、上記
冷媒貯蔵タンクを不凝縮ガス貯蔵タンク内に設けて成る
吸収冷凍機。1. An absorption refrigerator in which a refrigerant storage tank for temporarily storing a refrigerant liquid is provided in a refrigerant path from a condenser to an evaporator to adjust a concentration of a solution, and the refrigerant storage tank is provided with the refrigerant storage tank. An absorption chiller installed in a non-condensable gas storage tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1248592U JPH0566479U (en) | 1992-02-04 | 1992-02-04 | Absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1248592U JPH0566479U (en) | 1992-02-04 | 1992-02-04 | Absorption refrigerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0566479U true JPH0566479U (en) | 1993-09-03 |
Family
ID=11806705
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1248592U Pending JPH0566479U (en) | 1992-02-04 | 1992-02-04 | Absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0566479U (en) |
-
1992
- 1992-02-04 JP JP1248592U patent/JPH0566479U/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7891202B1 (en) | Absorption system | |
KR19990022970A (en) | Compression and Absorption Hybrid Heat Pump | |
JPH06307730A (en) | Absorption type freezer | |
JPH0566479U (en) | Absorption refrigerator | |
JPH0419410Y2 (en) | ||
JP3762217B2 (en) | refrigerator | |
JP3813348B2 (en) | Absorption refrigerator | |
JPH047502Y2 (en) | ||
JP3553833B2 (en) | Absorption refrigerator | |
JP3715157B2 (en) | 2-stage double-effect absorption refrigerator | |
JP2902305B2 (en) | Absorption air conditioner | |
JP3719490B2 (en) | Absorption refrigeration system | |
JP3719493B2 (en) | Absorption refrigerator | |
JP3719491B2 (en) | Absorption refrigeration system | |
KR100261545B1 (en) | Absorption type refrigerator | |
JP2639991B2 (en) | Absorption refrigerator | |
JP2000018761A (en) | Method for operating absorption heat pump | |
JP2823295B2 (en) | Absorption refrigerator | |
KR200172397Y1 (en) | High temperature generator for an absorption refrigerator | |
KR950008338B1 (en) | Evaporator instrlled air-absorption apparatus | |
JP3113195B2 (en) | Bleeding device for absorption refrigeration system | |
JP3241498B2 (en) | Absorption refrigerator | |
JP2000002472A (en) | Absorptive freezer | |
JPS6024903B2 (en) | Multiple effect absorption refrigerator | |
WO2010033373A2 (en) | Compact cryogenic cooling chamber for oxygen liquefaction system |