JPS602540Y2 - absorption cold water machine - Google Patents

absorption cold water machine

Info

Publication number
JPS602540Y2
JPS602540Y2 JP14926279U JP14926279U JPS602540Y2 JP S602540 Y2 JPS602540 Y2 JP S602540Y2 JP 14926279 U JP14926279 U JP 14926279U JP 14926279 U JP14926279 U JP 14926279U JP S602540 Y2 JPS602540 Y2 JP S602540Y2
Authority
JP
Japan
Prior art keywords
heat exchanger
water
cold water
liquid
refrigerant
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
Application number
JP14926279U
Other languages
Japanese (ja)
Other versions
JPS5666769U (en
Inventor
省三 尾上
Original Assignee
三洋電機株式会社
東京三洋電機株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 三洋電機株式会社, 東京三洋電機株式会社 filed Critical 三洋電機株式会社
Priority to JP14926279U priority Critical patent/JPS602540Y2/en
Publication of JPS5666769U publication Critical patent/JPS5666769U/ja
Application granted granted Critical
Publication of JPS602540Y2 publication Critical patent/JPS602540Y2/en
Expired legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【考案の詳細な説明】 本案は吸収冷温水機に使用される熱交換器の改良に関し
、該熱交換器に流れる水または吸水液の流量を変化させ
た場合にも熱交換器内での氷または吸収液の流速の変化
が軽微となるように熱交換器における流れの断面積を変
化させる構成とし、熱交換器の熱伝達係数をほぼ一定に
保って吸収冷温水機の安定した運転を可能にしたもので
ある。
[Detailed description of the invention] This invention relates to the improvement of a heat exchanger used in an absorption chiller/heater. Alternatively, the cross-sectional area of the flow in the heat exchanger is changed so that the change in the flow velocity of the absorption liquid is slight, and the heat transfer coefficient of the heat exchanger is kept almost constant, allowing stable operation of the absorption chiller/heater. This is what I did.

以下に図面に従い説明すると、1は稀吸収液から冷媒を
加熱分離する高温発生器、2は該高温発生器1からの冷
媒蒸気を再熱熱源として中間液から冷媒を再熱分離する
低温発生器、3は高温発生器1及び低温発生器2からの
冷媒を冷却水による熱交換器4で冷却、凝縮する凝縮器
、5は内蔵された水熱交換器7から気化潜熱を得て冷房
用冷水を機外に供給する蒸発器、6は蒸発器5で気化し
た冷媒を吸収液で吸収させ、その吸収熱を冷却水による
熱交換器8で冷却するようにした吸収器、9は高温冷媒
を用いた温水器、10は冷媒ポンプ、11は吸収液ポン
プ、12.13は吸収液の熱交換器であり、これらは冷
媒管14および吸収液管15で接続されて冷媒および吸
収液の循環サイクルを形成している。
Referring to the drawings, 1 is a high-temperature generator that heats and separates the refrigerant from the dilute absorption liquid, and 2 is a low-temperature generator that uses the refrigerant vapor from the high-temperature generator 1 as a reheating heat source to reheat and separate the refrigerant from the intermediate liquid. , 3 is a condenser that cools and condenses the refrigerant from the high-temperature generator 1 and the low-temperature generator 2 in a heat exchanger 4 using cooling water, and 5 is a condenser that obtains latent heat of vaporization from a built-in water heat exchanger 7 to produce cold water for cooling. 6 is an absorber that absorbs the refrigerant vaporized in the evaporator 5 with an absorption liquid, and the absorbed heat is cooled in a heat exchanger 8 using cooling water; 9 is an absorber that supplies high-temperature refrigerant; The used water heater, 10 is a refrigerant pump, 11 is an absorption liquid pump, 12.13 is an absorption liquid heat exchanger, and these are connected by a refrigerant pipe 14 and an absorption liquid pipe 15 to perform a circulation cycle of the refrigerant and absorption liquid. is formed.

又、16は冷房用冷水の循環ポンプ、17は温水用循環
の温水ポンプ、18は冷却水供給ポンプであり、これら
のポンプ10,11,16,17.18はポンプの回転
数又は運転台数を制御することにより循環液量が変化で
きる機構を有している。
Further, 16 is a cold water circulation pump for air conditioning, 17 is a hot water pump for hot water circulation, and 18 is a cooling water supply pump, and these pumps 10, 11, 16, 17. It has a mechanism that allows the amount of circulating fluid to be changed by controlling it.

又、第2図は前記凝縮器3、吸収器6の冷却をする熱交
換器4,8、溶液用熱交換器12、蒸発器の冷水用熱交
換器7、温水器9に使用される熱交換器19の構造の一
例を示す図であり、液流路は複数の管群20,21から
威り、水の入口側22および出口側23には切替弁24
.25. 26が配されると共に、入口側22と出口側
23とは側路管27で接続されている。
FIG. 2 shows the heat used in the condenser 3, the heat exchangers 4 and 8 for cooling the absorber 6, the solution heat exchanger 12, the evaporator cold water heat exchanger 7, and the water heater 9. It is a diagram showing an example of the structure of the exchanger 19, in which the liquid flow path extends from a plurality of pipe groups 20 and 21, and a switching valve 24 is provided on the water inlet side 22 and outlet side 23.
.. 25. 26 is arranged, and the inlet side 22 and the outlet side 23 are connected by a side pipe 27.

斯る構成を有する本案の吸収冷温水機において、通常の
運転状態の場合は、水熱交換器の切替弁は第2図の状態
にあって定格流量(100%)に応じた熱交換を行なう
In the proposed absorption chiller/heater having such a configuration, under normal operating conditions, the switching valve of the water heat exchanger is in the state shown in Figure 2, and heat exchange is performed according to the rated flow rate (100%). .

而して、冷房(又は暖房)負荷が減少して、冷水(又は
温水)ポンプ16.17あるいはこれに伴ない冷却水ポ
ンプ18、吸収液ポンプ11の回転数や運転台数が制御
され、熱交換器4,7゜8.12,19の流量が半減す
るような場合は、切替弁24乃至26を図とは逆の開閉
状態にすることにより水熱交換器の水流断面積を半減さ
せ、ポンプの制御によって生じた水流量の循環量の減少
が熱交換器内の水流速および熱伝達の減少とならないよ
うにしている。
As a result, the cooling (or heating) load is reduced, and the rotational speed and number of operating units of the cold water (or hot water) pumps 16, 17 or accompanying cooling water pumps 18 and absorption liquid pumps 11 are controlled, and heat exchange is performed. If the flow rate of the water heat exchangers 4, 7, 8, 12, 19 is reduced by half, the water flow cross-sectional area of the water heat exchanger is halved by opening and closing the switching valves 24 to 26 in the opposite direction to that shown in the diagram. This prevents the reduction in water flow rate caused by the control from reducing the water flow rate and heat transfer within the heat exchanger.

すなわち、第2図の切替弁24.25を閉じ、26を開
いた場合、入口側22から入った水は出口側の弁25で
方向を逆転され、弁26及び側路管27を経て流出して
いくため、同時に流れることのできる水流路の管群数は
半減されて水熱交換器における水の流れの断面積が半減
される結果、ポンプ制御によって生じた水循環量の減少
分は熱交換器を流れる水流速の減少として現れず、熱交
換器の熱伝達係数の低下を防止できる。
That is, when the switching valves 24 and 25 in FIG. As a result, the number of tube groups in the water flow path that can flow simultaneously is halved, and the cross-sectional area of water flow in the water heat exchanger is halved. This does not appear as a decrease in the flow rate of water flowing through the heat exchanger, thereby preventing a decrease in the heat transfer coefficient of the heat exchanger.

それ故、例えば冷房負荷が半減した際にポンプ16の吐
出量を半減させて冷水の循環量を半減させた場合にも、
熱交換器17での冷媒と冷水との熱交換量もほぼ半減し
て負荷側には負荷に見合う冷水が供給され、熱交換器1
7における冷水の出入口温度および蒸発器5内の温度、
圧力も負荷の変化前とほぼ同程度に保たれる。
Therefore, even if, for example, when the cooling load is halved, the discharge amount of the pump 16 is halved and the amount of cold water circulated is halved.
The amount of heat exchanged between the refrigerant and cold water in the heat exchanger 17 is also reduced by almost half, and the load side is supplied with cold water corresponding to the load, and the heat exchanger 1
The temperature at the inlet and outlet of the cold water at 7 and the temperature inside the evaporator 5,
The pressure is also maintained at approximately the same level as before the load change.

すなわち、冷水の循環量を変化させた場合に蒸発器5内
の温度が変化して吸収器6その他の機器に影響を及ぼし
、吸収冷温水機の運転が不安定となるような幣害を生じ
ない。
That is, when the circulating amount of cold water is changed, the temperature inside the evaporator 5 changes, which affects the absorber 6 and other equipment, causing damage such as unstable operation of the absorption chiller/heater. do not have.

このように、本案によれば、冷暖房負荷減少時に生じる
おそれのある吸収冷凍機各部の温度の不均衡な変化を無
くして低負荷時でも安定した吸収冷凍温水機の運転が可
能となる。
As described above, according to the present invention, it is possible to eliminate imbalanced temperature changes in the various parts of the absorption chiller that may occur when the cooling/heating load is reduced, and to enable stable operation of the absorption chiller/heater even under low load.

尚、このような熱交換器4,7,8,12,19必ずし
もすべてを同時に制御する必要はなく、斯る吸収冷温水
機の運転において熱伝達率の減少が問題になる部分に限
って本案の機構を採用すれば良く、この場合において冷
水、温水、冷却水系の弁の開閉信号は各ポンプの制御発
停に、溶液の熱交換器の弁の開閉信号は冷房負荷により
作動させるのが好ましい。
It should be noted that it is not necessary to control all of these heat exchangers 4, 7, 8, 12, and 19 at the same time, and the present proposal is limited to those parts where a decrease in heat transfer coefficient becomes a problem in the operation of such an absorption chiller/heater. In this case, it is preferable that the opening/closing signals for the valves of the cold water, hot water, and cooling water systems are activated by the control start/stop of each pump, and the opening/closing signals of the valves of the solution heat exchanger are activated by the cooling load. .

【図面の簡単な説明】[Brief explanation of drawings]

第1図は吸収冷温水機の一例を示すサイクル構成図、第
2図は本案に使用する熱交換器の構造の一例を示す図で
ある。 1.2・・・・・・発生器、3・・・・・・凝縮器、5
・・・・・・蒸発器、6・・・・・・吸収器、4.7.
8. 12. 13. 19・・・・・・熱交換器、1
0,11,16.17.18・・・・・・液体ポンプ、
24,25,26・・・・・・切替弁。
FIG. 1 is a cycle configuration diagram showing an example of an absorption chiller/heater, and FIG. 2 is a diagram showing an example of the structure of a heat exchanger used in the present invention. 1.2... Generator, 3... Condenser, 5
...Evaporator, 6...Absorber, 4.7.
8. 12. 13. 19...Heat exchanger, 1
0,11,16.17.18...Liquid pump,
24, 25, 26...Switching valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 発生器、凝縮器、蒸発器、吸収器、温水器、熱交換器、
液循環量を変化し得る液体ポンプを冷媒管および吸収液
管で接続して冷媒および吸収液の循環サイクルを形成し
、かつ、凝縮器用の熱交換器、蒸発器用の熱交換器、吸
収器用の熱交換器および温水器用の熱交換器のそれぞれ
に水の流量を変化し得る液体ポンプを管で接続して水の
流路を形成し、上記のこれら熱交換器のうちの一または
二以上の熱交換器には流れの断面積を変えることができ
る切替弁付の熱交換器を用いることにより上記液体ポン
プによる流量の増減に応じて熱交換器における流れの断
面積を増減するようにしたことを特徴とする吸収冷温水
機。
generator, condenser, evaporator, absorber, water heater, heat exchanger,
A liquid pump that can change the amount of liquid circulation is connected with a refrigerant pipe and an absorption liquid pipe to form a circulation cycle for the refrigerant and absorption liquid, and a heat exchanger for the condenser, a heat exchanger for the evaporator, and a heat exchanger for the absorber are connected. A liquid pump that can change the flow rate of water is connected to each of the heat exchanger and the water heater heat exchanger with a pipe to form a water flow path, and one or more of the above heat exchangers By using a heat exchanger equipped with a switching valve that can change the cross-sectional area of the flow, the cross-sectional area of the flow in the heat exchanger can be increased or decreased in accordance with the increase or decrease in the flow rate caused by the liquid pump. An absorption chiller/heater featuring:
JP14926279U 1979-10-26 1979-10-26 absorption cold water machine Expired JPS602540Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14926279U JPS602540Y2 (en) 1979-10-26 1979-10-26 absorption cold water machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14926279U JPS602540Y2 (en) 1979-10-26 1979-10-26 absorption cold water machine

Publications (2)

Publication Number Publication Date
JPS5666769U JPS5666769U (en) 1981-06-03
JPS602540Y2 true JPS602540Y2 (en) 1985-01-24

Family

ID=29380358

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14926279U Expired JPS602540Y2 (en) 1979-10-26 1979-10-26 absorption cold water machine

Country Status (1)

Country Link
JP (1) JPS602540Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5547560B2 (en) * 2010-06-18 2014-07-16 荏原冷熱システム株式会社 Absorption heat pump

Also Published As

Publication number Publication date
JPS5666769U (en) 1981-06-03

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