JPS60138377A - Absorption type refrigerator - Google Patents
Absorption type refrigeratorInfo
- Publication number
- JPS60138377A JPS60138377A JP26072384A JP26072384A JPS60138377A JP S60138377 A JPS60138377 A JP S60138377A JP 26072384 A JP26072384 A JP 26072384A JP 26072384 A JP26072384 A JP 26072384A JP S60138377 A JPS60138377 A JP S60138377A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat exchanger
- heat recovery
- solution
- solenoid valve
- 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】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は吸収式冷暖房機の熱回収用熱交換器に係り、小
形で動量の良い熱交換器に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a heat exchanger for heat recovery in an absorption type air-conditioning/heating machine, and more particularly to a heat exchanger that is small and has good movement.
従来のサイクル系統図を第１図に、また熱回収用熱交換
器の断面形状を第２図に説明する。１は加熱源、２は加
熱器、８は分離器で凝縮器４を結ぶ配管は電磁弁１１を
介して接続されている。−山側路管は電磁弁１０を介し
て蒸発器５１に接続され、膨張弁１８と逆止弁１９を直
列に接続した配管は電磁弁１１と凝縮器を結ぶ配管から
出て蒸発器５１の他の一方に接続される。１２は膨張弁
、蒸発器は５１１５２と２分割し逆止弁１８、電磁弁１
４を介して接続される。６は吸収器、７は溶液タンク、
８は溶液ポンプ、９は熱回収熱交換器である、絞り弁１
５、逆止弁１６、は直列に接続され熱回収用熱交換器９
の希液回路（冷媒濃度の低い溶液回路）と吸収器すを接
続し、電磁弁２０および２１は凝縮器４と吸収器６、お
よび吸収器６と溶液タンク７を結ぶ回路に接続されてい
る。また電磁弁１７．２２は膨張弁１２と溶液タンク７
、熱と内管２４からなる２重看にて形成されている。A conventional cycle system diagram is shown in FIG. 1, and a cross-sectional shape of a heat recovery heat exchanger is shown in FIG. 2. 1 is a heating source, 2 is a heater, 8 is a separator, and a pipe connecting the condenser 4 is connected via a solenoid valve 11. - The mountain side pipe is connected to the evaporator 51 via the solenoid valve 10, and the pipe connecting the expansion valve 18 and the check valve 19 in series exits from the pipe connecting the solenoid valve 11 and the condenser to the evaporator 51 and other parts. connected to one side of the 12 is an expansion valve, and the evaporator is divided into 2 with 51152, check valve 18, and solenoid valve 1.
Connected via 4. 6 is an absorber, 7 is a solution tank,
8 is a solution pump, 9 is a heat recovery heat exchanger, throttle valve 1
5. The check valve 16 is connected in series to the heat recovery heat exchanger 9.
The dilute liquid circuit (solution circuit with low refrigerant concentration) is connected to the absorber, and the solenoid valves 20 and 21 are connected to the circuit connecting the condenser 4 and the absorber 6, and the absorber 6 and the solution tank 7. . In addition, the solenoid valves 17 and 22 are the expansion valve 12 and the solution tank 7.
, is formed with a double wall consisting of a heat tube and an inner tube 24.
つぎに、作動について説明する。冷房時は加熱器２内の
濃溶液は加熱源１１１′ｉ：より加熱され分離器８で冷
媒ガスと希溶液に分離される。冷媒ガスは電磁弁１０が
閉、電磁弁１１が開のため凝縮器４へ送られ、冷却され
て液化する。電磁弁２０が閉じているため液冷媒は膨張
弁１２で減圧され、電磁弁１７は閉、電磁弁１４Ｖｉ開
の状態になっているので、蒸発器５＋＋５ｒ′ｃ蒸発し
、その蒸発潜熱にて冷房を行なう。一方希溶液は電磁弁
２２が閉じているため熱回収熱交換器９で濃溶液と熱交
換した後絞り弁１５で減圧された後、蒸発器５１Ｔ５２
で蒸発した冷媒ガスを吸収し、吸収熱全発生する。Next, the operation will be explained. During cooling, the concentrated solution in the heater 2 is heated by the heating source 111'i and separated into a refrigerant gas and a dilute solution in the separator 8. Since the solenoid valve 10 is closed and the solenoid valve 11 is opened, the refrigerant gas is sent to the condenser 4, where it is cooled and liquefied. Since the solenoid valve 20 is closed, the liquid refrigerant is depressurized by the expansion valve 12, the solenoid valve 17 is closed, and the solenoid valve 14Vi is open, so the evaporator 5++5r'c evaporates, and the latent heat of evaporation cools the liquid refrigerant. Do this. On the other hand, since the solenoid valve 22 is closed, the dilute solution exchanges heat with the concentrated solution in the heat recovery heat exchanger 9, is depressurized by the throttle valve 15, and is then transferred to the evaporator 51T52.
It absorbs the refrigerant gas that has evaporated and generates all the absorption heat.
その後吸収器で冷却され液化した後電磁弁２１を通って
溶液タンク７に回収され、溶液ポンプ８で昇圧された後
、熱回収熱交換器９を通って再び加熱器２に送られ冷房
サイクルを形成する。After that, it is cooled and liquefied in the absorber, and then collected in the solution tank 7 through the electromagnetic valve 21, and after being pressurized by the solution pump 8, it is sent to the heater 2 again through the heat recovery heat exchanger 9 and starts the cooling cycle. Form.
一方暖房時は分離器８で分離した冷媒ガスが電磁弁１１
，１４．２１が閉電磁弁１０，１７．２０．２２が開に
切り換わるため、蒸発器６で熱交換し、凝縮液化し、膨
張弁１８で減圧され冷房時凝縮器４、吸収器６が蒸発器
として働き液冷媒の蒸発潜熱をくみ上げる。また希溶液
は′電磁弁２２を通過後絞り弁１５にて減圧され蒸発し
た冷媒ガスと混合した後、蒸発器５２にて吸収熱を放出
した後液化し、電磁弁１７を通り溶液タンク２に回収さ
れ、溶液ポンプ８にて昇圧され熱回収熱交換器９を通過
し、この際希溶液は電磁弁２２を流れるため熱回収せず
に加熱器２に送られる。このように暖房は冷媒の凝縮熱
と吸収熱を利用するヒートポンプサイクルである。On the other hand, during heating, the refrigerant gas separated by the separator 8 is transferred to the solenoid valve 11.
, 14.21 are closed and the solenoid valves 10, 17, 20. It works as an evaporator and pumps up the latent heat of vaporization of the liquid refrigerant. After passing through the solenoid valve 22, the dilute solution is depressurized at the throttle valve 15 and mixed with the evaporated refrigerant gas. After releasing absorbed heat at the evaporator 52, the dilute solution is liquefied, passes through the solenoid valve 17, and enters the solution tank 2. The dilute solution is recovered, pressurized by the solution pump 8, and passed through the heat recovery heat exchanger 9. At this time, the dilute solution flows through the electromagnetic valve 22, so it is sent to the heater 2 without heat recovery. In this way, heating is a heat pump cycle that uses the condensation heat and absorption heat of the refrigerant.
上記サイクルの成績係数を向上させるためには熱回収熱
交換器での熱回収量を大きくする必要があるが、従来の
場合は第２図に示したように２重管力式のため大形化し
たり、外管と内管が偏心して熱効廐の悪化を誘発してい
た。In order to improve the coefficient of performance of the above-mentioned cycle, it is necessary to increase the amount of heat recovered by the heat recovery heat exchanger, but in the conventional case, as shown in Figure 2, it is a double tube force type and is large. The outer and inner tubes were eccentric, causing deterioration in thermal efficiency.
本発明は熱回収熱交換器の熱効藁を向上させ、熱回収量
を増大させなおかつ小形化をはかることを目的とする。An object of the present invention is to improve the heat efficiency of a heat recovery heat exchanger, increase the amount of heat recovered, and reduce the size of the heat recovery heat exchanger.
本発明は熱回収熱交換器の断面形状を複数層とし、一層
は複数個の角形の集合体とし、各層毎に冷媒、希溶液、
濃溶液の８流体を流し、濃溶液に熱回収しサイクルの成
績係数の向上、熱回収熱交換器の小形化をはかるもので
ある。In the present invention, the cross-sectional shape of the heat recovery heat exchanger is made of multiple layers, one layer is an aggregate of multiple squares, and each layer has a refrigerant, a dilute solution,
This system aims to improve the coefficient of performance of the cycle and downsize the heat recovery heat exchanger by flowing eight fluids of concentrated solution and recovering heat from the concentrated solution.
〔発明の実施例）
以下本発明を第８図、第４図に示す一実施例により詳細
に説明する。[Embodiment of the Invention] The present invention will be explained in detail below with reference to an embodiment shown in FIGS. 8 and 4.
従来例と比較して分離器８から出た冷媒回路２８を熱回
収熱交換器９′の第１層２５に接続した後電磁弁１０．
１１を接続し、濃溶液回路２９を熱回収熱交換器９′の
第２層に接続した後溶液ポンプ８に接続し、希溶液回路
８０を熱回収熱交換器の第８層２７に接続した後絞り弁
１５に接続し、第８層２７の＠後を電磁弁２２で側路を
形成するところのみ相異し、その他については同一であ
る。Compared to the conventional example, after connecting the refrigerant circuit 28 from the separator 8 to the first layer 25 of the heat recovery heat exchanger 9', the solenoid valve 10.
11 was connected, the concentrated solution circuit 29 was connected to the second layer of the heat recovery heat exchanger 9', and then connected to the solution pump 8, and the dilute solution circuit 80 was connected to the eighth layer 27 of the heat recovery heat exchanger. The only difference is that it is connected to the rear throttle valve 15 and a side passage is formed behind the eighth layer 27 by a solenoid valve 22, and the rest is the same.
つぎに動作について説明する。冷房時分離器８で分離発
生した冷媒ガスは希溶液とともに熱回収熱交換器９にて
、濃溶液に熱回収され冷媒ガスは凝縮器４へ、希溶液は
絞り弁１５で減圧され、その後の作用については従来例
と同一である。また暖房時は熱回収熱交換器９゛の希溶
液回路のみ電磁弁２２で側路を形成するため、溶液ポン
プ８で昇圧される濃溶液と分離器８から分離する冷媒ガ
スが熱回収熱交換器９′で熱回収される点が従来例と相
異し、その他の作用は同一である。Next, the operation will be explained. The refrigerant gas separated and generated in the separator 8 during cooling is heat-recovered together with the dilute solution into a concentrated solution in the heat recovery heat exchanger 9. The refrigerant gas is sent to the condenser 4, and the dilute solution is depressurized by the throttle valve 15. The operation is the same as the conventional example. In addition, during heating, only the dilute solution circuit of the heat recovery heat exchanger 9' forms a bypass with the solenoid valve 22, so that the concentrated solution pressurized by the solution pump 8 and the refrigerant gas separated from the separator 8 are used for heat recovery heat exchange. This differs from the conventional example in that heat is recovered in the vessel 9', but the other functions are the same.
以上説明したように本発明は熱回収熱交換器に多層の角
形形状をした熱交換器を採用し、冷媒ガス、希溶液、濃
溶液の８流体を流すことにより濃溶液の熱回収量を増大
をはかることができ、サイクルの成績係数が向上するた
め、熱交換器類の小形化？ｌｌ−はかることもできる。As explained above, the present invention employs a multilayer prismatic heat exchanger for the heat recovery heat exchanger, and increases the amount of heat recovery from the concentrated solution by flowing eight fluids: refrigerant gas, dilute solution, and concentrated solution. Is it possible to downsize heat exchangers to improve the coefficient of performance of the cycle? ll- can also be measured.
また、熱回収熱交換器においては従来の２重管の偏心の
問題もなくなり加工性が向上する効果もある。Further, in the heat recovery heat exchanger, there is no problem of eccentricity of the conventional double pipe, and workability is improved.
第１図は従来のサイクル系統図、第２図は従来の熱回収
熱交換器の断面図、第８図は本発明のサイクル系統図、
第４図は本発明の熱回収熱交換器の断面図を示す。Fig. 1 is a conventional cycle system diagram, Fig. 2 is a sectional view of a conventional heat recovery heat exchanger, and Fig. 8 is a cycle system diagram of the present invention.
FIG. 4 shows a cross-sectional view of the heat recovery heat exchanger of the present invention.
Claims (1)
および熱回収用熱交換器などからなる吸収式冷暖房機に
おいて、冷房時には冷媒、希溶液および濃溶液を、暖房
時には冷媒と濃溶液を熱交換させる熱回収用熱交換器を
設けたことを特徴とする吸収式冷暖房機。In an absorption air-conditioning system consisting of a heater, separator, condenser, evaporator, absorber, solution pump, heat recovery heat exchanger, etc., refrigerant, dilute solution, and concentrated solution are used for cooling, and refrigerant and concentrated solution are used for heating. An absorption air-conditioning/heating machine characterized by being equipped with a heat recovery heat exchanger for exchanging heat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26072384A JPS60138377A (en) | 1984-12-12 | 1984-12-12 | Absorption type refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26072384A JPS60138377A (en) | 1984-12-12 | 1984-12-12 | Absorption type refrigerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60138377A true JPS60138377A (en) | 1985-07-23 |
Family
ID=17351861
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26072384A Pending JPS60138377A (en) | 1984-12-12 | 1984-12-12 | Absorption type refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60138377A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1588710A1 (en) | 2004-04-06 | 2005-10-26 | Shinto Fine Co., Ltd. | Anti-allergic composition and method for denaturing allergens |
-
1984
- 1984-12-12 JP JP26072384A patent/JPS60138377A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1588710A1 (en) | 2004-04-06 | 2005-10-26 | Shinto Fine Co., Ltd. | Anti-allergic composition and method for denaturing allergens |
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