JPH0378543B2 - - Google Patents
Info
- Publication number
- JPH0378543B2 JPH0378543B2 JP19057484A JP19057484A JPH0378543B2 JP H0378543 B2 JPH0378543 B2 JP H0378543B2 JP 19057484 A JP19057484 A JP 19057484A JP 19057484 A JP19057484 A JP 19057484A JP H0378543 B2 JPH0378543 B2 JP H0378543B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature generator
- solution
- low
- valve
- heating
- 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
Links
- 230000007246 mechanism Effects 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 14
- 238000010521 absorption reaction Methods 0.000 claims description 12
- 230000009977 dual effect Effects 0.000 claims description 11
- 239000003507 refrigerant Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000006096 absorbing agent Substances 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 2
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 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
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、二重効用吸収冷凍機、特に溶液ポン
プから吐出される希溶液の一部が低温発生器に、
残部が高温発生器に導かれるよう構成された二重
効用吸収冷凍機に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention provides a dual-effect absorption refrigerator, in particular, a system in which a portion of a dilute solution discharged from a solution pump is sent to a low temperature generator.
The present invention relates to a dual-effect absorption refrigerator, the remainder of which is directed to a high temperature generator.
この種の冷凍機において、部分負荷時の効率を
上昇させるためには、低温側希溶液経路と高温側
希溶液経路の各々の希溶液流量を絞る必要がある
ことは広く知られており、大型の冷凍機では、ベ
ローシール弁が流量制御弁として通常用いられて
いる。しかしベローシール弁は高価であるばかり
でなく、ベローシール部が破損し易く寿命が短い
などの欠点がある。又、小型の冷凍機は、従来、
部分負荷時の希溶液流量制御を完全には行なつて
おらず、エネルギ損失を犠牲にしている場合が多
い。
It is widely known that in order to increase the efficiency of this type of refrigerator at partial load, it is necessary to reduce the dilute solution flow rate in each of the low-temperature side dilute solution path and the high-temperature side dilute solution path. In refrigerators, bellows seal valves are commonly used as flow control valves. However, bellows seal valves are not only expensive, but also have drawbacks such as the bellows seal portion being easily damaged and having a short lifespan. In addition, small refrigerators are conventionally
Dilute solution flow control during partial loads is often not fully controlled, at the expense of energy loss.
第2図に従来の二重効用吸収冷凍機の一例を示
す。 FIG. 2 shows an example of a conventional dual-effect absorption refrigerator.
第2図において1は吸収器、2は蒸発器、3は
高温発生器、4は低温発生器、5は凝縮器、6は
高温熱交換器、7は低温熱交換器、8は溶液ポン
プ、9は冷媒ポンプ、10は絞り機構、11は自
力式フロート弁であり、これらの機器を溶液経
路、冷媒経路で接続して冷凍サイクルを形成して
いる。部分負荷になると蒸発器2の冷水出口温度
を温度検出器12により検出して、制御機構13
が熱源制御弁14を絞る。この作動により、高温
発生器3内の発生冷媒蒸気量が減少し、内圧が下
がるため、高温発生器3内の溶液液面が上昇し、
自力式フロート弁11が、高温発生器3への供給
希溶液流量を絞る。これにより最低必要量の希溶
液の加熱にのみ熱源が有効利用できる。 In FIG. 2, 1 is an absorber, 2 is an evaporator, 3 is a high temperature generator, 4 is a low temperature generator, 5 is a condenser, 6 is a high temperature heat exchanger, 7 is a low temperature heat exchanger, 8 is a solution pump, 9 is a refrigerant pump, 10 is a throttle mechanism, and 11 is a self-powered float valve, and these devices are connected through a solution path and a refrigerant path to form a refrigeration cycle. When the load becomes partial, the cold water outlet temperature of the evaporator 2 is detected by the temperature detector 12, and the control mechanism 13
throttles the heat source control valve 14. As a result of this operation, the amount of refrigerant vapor generated within the high temperature generator 3 decreases and the internal pressure decreases, so the liquid level of the solution within the high temperature generator 3 rises.
A self-powered float valve 11 throttles the flow of dilute solution supplied to the high temperature generator 3. This allows the heat source to be effectively used only for heating the minimum required amount of dilute solution.
しかるに、低温発生器4への希溶液供給経路に
は流量制御機構を設けていないため、部分負荷時
も定格負荷時と同量の希溶液が低温発生器4へ供
給されることになる。これにより必要分以外の希
溶液の加熱にも高温発生器3で発生した冷媒蒸気
が使用されるため、効率が悪くなる欠点がある。 However, since no flow rate control mechanism is provided in the dilute solution supply path to the low temperature generator 4, the same amount of dilute solution is supplied to the low temperature generator 4 even during partial load as during rated load. As a result, the refrigerant vapor generated in the high-temperature generator 3 is used to heat the dilute solution other than the required amount, resulting in a disadvantage of poor efficiency.
また、高温発生器3の自力式フロート弁11を
溶液ポンプ8の出口部に配備して、高温側及び低
温側希溶液流量を自力式フロート弁11にて制御
する方法もある。 Alternatively, there is a method in which the self-powered float valve 11 of the high temperature generator 3 is provided at the outlet of the solution pump 8 and the flow rates of the dilute solution on the high temperature side and the low temperature side are controlled by the self-powered float valve 11.
第3図にその一例を示す。 An example is shown in FIG.
第3図において第2図と同一符号の部分は同様
な構成作用を有する。この種の冷凍機では第3図
においては自力式フロート弁11を高温発生器外
に配備したものを示しているが、通常、自力式フ
ロート弁11を希溶液の機外への漏れがないよう
に高温発生器3内に配備している。このため、高
温側及び低温側希溶液流量を制御する自力式フロ
ート弁11は、流量が多い為駆動トルクの大きな
ものを使う必要がありサイズが大きくなり、径の
大きなフロートボールが必要となる故、高温発生
器3の外径寸法が大きくなる欠点がある。また、
自力式フロート弁11に溶液ポンプ8の吐出圧が
常時かかるため、特に自力式フロート弁11が閉
止側の場合第4図に示すように、フロート弁の軸
シール部19での圧力が高くなり高温発生器3の
戻りラインへ軸シール部を通して矢印方向の希溶
液の漏れ込み量が無視出来ない量となり、効率の
低下をもたらす欠点もある。 In FIG. 3, parts having the same reference numerals as in FIG. 2 have similar structural functions. In this type of refrigerator, the self-powered float valve 11 is installed outside the high-temperature generator in Fig. 3, but the self-powered float valve 11 is normally installed to prevent leakage of dilute solution to the outside of the machine. It is installed in the high temperature generator 3. For this reason, the self-powered float valve 11 that controls the flow rate of the dilute solution on the high temperature side and the low temperature side has a large flow rate, so it is necessary to use one with a large drive torque, which increases the size and requires a float ball with a large diameter. However, there is a drawback that the outer diameter of the high temperature generator 3 becomes large. Also,
Since the discharge pressure of the solution pump 8 is constantly applied to the self-powered float valve 11, especially when the self-powered float valve 11 is on the closed side, as shown in FIG. There is also the drawback that the amount of dilute solution leaking in the direction of the arrow through the shaft seal into the return line of the generator 3 becomes a non-negligible amount, resulting in a decrease in efficiency.
本発明は、吸収器、蒸発器、凝縮器、低温発生
器、高温発生器、溶液熱交換器、溶液ポンプ、冷
媒ポンプ及びこれらを接続する溶液経路、冷媒経
路及び高温発生器の熱源制御機構、蒸発器の冷水
負荷検出機構を有し、前記冷水負荷検出機構の信
号により前記高温発生器熱源制御機構が前記高温
発生器の加熱量を高加熱、低加熱、加熱停止と段
階制御するように構成され、前記溶液ポンプから
送られる希溶液の一部が、前記熱交換器を経由し
て前記低温発生器に導かれ、残部が前記熱交換器
を経由して前記高温発生器に導かれるように構成
された二重効用吸収冷凍機において、前記吸収器
から前記熱交換器を経由して前記低温発生器に到
る希溶液経路を配備し、該経路中に開閉弁と絞り
機構を設けて、該開閉弁を前記低加熱信号により
前記低温再生器への希溶液送り量が減少するよう
に制御することを特徴とする二重効用吸収冷凍機
であつて、従来の二重効用吸収冷凍機の前記の欠
点を取り除き、部分負荷時にも効率の良い安価で
信頼性のある二重効用吸収冷凍機を提供するもの
である。
The present invention provides an absorber, an evaporator, a condenser, a low-temperature generator, a high-temperature generator, a solution heat exchanger, a solution pump, a refrigerant pump, a solution path connecting these, a refrigerant path, and a heat source control mechanism for the high-temperature generator. It has a cold water load detection mechanism for the evaporator, and is configured such that the high temperature generator heat source control mechanism controls the heating amount of the high temperature generator in stages such as high heating, low heating, and heating stop based on a signal from the cold water load detection mechanism. and a part of the dilute solution sent from the solution pump is guided to the low temperature generator via the heat exchanger, and the remaining part is guided to the high temperature generator via the heat exchanger. In the configured dual-effect absorption refrigerator, a dilute solution path is provided from the absorber to the low temperature generator via the heat exchanger, and an on-off valve and a throttle mechanism are provided in the path, The on-off valve is controlled by the low heating signal so that the amount of dilute solution sent to the low-temperature regenerator is reduced, the double-effect absorption refrigerating machine being different from the conventional dual-effect absorption refrigerating machine. The object of the present invention is to eliminate the above-mentioned drawbacks and provide a dual-effect absorption refrigerator that is efficient, inexpensive, and reliable even under partial load.
つぎに本発明の実施例を第1図に基いて説明す
る。 Next, an embodiment of the present invention will be explained based on FIG.
第1図において第2図と同一符号の部分は同様
な構成、作用を有する。また15,16は絞り機
構、17は電磁弁であり、低温発生器4への希溶
液経路の一部を並列2連とし、片方に絞り機構1
5を設け他方に絞り機構16と電磁弁17を設
け、絞り機構15,16の開口面積を、両者合わ
せて定格負荷時に低温発生器4への供給が必要な
希溶液流量を確保できる面積(即ち第2図中の絞
り機構10の開口面積)に、また、絞り機構15
の開口面積を部分負荷時に低温発生器4へ供給が
必要な希溶液流量を確保できる面積に設定してあ
る。部分負荷時に蒸発器2の冷水出口温度を温度
検出器12により検出して、制御機構13が熱源
制御弁14を絞ると同時に、同じ信号により電磁
弁17を閉じることにより、流量制御を行なう。 In FIG. 1, parts having the same reference numerals as those in FIG. 2 have similar structures and functions. In addition, 15 and 16 are throttle mechanisms, and 17 is a solenoid valve, and a part of the dilute solution path to the low temperature generator 4 is made into two series in parallel, with one throttle mechanism on one side.
5 is provided, and the other is provided with a throttle mechanism 16 and a solenoid valve 17, and the opening area of the throttle mechanisms 15 and 16 is set to an area that can secure the dilute solution flow rate required to be supplied to the low temperature generator 4 at the rated load (i.e. The aperture area of the aperture mechanism 10 in FIG.
The opening area is set to an area that can secure the flow rate of the dilute solution necessary to be supplied to the low temperature generator 4 during partial load. At partial load, the cold water outlet temperature of the evaporator 2 is detected by the temperature detector 12, and the control mechanism 13 throttles the heat source control valve 14 and at the same time closes the electromagnetic valve 17 using the same signal, thereby controlling the flow rate.
又、第1図に示す例では、電磁弁17と絞り機
構16を分けているが、もちろん電磁弁17のポ
ート径を適切に選ぶことができるならば、絞り機
構16を省き、電磁弁で兼用することもできる。
又、全開−全閉型の電磁弁ではなく、開度切替型
(開度大−小)の電磁弁を用いることにより、低
温発生器4への希溶液経路を並列多連にすること
なく本発明を実施できる。 In addition, in the example shown in Fig. 1, the solenoid valve 17 and the throttle mechanism 16 are separated, but of course if the port diameter of the solenoid valve 17 can be appropriately selected, the throttle mechanism 16 can be omitted and the solenoid valve can be used for both purposes. You can also.
In addition, by using an opening switching type (large to small opening) solenoid valve instead of a fully open-fully closed type solenoid valve, the main dilute solution path to the low temperature generator 4 can be routed to the low temperature generator 4 without having to connect multiple lines in parallel. Able to carry out inventions.
第5図にその実施例を示す。前記図と同一符号
の部分は同様な構成、作用を有する。又電磁弁1
8は開度が大及び小の時それぞれ所定の開口面積
となるように設定されている。熱源制御弁14の
制御機構13の高加熱信号により、該電磁弁18
の開度を大とし又低加熱信号により小とならし
め、低温発生器4への希溶液流量を制御できる。 An example is shown in FIG. Portions with the same reference numerals as those in the above figures have similar configurations and functions. Also, solenoid valve 1
8 is set to have a predetermined opening area when the opening degree is large and small. Due to the high heating signal of the control mechanism 13 of the heat source control valve 14, the solenoid valve 18
The dilute solution flow rate to the low temperature generator 4 can be controlled by increasing the opening degree and making it small by the low heating signal.
本発明によれば、部分負荷時に低温発生器への
希溶液供給量を適切に絞ることができる為、従来
の高温発生器への希溶液供給量制御と相まつて部
分負荷時に効率の良い、安価で信頼性の高い二重
効用吸収冷凍機を提供することができ、実用上極
めて大なる効果を奏す。
According to the present invention, since the amount of dilute solution supplied to the low-temperature generator can be appropriately reduced during partial load, it can be combined with the conventional control of the amount of dilute solution supplied to the high-temperature generator to be efficient and inexpensive during partial load. This makes it possible to provide a highly reliable dual-effect absorption refrigerator, which is extremely effective in practice.
第1図及び第5図は本発明の実施例のフローシ
ートを示し、第2図第3図は従来の例のフローシ
ートを示す。また、第4図は自力式フロート弁の
構造例を示す。
1…吸収器、2…蒸発器、3…高温発生器、4
…低温発生器、5…凝縮器、6…高温熱交換器、
7…低温熱交換器、8…溶液ポンプ、9…冷媒ポ
ンプ、10…絞り機構、11…自力式フロート
弁、12…温度検出器、13…制御機構、14…
熱源制御弁、15,16…絞り機構、17,18
…電磁弁、19…軸シール部。
FIGS. 1 and 5 show flow sheets of an embodiment of the present invention, and FIGS. 2 and 3 show flow sheets of conventional examples. Moreover, FIG. 4 shows an example of the structure of a self-powered float valve. 1...Absorber, 2...Evaporator, 3...High temperature generator, 4
...low temperature generator, 5...condenser, 6...high temperature heat exchanger,
7... Low temperature heat exchanger, 8... Solution pump, 9... Refrigerant pump, 10... Throttle mechanism, 11... Self-powered float valve, 12... Temperature detector, 13... Control mechanism, 14...
Heat source control valve, 15, 16... throttle mechanism, 17, 18
... Solenoid valve, 19... Shaft seal section.
Claims (1)
発生器、溶液熱交換器、溶液ポンプ、冷媒ポンプ
及びこれらを接続する溶液経路、冷媒経路及び蒸
発器の冷水負荷検出機構と、該負荷検出機構の信
号により前記高温発生器の加熱源を高加熱、低加
熱、加熱停止と段階的に制御する機構を有し、前
記溶液ポンプから送られる溶液の一部が前記低温
発生器に、残部が前記高温発生器に導かれるよう
に構成され、且つ、前記高温発生器に液面を保持
するための溶液流量制御機構を有する二重効用吸
収冷凍機において、前記溶液ポンプから低温発生
器への溶液経路に開閉弁を設け、前記冷水負荷検
出機構が高温発生器加熱源制御機構に送る低加熱
信号により、該開閉弁を低温発生器への溶液流量
を減少させるよう動作させることを特徴とする二
重効用吸収冷凍機。 2 前記開閉弁が電磁弁であり、電磁弁励磁時と
非励磁時に所定のポート径を弁部に保持するよう
構成されている特許請求の範囲第1項記載の二重
効用吸収冷凍機。 3 前記低温発生器への溶液経路を並列二連化
し、該経路の一方に流量制限オリフイスを他方に
開閉弁を設けた特許請求の範囲第1項記載の二重
効用吸収冷凍機。[Claims] 1. Absorber, evaporator, condenser, low-temperature generator, high-temperature generator, solution heat exchanger, solution pump, refrigerant pump, and the solution path connecting these, the refrigerant path, and the chilled water load of the evaporator. a detection mechanism, and a mechanism for controlling the heating source of the high temperature generator in stages such as high heating, low heating, and heating stop based on the signal from the load detection mechanism, and a part of the solution sent from the solution pump is In the dual-effect absorption refrigerator, the solution pump is configured to have a solution flow rate control mechanism for maintaining a liquid level in the high-temperature generator, and the remaining portion is guided to the high-temperature generator in the low-temperature generator. An on-off valve is provided in the solution path from to the low-temperature generator, and the on-off valve is operated to reduce the solution flow rate to the low-temperature generator in response to a low heating signal sent by the cold water load detection mechanism to the high temperature generator heating source control mechanism. A dual-effect absorption refrigerator characterized by: 2. The dual-effect absorption refrigerator according to claim 1, wherein the opening/closing valve is a solenoid valve, and the valve portion is configured to maintain a predetermined port diameter when the solenoid valve is energized and de-energized. 3. The dual-effect absorption refrigerator according to claim 1, wherein two solution paths to the low temperature generator are arranged in parallel, and one of the paths is provided with a flow rate limiting orifice and the other path is provided with an on-off valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19057484A JPS6170353A (en) | 1984-09-13 | 1984-09-13 | Double effect absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19057484A JPS6170353A (en) | 1984-09-13 | 1984-09-13 | Double effect absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6170353A JPS6170353A (en) | 1986-04-11 |
| JPH0378543B2 true JPH0378543B2 (en) | 1991-12-16 |
Family
ID=16260323
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19057484A Granted JPS6170353A (en) | 1984-09-13 | 1984-09-13 | Double effect absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6170353A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2708809B2 (en) * | 1988-09-28 | 1998-02-04 | 三洋電機株式会社 | Control method of absorption refrigerator |
| JPH02101354A (en) * | 1988-10-05 | 1990-04-13 | Sanyo Electric Co Ltd | Method for controlling absorptive type freezer |
-
1984
- 1984-09-13 JP JP19057484A patent/JPS6170353A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6170353A (en) | 1986-04-11 |
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