JPH052803B2 - - Google Patents
Info
- Publication number
- JPH052803B2 JPH052803B2 JP12619587A JP12619587A JPH052803B2 JP H052803 B2 JPH052803 B2 JP H052803B2 JP 12619587 A JP12619587 A JP 12619587A JP 12619587 A JP12619587 A JP 12619587A JP H052803 B2 JPH052803 B2 JP H052803B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant gas
- liquid
- compressor
- refrigerant
- temperature
- 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
- 239000003507 refrigerant Substances 0.000 claims description 47
- 239000007788 liquid Substances 0.000 claims description 37
- 238000001816 cooling Methods 0.000 claims description 13
- 230000002528 anti-freeze Effects 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000006096 absorbing agent Substances 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000003134 recirculating effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 47
- 239000002826 coolant Substances 0.000 description 5
- 238000009423 ventilation Methods 0.000 description 5
- 238000005057 refrigeration Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000110 cooling liquid Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はクーラーを利用した回転力転換装置に
関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a rotational force conversion device using a cooler.
(従来の技術)
周知の如く従来、ガス圧縮式冷凍装置では、冷
媒ガスを圧縮機で圧縮し高温高圧のガスとして凝
縮器に送り冷却して凝縮させ高圧の冷媒液とし、
膨張弁を通して減圧し、低温低圧の冷媒液として
蒸発器に送り蒸発に必要な潜熱を吸収させ冷凍効
果を得ていた。しかしながらこの方法では圧縮機
の電力消費量が著しく大きく、従つて、圧縮機の
電力を削減する方法として冷媒ガスの膨張圧力を
圧縮機の回転力に利用する方法が研究され、蒸発
器、圧縮機をベーン型式(ゲーテポンプ型モータ
ー)とすることにより一部目的が達成され、此れ
らの研究の成果としての発明は、例えば特開昭60
−117037号において公知である。(Prior Art) As is well known, in conventional gas compression type refrigeration systems, refrigerant gas is compressed by a compressor and sent to a condenser as a high-temperature, high-pressure gas, where it is cooled and condensed to form a high-pressure refrigerant liquid.
It was depressurized through an expansion valve and sent to the evaporator as a low-temperature, low-pressure refrigerant liquid to absorb the latent heat necessary for evaporation and obtain a refrigeration effect. However, with this method, the power consumption of the compressor is extremely large.Therefore, as a way to reduce the power consumption of the compressor, research has been conducted on a method of using the expansion pressure of the refrigerant gas as the rotational force of the compressor. Part of the purpose was achieved by making the motor a vane type (Goethe pump type motor), and the invention as a result of this research was published, for example, in Japanese Patent Application Laid-Open No.
-117037.
(発明が解決しようとする問題点)
上記の方式を採用した場合、圧縮機、凝縮器は
共にベーンポンプ型で小型となり収容箱中に収容
されており、且つ、圧縮機は高温となるために冷
却液中に、又、蒸発器は逆に低温となるために不
凍液中に没入された構成となつており、運転中は
互いに高温、低温を発生し続けながら収容箱中で
運転しているが、低温側は冷房機能を果たしなが
らの運転であるが逆の圧縮機側の高温エネルギー
は冷却液で冷却し有効に利用されずに放熱させて
しまつていた。(Problem to be solved by the invention) When the above method is adopted, both the compressor and the condenser are vane pump type and small and housed in a storage box. On the other hand, the evaporator is immersed in the antifreeze liquid to reach a low temperature, and during operation, it is operated in a storage box while continuously generating high and low temperatures. The low-temperature side operates while fulfilling its cooling function, but the high-temperature energy on the compressor side is cooled by the coolant and is not effectively used, but instead is dissipated.
(問題点を解決するための手段)
本発明は上記の収容箱中で、運転中は各々、高
温、低温を発生し、冷却液、不凍液を加熱、冷却
している両者の温度差を最大限に利用することを
計り、冷却、加熱されている冷却液、不凍液中に
冷媒ガスの循環系を導入して冷媒ガスを効率よく
冷却、加熱し、冷媒ガスの膨張力を回転力に転換
する目的で発明されたものである。(Means for Solving the Problems) The present invention generates high and low temperatures during operation in the above storage box, and maximizes the temperature difference between heating and cooling the coolant and antifreeze. The objective is to efficiently cool and heat the refrigerant gas by introducing a refrigerant gas circulation system into the coolant and antifreeze that are being cooled and heated, and to convert the expansion power of the refrigerant gas into rotational power. It was invented in
以下本発明を図面に基づいて説明すると、1,
1′はベーンポンプ型(ゲーテポンプモーター)
の圧縮機で冷却液2,2′を入れた収容箱3,
3′中に没入する。4,4′はベーンポンプ型の圧
縮機1,1′のロータ回転軸5と同軸で回動すべ
く、前記ベーンポンプ型の圧縮機1と並列位置に
設けたベーンポンプ型の蒸発器で、各付不凍液
6,6′を入れた収容箱7,7′の不凍液6,6′
中に没入せしめる。8,8′はベーンポンプ型の
圧縮機1,1′とベーンポンプ型の蒸発器4,
4′とに各々連通せしめた冷媒ガスの圧縮側の通
気管路である。9,9′は通気管路8の途中に連
通して設けた凝縮器である。10,10′は各々
ベーンポンプ型の圧縮機1,1′とベーンポンプ
型の蒸発器4,4′とに連通せしめた冷媒ガスの
膨張側の通気管路である。11は蒸発器4′を内
蔵した収容箱7′の外側位置に設けた冷媒ガス加
熱器である。12は冷媒ガス加熱器11内に入れ
た熱交換用液である。13は冷媒ガス加熱器11
と膨張側通気管14で連通したタービンである。
15はタービン13のガスの流出側(第1図にお
いて左方)に設けた吸熱器である。16は吸熱器
15のガス流出側(第1図において左方)に設け
た熱交換器である。17は熱交換器16内に入れ
た熱交換用液である。18は蒸発器4′を没入し
た前記不凍液6′中に曲折して設けた冷媒ガスの
ガス冷却管で、ガス流出側(第1図において下端
側)は前記冷媒ガス加熱器11と連通し、ガス流
入側(第1図において上端側)は前記熱交換器1
6と送気管19を介して連通する。20は圧縮機
1を没入した前記冷却液2中に曲折して設けた熱
交換用液加熱管で熱交換用液の流出側(第1図に
おいて上端側)は前記冷媒ガス加熱器11内の熱
交換用液12の下部と加熱送液管21にて連通せ
しめ、熱交換用液の流入側(第1図において下端
側)は送液管22を介して前記熱交換器16内の
熱交換用液17の高温側と連通せしめる。23は
前記冷媒ガス加熱器11内の熱交換用液12の低
温側と前記熱交換器16の熱交換用液17の低温
側とを連通した送液管である。24はロータ回転
軸5の一端に軸着したモーターである。25,2
5′は冷凍系内に封入した冷媒ガス(フロンガス)
である。 The present invention will be explained below based on the drawings.1.
1' is vane pump type (Goethe pump motor)
A storage box 3 containing coolant 2, 2' with a compressor,
Immerse yourself in 3'. 4 and 4' are vane pump type evaporators installed in parallel with the vane pump type compressor 1 in order to rotate coaxially with the rotor rotating shaft 5 of the vane pump type compressors 1 and 1'. Antifreeze 6, 6' in storage box 7, 7' containing 6, 6'
Immerse yourself inside. 8, 8' are vane pump type compressors 1, 1' and vane pump type evaporator 4,
4' are ventilation pipes on the compression side of the refrigerant gas, respectively. 9 and 9' are condensers provided in the middle of the ventilation pipe line 8 in communication with each other. Reference numerals 10 and 10' designate ventilation pipes on the expansion side of the refrigerant gas, which communicate with the vane pump type compressors 1 and 1' and the vane pump type evaporators 4 and 4', respectively. Reference numeral 11 denotes a refrigerant gas heater provided outside the storage box 7' containing the evaporator 4'. 12 is a heat exchange liquid placed in the refrigerant gas heater 11. 13 is a refrigerant gas heater 11
The turbine is connected to the turbine through an expansion side ventilation pipe 14.
15 is a heat absorber provided on the gas outflow side of the turbine 13 (left side in FIG. 1). 16 is a heat exchanger provided on the gas outflow side (left side in FIG. 1) of the heat absorber 15. 17 is a heat exchange liquid placed in the heat exchanger 16. Reference numeral 18 denotes a gas cooling pipe for refrigerant gas which is bent and provided in the antifreeze liquid 6' in which the evaporator 4' is immersed, and the gas outlet side (lower end side in FIG. 1) communicates with the refrigerant gas heater 11; The gas inflow side (upper end side in FIG. 1) is the heat exchanger 1.
6 via an air pipe 19. Reference numeral 20 denotes a heat exchange liquid heating tube which is bent into the refrigerant 2 into which the compressor 1 is immersed, and the outflow side of the heat exchange liquid (the upper end side in FIG. 1) is connected to the refrigerant gas heater 11. The lower part of the heat exchange liquid 12 is communicated with a heated liquid sending pipe 21, and the inflow side (lower end side in FIG. 1) of the heat exchange liquid is connected to the heat exchanger 16 through the liquid sending pipe 22. It communicates with the high temperature side of the service liquid 17. Reference numeral 23 denotes a liquid sending pipe that communicates the low temperature side of the heat exchange liquid 12 in the refrigerant gas heater 11 with the low temperature side of the heat exchange liquid 17 in the heat exchanger 16. Reference numeral 24 denotes a motor that is attached to one end of the rotor rotating shaft 5. 25,2
5' is the refrigerant gas (fluorocarbon gas) sealed in the refrigeration system.
It is.
(作用)
次に本発明の作用に就いて述べると、モーター
24でロータ回転軸5を始動すると、ベーンポン
プ型の圧縮機1,1′のロータ26,26′が回転
し、ベーン27,27′の偏芯作用で冷媒ガス2
5,25′を圧縮して高温高圧のガスとして凝縮
器9,9′に向かつて各々送り出し、凝縮器9で
冷却して凝縮させ高圧の冷媒液とし、ベーンポン
プ型の蒸発器4,4′中に噴入せしめると、冷媒
液はベーンポンプ型の蒸発器4,4′中で、潜熱
を吸収しながらガス化し、膨張してベーン27,
27′を押圧回転せしめ、ベーン27,27′の回
転力はロータ28,28′を介して回転軸5を回
動せしめながら膨張側の通気管路10,10′側
へ冷媒ガス25,25′は各々流出し、再度ベー
ンポンプ型の圧縮機1,1′中に還元して冷凍系
を形成している。又、前記の二連の冷媒系の内、
蒸発機4と圧縮機1′との各加熱、冷却温度は互
いに中央位置で連結相殺されるため通気管路10
より圧縮機1に戻る冷媒ガスは常温近くまで加熱
されて大となるためより圧縮機1はより高熱とな
り、又、圧縮機1′は温度が低くなり略常温とす
ることが可能となる。従つて蒸発器4′はより冷
却温度は低温となる。一方、運転により温度が高
くなつた冷却液2内に没入せしめた熱交換用液加
熱管20中で加熱された熱交換用液12は加熱送
液管21を通つて、冷媒ガス加熱器11内に到達
し、冷媒ガス加熱器11内を加熱し、熱交換後送
液管23を通つて熱交換器16に到達し、熱交換
器16内の熱交換用液17と熱交換を行なつた
後、送液管22を通過して熱交換用液加熱管20
に回帰する。他方、運転により冷えた不凍液6′
中に没入せしめたガス冷却管18中に封入した冷
媒ガス29は、ガス冷却管18中で冷やされて液
化し、ガス冷却管18より流出して冷媒ガス加熱
器11に流入するが、この場合冷媒ガス加熱器1
1内は前述の加熱された高温の熱交換用液12が
循環しているため液化している冷媒ガス29は加
熱されて膨張気化し、膨張側通気管14を通過し
てタービン13内に噴入し、タービン13を回転
させて回転力を機外に取り出した後、吸熱器15
を通過して外部より吸熱して略常温にまで熱エネ
ルギーをとりこみ、次に熱交換器16中に進入し
熱交換器16中の後半部(第1図において左半
部)では、熱交換用液12からの低温作用により
熱交換を行なつて冷やした後、送気管19を通つ
て冷媒ガスは前記ガス冷却管18に回帰循環す
る。(Function) Next, the function of the present invention will be described. When the rotor rotating shaft 5 is started by the motor 24, the rotors 26, 26' of the vane pump type compressors 1, 1' rotate, and the vanes 27, 27' Refrigerant gas 2 due to the eccentric action of
5 and 25' are compressed and sent as high-temperature, high-pressure gases to condensers 9 and 9', where they are cooled and condensed to form a high-pressure refrigerant liquid, which is then fed into vane pump type evaporators 4 and 4'. When the refrigerant liquid is injected into the vane pump type evaporators 4 and 4', it gasifies while absorbing latent heat, expands, and flows through the vanes 27 and 4'.
27' is pressed and rotated, and the rotational force of the vanes 27, 27' rotates the rotating shaft 5 via the rotors 28, 28', and the refrigerant gas 25, 25' is directed to the expansion side ventilation pipes 10, 10'. Each flows out and is reduced again into the vane pump type compressor 1, 1' to form a refrigeration system. Moreover, among the two refrigerant systems mentioned above,
The heating and cooling temperatures of the evaporator 4 and the compressor 1' are mutually connected at the center and cancel each other out.
The refrigerant gas that returns to the compressor 1 is heated to near room temperature and becomes larger, so the compressor 1 becomes hotter, and the temperature of the compressor 1' becomes lower and can be kept at about room temperature. Therefore, the cooling temperature of the evaporator 4' becomes lower. On the other hand, the heat exchange liquid 12 heated in the heat exchange liquid heating tube 20 immersed in the coolant 2 whose temperature has become high due to operation is passed through the heated liquid sending tube 21 into the refrigerant gas heater 11. The refrigerant gas reaches the temperature, heats the inside of the refrigerant gas heater 11, and after heat exchange, reaches the heat exchanger 16 through the liquid sending pipe 23, where it exchanges heat with the heat exchange liquid 17 in the heat exchanger 16. After that, the liquid passes through the liquid sending pipe 22 and is heated to the heat exchange liquid heating pipe 20.
Return to On the other hand, the antifreeze liquid 6' that has cooled down due to operation
The refrigerant gas 29 sealed in the gas cooling pipe 18 immersed therein is cooled and liquefied in the gas cooling pipe 18, flows out from the gas cooling pipe 18, and flows into the refrigerant gas heater 11, but in this case. Refrigerant gas heater 1
As the heated high-temperature heat exchange liquid 12 is circulated inside 1, the liquefied refrigerant gas 29 is heated, expands and vaporizes, passes through the expansion side vent pipe 14, and is injected into the turbine 13. After the turbine 13 is rotated and the rotational power is taken out of the machine, the heat absorber 15
It absorbs heat from the outside and captures thermal energy to approximately room temperature, then enters the heat exchanger 16, and in the latter half of the heat exchanger 16 (left half in Fig. 1), a After being cooled by heat exchange by the low temperature action from the liquid 12, the refrigerant gas is circulated back to the gas cooling pipe 18 through the air supply pipe 19.
(実施例)
本発明に利用する冷媒ガス25,25′はフロ
ンガスが適し、冷媒ガス29は液体窒素が適す
る。(Embodiment) Freon gas is suitable for the refrigerant gases 25 and 25' used in the present invention, and liquid nitrogen is suitable for the refrigerant gas 29.
(発明の効果)
本発明を実施するとベーンポンプ型の圧縮機及
び蒸発機を採用したクーラーにおいて、冷房運転
により当然発生する圧縮機の高熱を有効に利用
し、蒸発機で発生した低温を利用して冷却液化し
た冷媒ガスを瞬間的に加熱膨張せしめ、この膨張
力をタービンを介して転換し、回転力として有効
に機外に取出しが出来ると共に、冷媒ガスの循環
系に略常温になるまで熱エネルギーをも取入れて
出力効率を高めることが可能となる発明である。(Effect of the invention) When the present invention is carried out, in a cooler that employs a vane pump type compressor and evaporator, the high heat of the compressor that naturally occurs during cooling operation can be effectively used, and the low temperature generated by the evaporator can be used. The cooled and liquefied refrigerant gas is instantaneously heated and expanded, and this expansion force is converted through a turbine, allowing it to be effectively taken out of the machine as rotational force, and at the same time providing thermal energy to the refrigerant gas circulation system until it reaches approximately room temperature. This invention also makes it possible to increase output efficiency by incorporating
第1図は本発明を示す一部縦断した正面図であ
る。第2図はベーンの蒸発器を示す縦断面図。第
3図はベーンポンプ型の圧縮機を示す縦断面図で
ある。
1,1′…圧縮機、2,2′…冷却液、3,3′
…収容箱、4,4′…蒸発器、5…ローター回転
軸、6,6′…不凍液、7,7′…収容箱、8,
8′…通気管路、9,9′…凝縮器、10,10′
…通気管路、11…冷媒ガス加熱器、12…熱交
換用液、13…タービン、14…膨張側通気管、
15…吸熱器、16…熱交換器、17…熱交換用
液、18…ガス冷却管、19…送気管、20…熱
交換用液加熱管、21…加熱送液管、22…送液
管、23…送液管、24…モーター、25,2
5′…冷媒ガス、26,26′…ロータ、27,2
7′…ベーン、28,28′…ロータ、29…冷媒
ガス。
FIG. 1 is a partially longitudinally sectional front view showing the present invention. FIG. 2 is a longitudinal sectional view showing the vane evaporator. FIG. 3 is a longitudinal sectional view showing a vane pump type compressor. 1, 1'...Compressor, 2, 2'...Cooling liquid, 3, 3'
...Storage box, 4,4'...Evaporator, 5...Rotor rotating shaft, 6,6'...Antifreeze, 7,7'...Storage box, 8,
8'...Vent pipe line, 9,9'...Condenser, 10,10'
...Vent pipe line, 11... Refrigerant gas heater, 12... Heat exchange liquid, 13... Turbine, 14... Expansion side vent pipe,
DESCRIPTION OF SYMBOLS 15... Heat absorber, 16... Heat exchanger, 17... Liquid for heat exchange, 18... Gas cooling pipe, 19... Air supply pipe, 20... Liquid heating pipe for heat exchange, 21... Heating liquid supply pipe, 22... Liquid supply pipe , 23...liquid feeding pipe, 24...motor, 25,2
5'... Refrigerant gas, 26, 26'... Rotor, 27, 2
7'... Vane, 28, 28'... Rotor, 29... Refrigerant gas.
Claims (1)
ラーにおいて、蒸発機を没入せしめた収容箱の不
凍液中に冷媒ガスの通過するガス冷却管を導入
し、ガス冷却管の出口側に、冷媒ガス加熱器を設
けて圧縮機側の高温の冷却液を導入して前記冷媒
ガスを加熱膨張し、次に膨張した冷媒ガスをター
ビンに導いてタービンを回転し、次に吸熱器に導
いて略常温にまで熱を冷媒ガスに吸収し、更に熱
交換器中に冷媒ガスを導いて出口側後半部は前記
冷媒ガス加熱機の低温側と連通せしめて低温に下
げてから前記ガス冷却管の入口側に回帰循環する
冷媒ガスによる回転出力循環系を設けたことを特
徴とするクーラーを利用した回転力転換装置。1 In a cooler that uses a vane-type evaporator and compressor, a gas cooling pipe through which refrigerant gas passes is introduced into the antifreeze liquid in the storage box in which the evaporator is immersed, and a refrigerant gas heating The refrigerant gas is heated and expanded by introducing a high-temperature refrigerant from the compressor side, and then the expanded refrigerant gas is led to a turbine to rotate the turbine, and then to a heat absorber to bring it to approximately room temperature. The refrigerant gas is then introduced into the heat exchanger, and the latter half of the outlet side is connected to the low temperature side of the refrigerant gas heater to lower the temperature to the inlet side of the gas cooling pipe. A rotational power conversion device using a cooler, characterized by having a rotational output circulation system using recirculating refrigerant gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12619587A JPS63295808A (en) | 1987-05-22 | 1987-05-22 | Turning moment conversion device utilizing cooler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12619587A JPS63295808A (en) | 1987-05-22 | 1987-05-22 | Turning moment conversion device utilizing cooler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63295808A JPS63295808A (en) | 1988-12-02 |
| JPH052803B2 true JPH052803B2 (en) | 1993-01-13 |
Family
ID=14929051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12619587A Granted JPS63295808A (en) | 1987-05-22 | 1987-05-22 | Turning moment conversion device utilizing cooler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63295808A (en) |
-
1987
- 1987-05-22 JP JP12619587A patent/JPS63295808A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63295808A (en) | 1988-12-02 |
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