JPH086209Y2 - Solution pump for absorption refrigerator - Google Patents
Solution pump for absorption refrigeratorInfo
- Publication number
- JPH086209Y2 JPH086209Y2 JP5765690U JP5765690U JPH086209Y2 JP H086209 Y2 JPH086209 Y2 JP H086209Y2 JP 5765690 U JP5765690 U JP 5765690U JP 5765690 U JP5765690 U JP 5765690U JP H086209 Y2 JPH086209 Y2 JP H086209Y2
- Authority
- JP
- Japan
- Prior art keywords
- solution
- pump
- solution pump
- electric motor
- dilute
- 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.)
- Expired - Lifetime
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 14
- 239000000243 solution Substances 0.000 claims description 148
- 239000006096 absorbing agent Substances 0.000 claims description 19
- 239000003507 refrigerant Substances 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 12
- 238000005192 partition Methods 0.000 claims description 11
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 10
- 230000001050 lubricating effect Effects 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000010586 diagram Methods 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 230000009897 systematic effect Effects 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】 〔産業上の利用分野〕 本考案は吸収冷凍機用溶液ポンプに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a solution pump for an absorption refrigerator.
吸収器,蒸発器,凝縮器,再生器,溶液熱交換器と、
吸収器から溶液熱交換器を介し再生器へ溶液を送る溶液
ポンプ,吸収器から蒸発器へ冷媒を送る冷媒ポンプから
構成され、臭化リチウム水溶液など結晶質の溶液と水を
冷媒として用いる吸収冷凍機において、通常用いる溶液
ポンプは密閉電動機駆動式で、そのポンプで昇圧された
溶液の一部を電動機の冷却及び軸受の潤滑に用いる自己
冷却,自己潤滑方式を採用している。Absorber, evaporator, condenser, regenerator, solution heat exchanger,
Absorption refrigeration consisting of a solution pump that sends a solution from an absorber to a regenerator via a solution heat exchanger, and a refrigerant pump that sends a refrigerant from the absorber to an evaporator, using a crystalline solution such as an aqueous solution of lithium bromide and water as the refrigerant. In a machine, a solution pump that is usually used is a sealed electric motor drive type, and a self-cooling and self-lubricating method is used in which a part of the solution pressurized by the pump is used for cooling the electric motor and lubricating the bearing.
しかして、濃溶液が再生器から吸収器へ導かれる濃溶
液系統に溶液ポンプを設置する場合、従来のポンプで
は、昇圧された溶液の一部を電動機の冷却や軸受の潤滑
に用いることになるが、隙間が小さい個所では流れによ
どみができたり、周囲への放熱により溶液の温度が低下
し易く、この場合濃溶液では溶液中に結晶を生じること
があり、その結果電動機の回転に支障を来し、溶液ポン
プの運転ができなくなる問題がある。Therefore, when a solution pump is installed in a concentrated solution system in which the concentrated solution is guided from the regenerator to the absorber, in the conventional pump, a part of the pressurized solution is used for cooling the electric motor and lubricating the bearing. However, in a place with a small gap, the flow may cause stagnation, and heat dissipation to the surroundings may easily lower the temperature of the solution.In this case, concentrated solution may cause crystals to form in the solution, and as a result, rotation of the motor is hindered. Then, there is a problem that the solution pump cannot be operated.
本考案は、このような事情に鑑みて提案されたもの
で、溶液が電動機内部、軸受などの隙間部で結晶するこ
となく電動機の冷却や軸受の潤滑を行いながら、濃溶液
を十分昇圧することができる吸収冷凍機用溶液ポンプを
提供することを目的とする。The present invention has been proposed in view of such circumstances, and it is possible to sufficiently pressurize the concentrated solution while cooling the motor and lubricating the bearing without the solution crystallizing in the gaps inside the motor and the bearing. It is an object of the present invention to provide a solution pump for an absorption refrigerating machine.
そのために本考案は、吸収器,蒸発器,凝縮器,再生
器,溶液熱交換器,溶液ポンプ,冷媒ポンプから構成さ
れ臭化リチウム水溶液など結晶質の溶液と水を冷媒とし
て用いる吸収冷凍機において、濃溶液が上記再生器から
上記吸収器へ導かれる濃溶液配管系に上記濃溶液を流し
易くするための溶液ポンプを備え、かつ上記溶液ポンプ
が上記吸収器から上記再生器へ稀溶液を送る溶液ポンプ
と同一電動機に連結されるとともに、同電動機と稀溶液
側のポンプとの仕切板及び同ポンプの羽根車にそれぞれ
孔を穿設するとともに、電動機軸又は濃溶液側のポンプ
の羽根車に孔を穿設し、電動機の冷却及び軸受部の潤滑
用に稀溶液側のポンプで昇圧された稀溶液だけが供せら
れることを特徴とする。To this end, the present invention is directed to an absorption refrigerator that uses a crystalline solution such as an aqueous solution of lithium bromide and water as a refrigerant, which is composed of an absorber, an evaporator, a condenser, a regenerator, a solution heat exchanger, a solution pump, and a refrigerant pump. , A concentrated solution is provided from the regenerator to the absorber, and a solution pump is provided in the concentrated solution piping system for facilitating the flow of the concentrated solution, and the solution pump sends the dilute solution from the absorber to the regenerator. The pump is connected to the same electric motor as the solution pump, and holes are made in the partition plate between the electric motor and the pump on the dilute solution side and on the impeller of the pump, and on the impeller of the electric motor shaft or the concentrated solution side pump. It is characterized in that a hole is bored and only the diluted solution whose pressure is increased by the pump on the diluted solution side is provided for cooling the electric motor and lubricating the bearing portion.
本考案吸収冷凍機用溶液ポンプにおいては、再生器か
ら吸収器へ濃溶液を送る濃溶液ポンプと吸収器から再生
器へ稀溶液を送る稀溶液ポンプとが同一電動機で駆動さ
れるとともに、電動機の冷却,軸受の潤滑が稀溶液ポン
プで昇圧された稀溶液の一部のみを利用して行われ、従
って溶液が電動機内部,軸受部の隙間で結晶することな
く電動機の冷却,潤滑を行いながら、濃溶液ポンプを稼
動することができる。In the solution pump for absorption chiller of the present invention, the concentrated solution pump that sends the concentrated solution from the regenerator to the absorber and the diluted solution pump that sends the diluted solution from the absorber to the regenerator are driven by the same electric motor, and Cooling and lubrication of the bearing are performed by using only a part of the diluted solution that is boosted by the diluted solution pump. Therefore, while the solution cools and lubricates the motor without crystallizing in the gap between the inside of the motor and the bearing, The concentrated solution pump can be operated.
本考案吸収冷凍機用溶液ポンプの実施例を図面につい
て説明すると、第1図は第1実施例の縦断面図、第2図
は第2実施例の縦断面図、第3図は本考案の溶液ポンプ
を設置した直焚吸収冷凍機の系統図である。An embodiment of the solution pump for an absorption refrigerator according to the present invention will be described with reference to the drawings. FIG. 1 is a vertical sectional view of the first embodiment, FIG. 2 is a vertical sectional view of the second embodiment, and FIG. It is a systematic diagram of the direct-heating absorption refrigerator which installed the solution pump.
まず、第1図,第2図に示す溶液ポンプを設置した直
焚吸収冷凍機を、第3図について説明すると、吸収器1,
蒸発器2,凝縮器3,低圧再生器4,高圧再生器5,低温側溶液
熱交換器6及び高温側溶液熱交換器7が、それぞれ所定
の位置関係で配置されるとともに、臭化リチウム水溶液
など溶液からなる吸収剤の配管系と、水からなる冷媒の
配管系とにより、それぞれ所定の相互関係で接続されて
おり、かつ吸収器1から溶液熱交換器6,7を介し高圧再
生器5へ通ずる配管系に稀溶液ポンプ8が設置されると
ともに、低圧再生器4から溶液熱交換器6を介し吸収器
1へ通ずる濃溶液配管系に濃溶液ポンプ9が設置された
うえ、両ポンプ8,9は同一の溶液ポンプ用電動機10に共
通に連結されており、その詳細は第1図,第2図につき
後述する通りである。なお吸収器1から蒸発器2へ通ず
る冷媒配管系には冷媒ポンプ11が設置されている。First, a direct-fired absorption refrigerator equipped with the solution pump shown in FIGS. 1 and 2 will be described with reference to FIG.
The evaporator 2, the condenser 3, the low pressure regenerator 4, the high pressure regenerator 5, the low temperature side solution heat exchanger 6 and the high temperature side solution heat exchanger 7 are respectively arranged in a predetermined positional relationship, and a lithium bromide aqueous solution is provided. A high-pressure regenerator 5 which is connected in a predetermined mutual relationship by a piping system of an absorbent composed of a solution and a piping system of a refrigerant composed of water, and which is connected from the absorber 1 via the solution heat exchangers 6 and 7. A dilute solution pump 8 is installed in the piping system leading to the above, and a concentrated solution pump 9 is installed in the concentrated solution piping system leading from the low pressure regenerator 4 to the absorber 1 through the solution heat exchanger 6 and both pumps 8 , 9 are commonly connected to the same solution pump electric motor 10, and details thereof will be described later with reference to FIGS. 1 and 2. A refrigerant pump 11 is installed in the refrigerant piping system that leads from the absorber 1 to the evaporator 2.
次に、このような同一の溶液ポンプ用電動機10に共通
に連結されている稀溶液ポンプ8及び濃溶液ポンプ9の
詳細を、第1図,第2図について説明する。Next, details of the dilute solution pump 8 and the concentrated solution pump 9 commonly connected to the same solution pump electric motor 10 will be described with reference to FIGS. 1 and 2.
第1実施例の第1図において、この例は溶液ポンプ用
電動機10の片側軸端に稀溶液ポンプ8及び濃溶液ポンプ
9を連結したもので、電動機10のステーター12の内部に
収容されたローター13の軸14が両端の軸受15,16に支承
されたうえ、左側へ延長してその延長部分に、稀溶液ポ
ンプ羽根車17及び濃溶液ポンプ羽根車18が取付けられる
とともに、電動機10と稀溶液ポンプ8との間には仕切板
19,両溶液ポンプ8,9の間には仕切板20及びシールリング
20aがそれぞれ介装されている。また軸14の軸心に右側
端からシールリング20aの内縁へ開口する孔21が穿設さ
れるとともに、仕切板19に孔22,稀溶液ポンプ羽根車17
に孔23がそれぞれ穿設されている。In FIG. 1 of the first embodiment, in this example, a dilute solution pump 8 and a concentrated solution pump 9 are connected to one end of a solution pump electric motor 10, and a rotor housed inside a stator 12 of the electric motor 10. A shaft 14 of 13 is supported by bearings 15 and 16 at both ends, and is extended to the left side, and a dilute solution pump impeller 17 and a concentrated solution pump impeller 18 are attached to the extended portion, and an electric motor 10 and a dilute solution are also provided. Partition plate between pump 8
19, Partition plate 20 and seal ring between both solution pumps 8 and 9
20a are installed respectively. Further, a hole 21 that opens from the right end to the inner edge of the seal ring 20a is formed in the shaft center of the shaft 14, and the partition plate 19 has a hole 22 and a dilute solution pump impeller 17
Holes 23 are formed in each.
このような装置において、稀溶液ポンプ8によって昇
圧された稀溶液の一部は、仕切板19の孔22を通って電動
機10側に流入する。ここで2方向に分れ、その1つは左
側の軸受15に流入し同軸受15を潤滑しながら稀溶液ポン
プ8側に出て、その後稀溶液ポンプ羽根車17の孔23から
稀溶液ポンプ8の吸込部に戻る。In such a device, a part of the diluted solution whose pressure is increased by the diluted solution pump 8 flows into the electric motor 10 side through the hole 22 of the partition plate 19. Here, it is divided into two directions, one of which flows into the bearing 15 on the left side and goes out to the side of the dilute solution pump 8 while lubricating the bearing 15, and then from the hole 23 of the dilute solution pump impeller 17 to the dilute solution pump 8. Return to the suction section of.
もう1つは電動機10のローター13とステーター12の間
の隙間を冷却しながら右側に流れ、更に右側の軸受16に
流入して同軸受16を潤滑した後、軸14の孔21に右端から
入りシールリング20aと軸14の隙間に導かれる。The other one flows to the right side while cooling the gap between the rotor 13 and the stator 12 of the electric motor 10, and then flows into the bearing 16 on the right side to lubricate the bearing 16 and then enters the hole 21 of the shaft 14 from the right end. It is guided to the gap between the seal ring 20a and the shaft 14.
この稀溶液の上記系路を流れる圧力は、流路の抵抗に
より稀溶液ポンプ8の吐出部圧力より僅か低下している
が、シールリング20aの右端は稀溶液ポンプ8の吸込
部、また左端は濃溶液ポンプ9の吸込部であり、通常こ
れらの吸込部圧力は低いので、軸14内の孔21を流れてき
た稀溶液は差圧によりこのシールリング20aの隙間に流
入し、濃溶液がこの隙間に流入するのを防止する。ここ
に導かれた稀溶液の一部は右側に流れ稀溶液ポンプ8の
吸込部に戻り、左側に流れた稀溶液は濃溶液ポンプ9の
吸込部に流入する。The pressure of the dilute solution flowing through the system passage is slightly lower than the discharge portion pressure of the dilute solution pump 8 due to the resistance of the passage, but the right end of the seal ring 20a is the suction portion of the dilute solution pump 8 and the left end is It is the suction part of the concentrated solution pump 9, and normally the pressure of these suction parts is low, so the dilute solution flowing through the hole 21 in the shaft 14 flows into the gap of this seal ring 20a due to the differential pressure, and the concentrated solution is Prevent it from flowing into the gap. A part of the diluted solution introduced here flows to the right side and returns to the suction section of the diluted solution pump 8, and the diluted solution flowed to the left side flows into the suction section of the concentrated solution pump 9.
次に第2実施例の第2図において、この例は溶液ポン
プ用電動機10の両側軸端に稀溶液ポンプ8及び濃溶液ポ
ンプ9をそれぞれ連結したもので、電動機10の軸14の右
側延長部に稀溶液ポンプ羽根車17が取付けられるととも
に、左側延長部に濃溶液ポンプ羽根車18が取付けられて
おり、更に電動機10と稀溶液ポンプ8との間の仕切板19
に孔22、稀溶液ポンプ羽根車17に孔23がそれぞれ穿設さ
れるとともに、濃溶液ポンプ羽根車18に孔24が穿設され
ている。Next, referring to FIG. 2 of the second embodiment, in this example, a dilute solution pump 8 and a concentrated solution pump 9 are connected to both shaft ends of a solution pump electric motor 10, respectively, and a right extension portion of a shaft 14 of the electric motor 10 is connected. A dilute solution pump impeller 17 is attached to the above, a concentrated solution pump impeller 18 is attached to the left extension, and a partition plate 19 between the electric motor 10 and the dilute solution pump 8 is attached.
A hole 22 is formed in the dilute solution pump impeller 17, a hole 23 is formed in the dilute solution pump impeller 17, and a hole 24 is formed in the concentrated solution pump impeller 18.
このような装置において、稀溶液ポンプ8によって昇
圧された稀溶液の一部は、仕切板19の孔22を通って電動
機10側へ流入する。ここで2方向に分れ、その1つは右
側の軸受16に流入し軸受16を潤滑しながら稀溶液ポンプ
8側に出て、その後稀溶液ポンプ羽根車17の孔23から稀
溶液ポンプ8の吸込部に戻る。In such a device, a part of the diluted solution whose pressure is increased by the diluted solution pump 8 flows into the electric motor 10 side through the hole 22 of the partition plate 19. Here, it is divided into two directions, one of which flows into the bearing 16 on the right side, and while lubricating the bearing 16, exits to the dilute solution pump 8 side, and then from the hole 23 of the dilute solution pump impeller 17 to the dilute solution pump 8 Return to the suction section.
もう1つは電動機10のローター13とステーター12の間
の隙間を冷却しながら左側に流れ、更に左側の軸受15に
流入し同軸受15を潤滑しながら濃溶液ポンプ9側に出
て、その後濃溶液ポンプ羽根車18の孔24から濃溶液ポン
プ9の吸込部に流入する。このときも、第1実施例で説
明したように、濃溶液ポンプ9の吸込部圧力は稀溶液ポ
ンプ8の吐出圧力より十分低いので、差圧により稀溶液
を上述のように流すことができる。The other one flows to the left side while cooling the gap between the rotor 13 and the stator 12 of the electric motor 10, further flows into the bearing 15 on the left side, and while lubricating the bearing 15, flows out to the concentrated solution pump 9 side, and then to the concentrated solution pump 9. From the hole 24 of the solution pump impeller 18 flows into the suction part of the concentrated solution pump 9. Also at this time, as described in the first embodiment, the suction portion pressure of the concentrated solution pump 9 is sufficiently lower than the discharge pressure of the diluted solution pump 8, so that the diluted solution can be flown as described above by the differential pressure.
かくして、本考案装置によれば、濃溶液ポンプ9を稀
溶液ポンプ8と同一の溶液ポンプ用電動機10で駆動され
るような構造とし、電動機10の冷却,軸受15,16の潤滑
には、稀溶液ポンプ8で昇圧された稀溶液の一部だけを
利用して行うようにしたことで、溶液が電動機10,軸受1
5,16又はシールリング20aなどの隙間部で結晶するのを
防止しながら、濃溶液を昇圧することが可能である。Thus, according to the device of the present invention, the concentrated solution pump 9 is structured to be driven by the same solution pump electric motor 10 as the rare solution pump 8, and is rarely used for cooling the electric motor 10 and lubricating the bearings 15, 16. By using only a part of the dilute solution whose pressure is increased by the solution pump 8, the solution can be used as the electric motor 10 and the bearing 1.
It is possible to pressurize the concentrated solution while preventing crystallization in the gaps such as 5, 16 or the seal ring 20a.
要するに本考案によれば、吸収器,蒸発器,凝縮器,
再生器,溶液熱交換器,溶液ポンプ,冷媒ポンプから構
成され臭化リチウム水溶液など結晶質の溶液と水を冷媒
として用いる吸収冷凍機において、濃溶液が上記再生器
から上記吸収器へ導かれる濃溶液配管系に上記濃溶液を
流し易くするための溶液ポンプを備え、かつ上記溶液ポ
ンプが上記吸収器から上記再生器へ稀溶液を送る溶液ポ
ンプと同一電動機に連結されるとともに、同電動機と稀
溶液側のポンプとの仕切板及び同ポンプの羽根車にそれ
ぞれ孔を穿設するとともに、電動機軸又は濃溶液側のポ
ンプの羽根車に孔を穿設し、電動機の冷却及び軸受部の
潤滑用に稀溶液側のポンプで昇圧された稀溶液だけが供
せられることにより、溶液が電動機内部,軸受などの隙
間部で結晶することなく電動機の冷却や軸受の潤滑を行
いながら、濃溶液を十分昇圧することができる吸収冷凍
機用溶液ポンプを得るから、本考案は産業上極めて有益
なものである。In short, according to the present invention, an absorber, an evaporator, a condenser,
In an absorption refrigerator comprising a regenerator, a solution heat exchanger, a solution pump, and a refrigerant pump and using a crystalline solution such as an aqueous solution of lithium bromide and water as a refrigerant, a concentrated solution is introduced from the regenerator to the absorber. The solution piping system is equipped with a solution pump for facilitating the flow of the concentrated solution, and the solution pump is connected to the same electric motor as the solution pump for sending the dilute solution from the absorber to the regenerator, and is rarely connected to the electric motor. For the cooling of the electric motor and the lubrication of the bearing, make holes in the partition plate with the pump on the solution side and in the impeller of the pump, and also in the impeller of the motor shaft or the concentrated solution side pump. By supplying only the diluted solution whose pressure is increased by the pump on the diluted solution side, the concentrated solution can be cooled while cooling the motor and lubricating the bearing without crystallizing the solution in the gaps inside the motor and bearings. Since obtaining the absorption chiller solution pump can be sufficiently boosted, the present invention is intended on extremely valuable industrial.
第1図は本考案吸収冷凍機用溶液ポンプの第1実施例の
縦断面図、第2図は第2実施例の縦断面図、第3図は本
考案の溶液ポンプを設置した直焚吸収冷凍機の系統図で
ある。 1…吸収器、2…蒸発器、3…凝縮器、4…低圧再生
器、5…高圧再生器、6…低温側溶液熱交換器、7…高
温側溶液熱交換器、8…稀溶液ポンプ、9…濃溶液ポン
プ、10…溶液ポンプ用電動機、11…冷媒ポンプ、12…ス
テーター、13…ローター、14…軸、15…軸受、16…軸
受、17…稀溶液ポンプ羽根車、18…濃溶液ポンプ羽根
車、19…仕切板、20…仕切板、20a…シールリング、21
…孔、22…孔、23…孔、24…孔。FIG. 1 is a vertical sectional view of a first embodiment of a solution pump for an absorption refrigerator of the present invention. FIG. 2 is a vertical sectional view of a second embodiment of the present invention. It is a systematic diagram of a refrigerator. 1 ... Absorber, 2 ... Evaporator, 3 ... Condenser, 4 ... Low pressure regenerator, 5 ... High pressure regenerator, 6 ... Low temperature side solution heat exchanger, 7 ... High temperature side solution heat exchanger, 8 ... Dilute solution pump , 9 ... concentrated solution pump, 10 ... solution pump electric motor, 11 ... refrigerant pump, 12 ... stator, 13 ... rotor, 14 ... shaft, 15 ... bearing, 16 ... bearing, 17 ... rare solution pump impeller, 18 ... concentrated Solution pump impeller, 19 ... Partition plate, 20 ... Partition plate, 20a ... Seal ring, 21
... hole, 22 ... hole, 23 ... hole, 24 ... hole.
フロントページの続き (56)参考文献 特開 昭56−110858(JP,A) 特開 昭56−25662(JP,A)Continuation of front page (56) References JP-A-56-110858 (JP, A) JP-A-56-25662 (JP, A)
Claims (1)
交換器,溶液ポンプ,冷媒ポンプから構成され臭化リチ
ウム水溶液など結晶質の溶液と水を冷媒として用いる吸
収冷凍機において、濃溶液が上記再生器から上記吸収器
へ導かれる濃溶液配管系に上記濃溶液を流し易くするた
めの溶液ポンプを備え、かつ上記溶液ポンプが上記吸収
器から上記再生器へ稀溶液を送る溶液ポンプと同一電動
機に連結されるとともに、同電動機と稀溶液側のポンプ
との仕切板及び同ポンプの羽根車にそれぞれ孔を穿設す
るとともに、電動機軸又は濃溶液側のポンプの羽根車に
孔を穿設し、電動機の冷却及び軸受部の潤滑用に稀溶液
側のポンプで昇圧された稀溶液だけが供せられることを
特徴とする吸収冷凍機用溶液ポンプ。1. An absorption refrigerator comprising a crystalline solution such as an aqueous solution of lithium bromide and water as a refrigerant, which comprises an absorber, an evaporator, a condenser, a regenerator, a solution heat exchanger, a solution pump and a refrigerant pump. A solution in which a concentrated solution is introduced from the regenerator to the absorber is equipped with a solution pump for facilitating the flow of the concentrated solution into the concentrated solution piping system, and the solution pump sends a dilute solution from the absorber to the regenerator. It is connected to the same electric motor as the pump, and holes are made in the partition plate between the electric motor and the pump on the dilute solution side and on the impeller of the pump, and on the motor shaft or on the impeller of the pump on the concentrated solution side. A solution pump for an absorption refrigerating machine, characterized in that only a dilute solution whose pressure is increased by a dilute solution side pump is provided for cooling an electric motor and lubricating a bearing portion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5765690U JPH086209Y2 (en) | 1990-05-31 | 1990-05-31 | Solution pump for absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5765690U JPH086209Y2 (en) | 1990-05-31 | 1990-05-31 | Solution pump for absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0418266U JPH0418266U (en) | 1992-02-14 |
| JPH086209Y2 true JPH086209Y2 (en) | 1996-02-21 |
Family
ID=31582564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5765690U Expired - Lifetime JPH086209Y2 (en) | 1990-05-31 | 1990-05-31 | Solution pump for absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH086209Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2022098644A (en) * | 2020-12-22 | 2022-07-04 | 株式会社デンソー | Cooling system |
-
1990
- 1990-05-31 JP JP5765690U patent/JPH086209Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0418266U (en) | 1992-02-14 |
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| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| EXPY | Cancellation because of completion of term |