JPH0758146B2 - Absorption cold / hot water device - Google Patents
Absorption cold / hot water deviceInfo
- Publication number
- JPH0758146B2 JPH0758146B2 JP2411960A JP41196090A JPH0758146B2 JP H0758146 B2 JPH0758146 B2 JP H0758146B2 JP 2411960 A JP2411960 A JP 2411960A JP 41196090 A JP41196090 A JP 41196090A JP H0758146 B2 JPH0758146 B2 JP H0758146B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- heat source
- valve
- evaporator
- pipe
- 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 - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 63
- 238000010521 absorption reaction Methods 0.000 title claims description 34
- 239000003507 refrigerant Substances 0.000 claims description 145
- 239000006096 absorbing agent Substances 0.000 claims description 31
- 239000012530 fluid Substances 0.000 claims description 23
- 238000001514 detection method Methods 0.000 claims description 15
- 238000005057 refrigeration Methods 0.000 claims description 11
- 239000000470 constituent Substances 0.000 claims description 6
- 238000001816 cooling Methods 0.000 description 13
- 238000010586 diagram Methods 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 7
- 239000000498 cooling water Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 3
- 235000006506 Brasenia schreberi Nutrition 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、吸収冷温水装置に係
り、特にエンジンの排出熱などを熱源として運転する吸
収冷温水装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption cold / hot water system, and more particularly to an absorption cold / hot water system which operates using exhaust heat of an engine as a heat source.
【0002】[0002]
【従来の技術】通常、吸収冷凍機では、冷房運転時は、
吸収器、凝縮器に冷却水を通水し、発生器に熱源となる
温水(エンジンの排出熱など)を通し、蒸発器から、冷
房用の冷水を取り出す。冷房サイクルは通常の吸収冷凍
サイクルで運転される。一方、暖房の場合は、熱源とな
る温水と、暖房用温水とを直接、熱交換させてもよいの
であるが、空調用流体(冷水、温水)の経路が、冷房と
暖房とで異なり、切替弁が必要になる。すなわち、冷水
は蒸発器から、温水は熱源温水と暖房温水との熱交換器
から得ることになる。2. Description of the Related Art Normally, in an absorption refrigerator, during cooling operation,
Cooling water is passed through the absorber and condenser, hot water that is a heat source (heat discharged from the engine, etc.) is passed through the generator, and cold water for cooling is taken out from the evaporator. The cooling cycle operates as a normal absorption refrigeration cycle. On the other hand, in the case of heating, the hot water serving as a heat source and the hot water for heating may be directly heat-exchanged, but the route of the air conditioning fluid (cool water, hot water) is different between cooling and heating. I need a valve. That is, cold water is obtained from the evaporator, and hot water is obtained from the heat exchanger between the heat source hot water and the heating hot water.
【0003】また、エンジンの排出熱などを熱源として
運転する吸収冷凍装置では、吸収冷凍装置の役目として
冷水を製造する以外に、熱源である排出熱を冷却する役
目がある。通常、エンジンの排出熱などを熱源として運
転する吸収冷凍装置では、発生器に入る熱源の量(温水
流量あるいは蒸気量)を調節して、冷水温度を制御し、
熱源温度が高すぎる場合には、ラジエータ(あるいは冷
却器)を用いて、熱源の熱を放出するのが一般的であ
る。Further, in the absorption refrigeration system which operates by using the exhaust heat of the engine as a heat source, the absorption refrigeration system serves not only to produce cold water but also to cool the exhaust heat as a heat source. Usually, in an absorption refrigeration system that operates using exhaust heat of an engine as a heat source, the amount of heat source entering the generator (hot water flow rate or steam amount) is adjusted to control the cold water temperature,
When the temperature of the heat source is too high, it is common to use a radiator (or a cooler) to release the heat of the heat source.
【0004】[0004]
【発明が解決しようとする課題】本発明は、同一の機器
から温度制御された冷水、温水が取り出せ、しかも熱源
を放出するラジエータ(あるいは冷却器)の役目を兼用
することのできる吸収冷温水装置を提供することを目的
とする。DISCLOSURE OF THE INVENTION The present invention provides an absorption cold / hot water apparatus which can take out cold water and hot water of which temperature is controlled from the same equipment and can also serve as a radiator (or a cooler) which releases a heat source. The purpose is to provide.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
に、本発明では、発生器、凝縮器、吸収器、蒸発器、溶
液熱交換器を主要構成機器とし、これらを溶液配管、冷
媒配管で結んでサイクルを構成する吸収冷温水装置にお
いて、発生器又は凝縮器の冷媒蒸気を、吸収器又は蒸発
器に導く冷媒蒸気配管を設け、該蒸気配管には冷媒蒸気
弁を設け、また、蒸発器を通る外部流体通路に温度検出
器を設け、発生器を通る外部流体通路には熱源過剰度検
出器を設けるとともに、前記温度検出器及び熱源過剰度
検出器からの検出値を基に冷媒蒸気弁の調節を行う機構
としたことを特徴とする吸収冷温水装置としたものであ
り、また、本発明では、発生器、凝縮器、吸収器、蒸発
器、溶液熱交換器を主要構成機器とし、これらを溶液配
管、冷媒配管で結んでサイクルを構成する吸収冷温水装
置において、凝縮器、蒸発器の冷媒系統から、吸収器、
溶液熱交換器、発生器の溶液循環系に冷媒を導く冷媒配
管を設け、該冷媒配管には冷媒弁を設け、また、蒸発器
を通る外部流体通路に温度検出器を設け、発生器を通る
外部流体通路には熱源過剰度検出器を設けるとともに、
前記温度検出器及び熱源過剰度検出器からの検出値を基
に冷媒弁の調節を行う機構としたことを特徴とする吸収
冷凍装置としたものである。In order to achieve the above object, in the present invention, a generator, a condenser, an absorber, an evaporator and a solution heat exchanger are main constituent devices, and these are solution pipes and refrigerant pipes. In the absorption chilled / hot water device that is connected by the above to form a cycle, a refrigerant vapor pipe for guiding the refrigerant vapor of the generator or the condenser to the absorber or the evaporator is provided, and a refrigerant vapor valve is provided in the vapor pipe, and the evaporation is also performed. A temperature detector is provided in the external fluid passage passing through the reactor, and a heat source excess degree detector is provided in the external fluid passage passing through the generator.Refrigerant vapor based on the detection values from the temperature detector and the heat source excess degree detector. An absorption cold / hot water device characterized by having a mechanism for adjusting a valve, and in the present invention, a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger as main constituent devices. , Connect these with solution piping and refrigerant piping. In the absorption cold water system constituting a cycle, a condenser, a refrigerant system of the evaporator, the absorber,
A refrigerant pipe for guiding a refrigerant to the solution circulation system of the solution heat exchanger and the generator is provided, a refrigerant valve is provided to the refrigerant pipe, and a temperature detector is provided to an external fluid passage passing through the evaporator, and the generator is passed through the generator. A heat source excess detector is installed in the external fluid passage,
An absorption refrigerating apparatus is characterized in that a mechanism for adjusting a refrigerant valve is provided based on detection values from the temperature detector and the heat source excess degree detector.
【0006】上記の吸収冷温水装置において、冷媒蒸気
弁及び冷媒弁の弁の調節を行う機構は、熱源過剰度検出
器からの弁を開方向にする検出値を、温度検出器からの
弁を閉方向にする検出値よりも優先させる機構とするの
がよい。In the above-described absorption cold / hot water system, the mechanism for adjusting the valves of the refrigerant vapor valve and the refrigerant valve uses the detection value for opening the valve from the heat source excess degree detector as the valve value from the temperature detector. It is preferable that the detection value in the closing direction is prioritized over the detection value.
【0007】更に、本発明では、発生器、凝縮器、吸収
器、蒸発器、溶液熱交換器を主要構成機器とし、これら
を溶液配管、冷媒配管で結んでサイクルを構成する吸収
冷温水装置において、発生器又は凝縮器の冷媒蒸気を、
吸収器又は蒸発器に導く冷媒蒸気配管を設け、該蒸気配
管には冷媒蒸気弁を設け、また、凝縮器、蒸発器の冷媒
系統から、吸収器、溶液熱交換器、発生器の溶液循環系
に冷媒を導く冷媒配管を設け、該冷媒配管には冷媒弁を
設け、更に、蒸発器を通る外部流体通路に温度検出器を
設け、発生器を通る外部流体通路には熱源過剰度検出器
を設けるとともに、前記温度検出器からの検出値を基に
前記冷媒弁の調節を行い、前記熱源過剰度検出器からの
検出値を基に冷媒蒸気弁の調節を行う機構としたことを
特徴とする吸収冷温水装置としたものである。Further, according to the present invention, in the absorption cold / hot water apparatus in which a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger are main constituent devices, and these are connected by a solution pipe and a refrigerant pipe to form a cycle. , The refrigerant vapor of the generator or condenser,
A refrigerant vapor pipe leading to the absorber or the evaporator is provided, a refrigerant vapor valve is provided in the vapor pipe, and a refrigerant circulation system of a condenser, an evaporator, a solution circulation system of an absorber, a solution heat exchanger, and a generator. A refrigerant pipe for guiding a refrigerant is provided, a refrigerant valve is provided in the refrigerant pipe, a temperature detector is provided in an external fluid passage passing through the evaporator, and a heat source excess detector is provided in the external fluid passage passing through the generator. A mechanism for adjusting the refrigerant valve based on the detection value from the temperature detector and adjusting the refrigerant vapor valve based on the detection value from the heat source excess degree detector is provided. It is an absorption cold / hot water device.
【0008】上記の吸収冷温水装置において、熱源過剰
度検出器としては、熱源が温水の場合は熱源温度計を用
いるのがよく、また、熱源が蒸気の場合は熱源温度計又
は熱源蒸気圧計を用いるのがよい。In the above-mentioned absorption cold / hot water system, the heat source excess detector is preferably a heat source thermometer when the heat source is hot water, and a heat source thermometer or a heat source steam pressure meter when the heat source is steam. Good to use.
【0009】[0009]
【作用】本発明では、発生器に入ってくる熱源熱量は、
直接的には調節せず、発生器に入ってきた熱源で、溶液
を常に加熱濃縮する。冷水の温度制御は、冷水温度が高
い場合すなわち、冷凍機の冷凍能力が、冷房負荷より小
さい場合は、冷媒蒸気弁又は冷媒弁を閉止する。それで
も高い場合、熱源熱量が不足しており、制御の範囲外で
ある。冷水温度が低い場合すなわち、冷凍機の冷凍能力
が、冷房負荷より大きい場合は、冷媒蒸気配管と弁を設
けた装置では高圧側(発生器および凝縮器)の冷媒蒸気
を、冷媒蒸気弁を通して、低圧側(吸収器および蒸発
器)に放出する。吸収器では、高圧側からの冷媒蒸気
と、蒸発器からの冷媒蒸気とを吸収することになり、蒸
発器での冷媒蒸発量が制限され、冷凍機の能力を減少さ
せることができる。In the present invention, the heat quantity of the heat source coming into the generator is
Rather than directly controlling, the heat source coming into the generator always heats and concentrates the solution. The cold water temperature control closes the refrigerant vapor valve or the refrigerant valve when the cold water temperature is high, that is, when the refrigerating capacity of the refrigerator is smaller than the cooling load. If it is still high, the heat source heat quantity is insufficient and out of the control range. When the cold water temperature is low, that is, when the refrigerating capacity of the refrigerator is larger than the cooling load, in the device provided with the refrigerant vapor piping and valve, the refrigerant vapor on the high pressure side (generator and condenser) is passed through the refrigerant vapor valve, Discharge to low pressure side (absorber and evaporator). In the absorber, the refrigerant vapor from the high pressure side and the refrigerant vapor from the evaporator are absorbed, the amount of refrigerant vaporized in the evaporator is limited, and the capacity of the refrigerator can be reduced.
【0010】また、冷媒配管と弁を設けた装置では、冷
媒系統(蒸発器及び凝縮器系)の冷媒(主に冷媒液)
を、冷媒弁を通して、溶液循環系統(吸収器、溶液熱交
換器、発生器系統)に放出する。これにより、溶液濃度
が低下し、吸収器の吸収能力が減少し、蒸発器での冷媒
蒸発量が少なくなり、冷凍機の能力を減少させることが
できる。Further, in the device provided with the refrigerant pipe and the valve, the refrigerant (mainly the refrigerant liquid) of the refrigerant system (evaporator and condenser system) is used.
Is discharged to the solution circulation system (absorber, solution heat exchanger, generator system) through the refrigerant valve. As a result, the solution concentration decreases, the absorption capacity of the absorber decreases, the amount of refrigerant evaporated in the evaporator decreases, and the capacity of the refrigerator can be reduced.
【0011】熱源温度は、高すぎるとエンジンの冷却に
支障をきたすが、低下に対しては、特に考慮しなくてよ
い。吸収冷凍機の熱源として使って、エンジンに支障を
きたすほど低下することはない。熱源温度が高い場合
(熱源が過剰の場合)、冷媒蒸気配管と弁を設けた装置
では、冷媒蒸気弁を開方向にして、発生器または凝縮器
の冷媒蒸気を、吸収器または蒸発器に放出し、発生器の
冷媒蒸気圧を低下させ、それに伴い発生器溶液の温度低
下させて、発生器で熱源の熱量を消費させて、熱源温度
あるいは熱源蒸気圧を低下させる。この運転は、この装
置を暖房運転に用いる場合の運転であり、冷却水の導入
をとめて、冷媒蒸気を蒸発器で凝縮させて、蒸発器の外
部液通路に温水を通すと暖房運転ができる。If the heat source temperature is too high, the cooling of the engine will be hindered, but the lowering of the heat source temperature need not be considered. It can be used as a heat source for an absorption chiller, and does not reduce the temperature to a level that would damage the engine. When the heat source temperature is high (when the heat source is excessive), in the device equipped with the refrigerant vapor pipe and valve, the refrigerant vapor valve is opened and the refrigerant vapor from the generator or condenser is discharged to the absorber or evaporator. Then, the refrigerant vapor pressure of the generator is reduced, the temperature of the generator solution is reduced accordingly, and the heat amount of the heat source is consumed in the generator to reduce the heat source temperature or the heat source vapor pressure. This operation is an operation when this device is used for heating operation, and heating operation can be performed by stopping the introduction of cooling water, condensing the refrigerant vapor in the evaporator, and passing hot water through the external liquid passage of the evaporator. .
【0012】また、冷媒配管と弁を設けた装置では、前
記冷媒弁を開方向にして、冷媒系統(蒸発器および凝縮
器系)の冷媒(主に冷媒液)を、冷媒弁を通して、溶液
循環系統(吸収器、溶液熱交換器、発生器系統)に放出
する。これにより、溶液濃度が低下し、発生器での沸騰
温度が低下する。従って、発生器で熱源の熱量を多く消
費させて、熱源温度あるいは熱源蒸気圧を低下させるこ
とができる。Further, in an apparatus provided with a refrigerant pipe and a valve, the refrigerant valve is opened and the refrigerant (mainly the refrigerant liquid) in the refrigerant system (evaporator and condenser system) is circulated through the refrigerant valve in the solution circulation. Discharge to the system (absorber, solution heat exchanger, generator system). This reduces the solution concentration and the boiling temperature in the generator. Therefore, it is possible to consume a large amount of heat of the heat source in the generator and reduce the heat source temperature or the heat source vapor pressure.
【0013】次に、冷媒配管と弁及び冷媒蒸気配管と弁
の両方を設けた装置においては、冷水の温度制御は、冷
水温度が高い場合は、冷媒弁を閉止する。冷水温度が低
い場合は、冷媒系統(蒸発器および凝縮器系)の冷媒
(主に冷媒液)を、冷媒弁を通して、溶液循環系統(吸
収器、溶液熱交換器、発生器系統)に放出する。これに
より、溶液濃度が低下し、吸収器の吸収能力が減少し、
蒸発器での冷媒蒸発量が少なくなり、冷凍機の能力を減
少させることができる。Next, in the apparatus provided with both the refrigerant pipe and the valve and the refrigerant vapor pipe and the valve, the temperature control of the cold water closes the refrigerant valve when the cold water temperature is high. When the cold water temperature is low, the refrigerant (mainly the refrigerant liquid) of the refrigerant system (evaporator and condenser system) is discharged to the solution circulation system (absorber, solution heat exchanger, generator system) through the refrigerant valve. . This reduces the solution concentration and reduces the absorption capacity of the absorber,
The amount of refrigerant evaporated in the evaporator is reduced, and the capacity of the refrigerator can be reduced.
【0014】熱源温度が高い場合(熱源が過剰の場
合)、冷媒蒸気弁を開方向にして、発生器または凝縮器
の冷媒蒸気を、吸収器または蒸発器に放出し、発生器の
冷媒蒸気圧を低下させ、それに伴い発生器溶液の温度を
低下させて、発生器で熱源の熱量を消費させて、熱源温
度あるいは熱源蒸気圧を低下させる。When the heat source temperature is high (when the heat source is excessive), the refrigerant vapor valve is opened and the refrigerant vapor of the generator or condenser is discharged to the absorber or evaporator, and the refrigerant vapor pressure of the generator is increased. Is lowered, and the temperature of the generator solution is lowered accordingly, and the amount of heat of the heat source is consumed in the generator to lower the heat source temperature or the heat source vapor pressure.
【0015】そして、本発明においては、蒸発器を通る
外部流体通路に温度検出器を設けて該流体温度を検出
し、また発生器を通る外部流体通路には熱源過剰度検出
器を設けて、該流体の温度又は蒸気圧を検出して、該検
出値に基づいて、冷媒蒸気弁又は冷媒弁を調節する機構
としているため、自動的に冷水温度及び熱源温度が制御
でき一定に保つことができる。In the present invention, a temperature detector is provided in the external fluid passage passing through the evaporator to detect the temperature of the fluid, and a heat source excess detector is provided in the external fluid passage passing through the generator. Since the temperature or vapor pressure of the fluid is detected and the refrigerant vapor valve or the mechanism for adjusting the refrigerant valve is adjusted based on the detected value, the cold water temperature and the heat source temperature can be automatically controlled and kept constant. .
【0016】[0016]
【実施例】以下、本発明を実施例により具体的に説明す
るが、本発明はこれらに限定されるものではない。EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited thereto.
【0017】実施例1 図1に本発明の吸収冷凍装置のフロー構成図を示す。図
1において、Gは発生器、Aは吸収器、Eは蒸発器、C
は凝縮器、Hは溶液熱交換器、V1 は冷媒蒸気弁、1
1,12はポンプ、TH は熱源過剰度検出器、TC は冷
水温度検出器、17は冷却塔、管1〜4は溶液通路、管
5〜6は冷媒通路、管8は冷媒蒸気配管、管13,14
は熱源通路、管18は冷水通路、19〜20は冷却水通
路を示す。Embodiment 1 FIG. 1 shows a flow diagram of the absorption refrigeration system of the present invention. In FIG. 1, G is a generator, A is an absorber, E is an evaporator, and C is
Is a condenser, H is a solution heat exchanger, V 1 is a refrigerant vapor valve, 1
1, 12 are pumps, T H is a heat source excess detector, T C is a cold water temperature detector, 17 is a cooling tower, pipes 1 to 4 are solution passages, pipes 5 to 6 are refrigerant passages, and pipe 8 is refrigerant vapor piping. , Tubes 13, 14
Is a heat source passage, pipe 18 is a cold water passage, and 19 to 20 are cooling water passages.
【0018】次に、この装置を用いた冷房サイクルを説
明する。冷媒を吸収した希溶液は吸収器Aから管1を通
り、ポンプ11により熱交換器Hの被加熱側に送られ、
熱交換により加温された希溶液は管2を通り発生器Gに
導入される。発生器Gでは、管13からのエンジンのジ
ャケット温水等の熱源により加熱されて、吸収した冷媒
蒸気を蒸発して濃縮される。濃縮された濃溶液は管3か
ら熱交換器Hの加熱側を通って、管4から吸収器Aに導
入され再び冷媒を吸収して希溶液となって管1から循環
される。Next, a cooling cycle using this device will be described. The diluted solution that has absorbed the refrigerant passes from the absorber A through the pipe 1 and is sent to the heated side of the heat exchanger H by the pump 11.
The diluted solution heated by heat exchange is introduced into the generator G through the tube 2. In the generator G, the refrigerant vapor that has been heated by a heat source such as hot water of the engine jacket from the pipe 13 is evaporated and concentrated. The concentrated concentrated solution passes from the pipe 3 through the heating side of the heat exchanger H, is introduced from the pipe 4 to the absorber A, absorbs the refrigerant again, and becomes a dilute solution, which is circulated from the pipe 1.
【0019】一方、発生器Gで発生した冷媒蒸気は凝縮
器Cに至り、凝縮器C中の冷却水によって冷却されて凝
縮し、管5から蒸発器Eに導入される。蒸発器Eでは、
冷媒は冷水から熱を奪い、冷凍効果を発揮して蒸発す
る。蒸発した冷媒蒸気は吸収器Aで溶液に吸収される。
吸収の際の吸収熱は吸収器Aを流れる管19からの冷却
水により冷却される。On the other hand, the refrigerant vapor generated in the generator G reaches the condenser C, is cooled by the cooling water in the condenser C, is condensed, and is introduced into the evaporator E from the pipe 5. In the evaporator E,
The refrigerant takes heat from the cold water, exerts a freezing effect, and evaporates. The vaporized refrigerant vapor is absorbed by the solution in the absorber A.
The absorbed heat at the time of absorption is cooled by the cooling water from the pipe 19 flowing through the absorber A.
【0020】このような冷房サイクルにおいて、冷水温
度又は熱源温度が変動し、調整の必要が生じた場合は、
凝縮器から蒸発器に導く冷媒蒸気配管8の冷媒蒸気弁V
1 の開度を調節することにより行う。まず、冷水温度検
出器TC 及び熱源過剰度検出器TH により、冷水温度及
び熱源温度を検出し、その検出値に基づいて、冷媒蒸気
弁V1 を調節する。In such a cooling cycle, when the chilled water temperature or the heat source temperature fluctuates and adjustment becomes necessary,
Refrigerant vapor valve V of the refrigerant vapor pipe 8 leading from the condenser to the evaporator
This is done by adjusting the opening of 1 . First, the cold water temperature detector T C and the heat source excessive Detector T H, detects the cold water temperature and heat source temperature, based on the detected value, to adjust the refrigerant vapor valve V 1.
【0021】具体的には冷媒蒸気弁V1 の調節は、熱源
過剰度検出器TH からの弁を開方向にする検出値を、前
記蒸発器外部流体温度検出器TC からの弁を閉方向にす
る検出値よりも優先させるのがよく、その例を図2にフ
ローチャートで示す。図3は、図2のフローチャートを
グラフにしたものである。図中TCOは冷水目標温度、T
HOは熱源目標温度を示す。Specifically, the refrigerant vapor valve V 1 is adjusted by closing the valve from the evaporator external fluid temperature detector T C with a detected value from the heat source excess detector T H in the opening direction. It is preferable to give priority to the detection value to be oriented, and an example thereof is shown in a flowchart in FIG. FIG. 3 is a graph of the flowchart of FIG. In the figure, T CO is the cold water target temperature, T
HO indicates the heat source target temperature.
【0022】図4及び図5に、冷媒蒸気弁V1 の調節に
関し、熱源過剰度検出器TH から弁開度を求め、また、
前記蒸発器外部流体温度検出器TC からも弁の開度を求
める例を示す。弁の調節には、大きい方の値を用いる。
冷媒蒸気弁V1 の開度は、熱源過剰度検出器THの検出
値、蒸発器外部流体温度検出器TC からの検出値から演
算で求め、それをもとに調節してもよい。なお高圧側か
らの低圧側に導く冷媒蒸気中には、冷媒液が入っても差
し支えない。4 and 5, regarding the adjustment of the refrigerant vapor valve V 1 , the valve opening is obtained from the heat source excess detector T H , and
An example of obtaining the valve opening from the evaporator external fluid temperature detector T C is also shown. The larger value is used to adjust the valve.
The opening of the refrigerant vapor valve V 1 may be calculated from the detected value of the heat source excess detector TH and the detected value from the evaporator external fluid temperature detector T C, and may be adjusted based on that. It should be noted that there is no problem even if the refrigerant liquid enters the refrigerant vapor guided from the high pressure side to the low pressure side.
【0023】実施例2 図6に本発明の他の例の吸収冷凍装置のフロー構成図を
示す。図6は、図1との相違点は、冷媒蒸気配管8と冷
媒蒸気弁V1 に代えて、冷媒通路6から溶液通路1へ冷
媒配管7を設けて、該配管7に冷媒弁V2 を設けた点に
ある。Embodiment 2 FIG. 6 shows a flow diagram of an absorption refrigerating apparatus of another example of the present invention. 6 is different from FIG. 1 in that instead of the refrigerant vapor pipe 8 and the refrigerant vapor valve V 1 , a refrigerant pipe 7 is provided from the refrigerant passage 6 to the solution passage 1 and the refrigerant valve V 2 is provided in the pipe 7. It is in the point provided.
【0024】そして、この装置の冷房サイクルは図1の
装置と同じであるが、冷水温度又は熱源温度が変動し、
調整の必要が生じた場合の制御方法が相違する。すなわ
ち、この実施例では、冷媒配管7に設けた冷媒弁V2 の
開度を調節することにより行う。まず、冷水温度検出器
TC 及び熱源過剰度検出器TH により、冷水温度及び熱
源温度を検出し、その検出値に基づいて、冷媒弁V2 を
調節する。The cooling cycle of this device is the same as that of the device of FIG. 1, but the chilled water temperature or the heat source temperature fluctuates,
The control method is different when adjustment is necessary. That is, in this embodiment, the operation is performed by adjusting the opening degree of the refrigerant valve V 2 provided in the refrigerant pipe 7. First, the cold water temperature detector T C and the heat source excessive Detector T H, detects the cold water temperature and heat source temperature, based on the detected value, to adjust the refrigerant valve V 2.
【0025】具体的には、冷媒弁V2 の調節は熱源過剰
度検出器TH からの弁を開方向にする検出値を、前記蒸
発器外部流体温度検出器TC からの弁を閉方向にする検
出値よりも優先させるのがよく、その例を図7にフロー
チャートで示す。図8は、図7のフローチャートをグラ
フにしたものである。More specifically, the adjustment of the refrigerant valve V 2 is performed by setting the detected value from the heat source excess detector T H in the opening direction to the valve from the evaporator external fluid temperature detector T C in the closing direction. It is preferable to give priority to the detected value of (1), and an example thereof is shown in a flowchart in FIG. FIG. 8 is a graph of the flowchart of FIG.
【0026】図9及び図10に、冷媒弁V2 の調節に関
し、熱源過剰度検出器TH から弁開度を求め、また、前
記蒸発器外部流体温度検出器TC からも弁の開度を求め
る例を示す。弁の調節には、大きい方の値を用いる。冷
媒弁V2 の開度は、熱源過剰度検出器TH の検出値、蒸
発器外部流体温度検出器TC からの検出値から演算で求
め、それをもとに調節してもよい。9 and 10, regarding the adjustment of the refrigerant valve V 2 , the valve opening degree is obtained from the heat source excess degree detector T H, and the valve opening degree is also obtained from the evaporator external fluid temperature detector T C. An example of obtaining The larger value is used to adjust the valve. The opening degree of the refrigerant valve V 2 may be calculated from the detected value of the heat source excess degree detector TH and the detected value from the evaporator external fluid temperature detector T C, and may be adjusted based on that.
【0027】実施例3 図11に本発明のもう1つの例の吸収冷凍装置のフロー
構成図を示す。図11では、図1の冷媒蒸気配管8及び
冷媒蒸気弁V1 と、図6の冷媒配管7及び冷媒弁V2 の
両方を具備している。Embodiment 3 FIG. 11 shows a flow configuration diagram of an absorption refrigeration system of another example of the present invention. In FIG. 11, both the refrigerant vapor pipe 8 and the refrigerant vapor valve V 1 of FIG. 1 and the refrigerant pipe 7 and the refrigerant valve V 2 of FIG. 6 are provided.
【0028】そして、この装置の冷房サイクルは図1の
装置と同じであるが、冷水温度又は熱源温度が変動し、
調整の必要が生じた場合の制御は次のように行う。すな
わち、冷水の温度制御は、冷媒弁V2 で行い、冷水の温
度検出器TC の検出値に基づいて冷媒弁V2 を操作する
ことによる。冷水の温度が高い場合は冷媒弁V2 は閉止
し、冷水の温度が低い場合は、冷媒弁V2 を通して冷媒
を溶液循環系に流すことにより冷凍能力を減少させる。The cooling cycle of this device is the same as that of the device of FIG. 1, but the chilled water temperature or the heat source temperature fluctuates,
The control when adjustment is necessary is performed as follows. That is, the temperature control of the cold water is performed by the refrigerant valve V 2 , and the refrigerant valve V 2 is operated based on the detection value of the temperature detector T C of the cold water. When the temperature of the cold water is high, the refrigerant valve V 2 is closed, and when the temperature of the cold water is low, the refrigerant is flowed through the refrigerant valve V 2 into the solution circulation system to reduce the refrigeration capacity.
【0029】一方、熱源の温度制御は、冷媒蒸気弁V1
で行い、熱源の過剰度検出器TH の検出値に基づいて冷
媒蒸気弁V1 を操作することによる。熱源温度が高い場
合、冷媒蒸気弁V1 を開方向にして、発生器G又は凝縮
器Cの冷媒蒸気を吸収器A又は蒸発器Eに放出して、発
生器Gの冷媒蒸気圧を低下させることにより、発生器中
の温度を下げて、熱源温度を低下させる。図12に冷媒
蒸気弁V1 の調節例を示し、図13に冷媒弁V2 の調節
例を示す。On the other hand, the temperature control of the heat source is performed by the refrigerant vapor valve V 1
Performed in, by operating the refrigerant vapor valve V 1 on the basis of the detected value of the excess of the detector T H of the heat source. When the heat source temperature is high, the refrigerant vapor valve V 1 is opened and the refrigerant vapor of the generator G or the condenser C is discharged to the absorber A or the evaporator E to reduce the refrigerant vapor pressure of the generator G. This lowers the temperature in the generator and lowers the heat source temperature. FIG. 12 shows an example of adjusting the refrigerant vapor valve V 1 , and FIG. 13 shows an example of adjusting the refrigerant valve V 2 .
【0030】[0030]
【発明の効果】本発明によれば、冷媒蒸気配管と弁及び
/又は冷媒配管と弁とを配備したことにより、冷水及び
熱源の温度制御が容易にでき、また、熱源の熱を放出で
きるので、エンジンの排出熱を放出するラジエータの役
目を兼用することができる。According to the present invention, by disposing the refrigerant vapor pipe and the valve and / or the refrigerant pipe and the valve, the temperature of the cold water and the heat source can be easily controlled, and the heat of the heat source can be released. , Can also serve as a radiator that releases the exhaust heat of the engine.
【図1】本発明の一例を示す吸収冷凍装置のフロー構成
図である。FIG. 1 is a flow configuration diagram of an absorption refrigeration apparatus showing an example of the present invention.
【図2】冷媒蒸気弁の調節を示すフローチャートであ
る。FIG. 2 is a flow chart showing adjustment of a refrigerant vapor valve.
【図3】図2のフローチャートをグラフ化した模式図で
ある。FIG. 3 is a schematic diagram in which the flowchart of FIG. 2 is graphed.
【図4】冷水温度と冷媒蒸気弁開度の関係を示すグラフ
である。FIG. 4 is a graph showing the relationship between cold water temperature and refrigerant vapor valve opening.
【図5】熱源温度と冷媒蒸気弁開度の関係を示すグラフ
である。FIG. 5 is a graph showing the relationship between heat source temperature and refrigerant vapor valve opening.
【図6】本発明の他の例を示す吸収冷凍装置のフロー構
成図である。FIG. 6 is a flow configuration diagram of an absorption refrigeration apparatus showing another example of the present invention.
【図7】冷媒弁の調節を示すフローチャートである。FIG. 7 is a flow chart showing adjustment of a refrigerant valve.
【図8】図7のフローチャートをグラフ化した模式図で
ある。FIG. 8 is a schematic diagram in which the flowchart of FIG. 7 is graphed.
【図9】冷水温度と冷媒弁開度の関係を示すグラフであ
る。FIG. 9 is a graph showing the relationship between cold water temperature and refrigerant valve opening.
【図10】熱源温度と冷媒弁開度の関係を示すグラフで
ある。FIG. 10 is a graph showing the relationship between heat source temperature and refrigerant valve opening.
【図11】本発明のもう一つの例を示す吸収冷凍装置の
フロー構成図である。FIG. 11 is a flow configuration diagram of an absorption refrigeration apparatus showing another example of the present invention.
【図12】熱源温度と冷媒蒸気弁開度の関係を示すグラ
フである。FIG. 12 is a graph showing the relationship between heat source temperature and refrigerant vapor valve opening.
【図13】冷水温度と冷媒弁開度の関係を示すグラフで
ある。FIG. 13 is a graph showing the relationship between cold water temperature and refrigerant valve opening.
G 発生器 A 吸収器 E 蒸発器 C 凝縮器 H 溶液熱交換器 V1 冷媒蒸気弁 V2 冷媒弁 TH 熱源過剰度検出器 TC 温度検出器 1〜4 溶液通路 5,6 冷媒通路 7 冷媒配管 8 冷媒蒸気配管 11,12 ポンプ 13,14 熱源通路 17 冷却塔 18 冷水通路 19,20 冷却水通路G generator A absorber E evaporator C condenser H solution heat exchanger V 1 refrigerant vapor valve V 2 refrigerant valve TH heat source excess detector T C temperature detector 1-4 solution passage 5, 6 refrigerant passage 7 refrigerant Piping 8 Refrigerant vapor piping 11, 12 Pump 13, 14 Heat source passage 17 Cooling tower 18 Cold water passage 19, 20 Cooling water passage
Claims (5)
熱交換器を主要構成機器とし、これらを溶液配管、冷媒
配管で結んでサイクルを構成する吸収冷温水装置におい
て、発生器又は凝縮器の冷媒蒸気を、吸収器又は蒸発器
に導く冷媒蒸気配管を設け、該蒸気配管には冷媒蒸気弁
を設け、また、蒸発器を通る外部流体通路に温度検出器
を設け、発生器を通る外部流体通路には熱源過剰度検出
器を設けるとともに、前記温度検出器及び熱源過剰度検
出器からの検出値を基に冷媒蒸気弁の調節を行う機構と
したことを特徴とする吸収冷温水装置。1. An absorption chilled / hot water apparatus comprising a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger as main constituent devices, and connecting them with a solution pipe and a refrigerant pipe to form a cycle. A refrigerant vapor pipe for guiding the refrigerant vapor of the condenser to the absorber or the evaporator is provided, a refrigerant vapor valve is provided for the vapor pipe, and a temperature detector is provided for an external fluid passage passing through the evaporator. Absorbed cold / hot water characterized in that a mechanism for adjusting the refrigerant vapor valve based on the detection values from the temperature detector and the heat source excess degree detector is provided along with a heat source excess degree detector provided in the external fluid passage. apparatus.
熱交換器を主要構成機器とし、これらを溶液配管、冷媒
配管で結んでサイクルを構成する吸収冷温水装置におい
て、凝縮器、蒸発器の冷媒系統から、吸収器、溶液熱交
換器、発生器の溶液循環系に冷媒を導く冷媒配管を設
け、該冷媒配管には冷媒弁を設け、また、蒸発器を通る
外部流体通路に温度検出器を設け、発生器を通る外部流
体通路には熱源過剰度検出器を設けるとともに、前記温
度検出器及び熱源過剰度検出器からの検出値を基に冷媒
弁の調節を行う機構としたことを特徴とする吸収冷凍装
置。2. An absorption cold / hot water apparatus in which a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger are main constituent devices, and these are connected by a solution pipe and a refrigerant pipe to form a cycle. A refrigerant pipe for guiding the refrigerant from the refrigerant system of the evaporator to the solution circulation system of the absorber, the solution heat exchanger, and the generator is provided with a refrigerant valve in the refrigerant pipe, and an external fluid passage passing through the evaporator is provided. A temperature detector is provided, a heat source excess degree detector is provided in the external fluid passage passing through the generator, and the refrigerant valve is adjusted based on the detection values from the temperature detector and the heat source excess degree detector. An absorption refrigeration system characterized by the above.
検出器からの弁を開方向にする検出値を、温度検出器か
らの弁を閉方向にする検出値よりも優先させる機構とし
たことを特徴とする請求項1又は2記載の吸収冷温水装
置。3. The mechanism for adjusting the valve includes a mechanism for prioritizing a detection value from the heat source excess degree detector in the opening direction over a detection value from the temperature detector in the closing direction. The absorption cold water heater according to claim 1 or 2, characterized in that.
熱交換器を主要構成機器とし、これらを溶液配管、冷媒
配管で結んでサイクルを構成する吸収冷温水装置におい
て、発生器又は凝縮器の冷媒蒸気を、吸収器又は蒸発器
に導く冷媒蒸気配管を設け、該蒸気配管には冷媒蒸気弁
を設け、また、凝縮器、蒸発器の冷媒系統から、吸収
器、溶液熱交換器、発生器の溶液循環系に冷媒を導く冷
媒配管を設け、該冷媒配管には冷媒弁を設け、更に、蒸
発器を通る外部流体通路に温度検出器を設け、発生器を
通る外部流体通路には熱源過剰度検出器を設けるととも
に、前記温度検出器からの検出値を基に前記冷媒弁の調
節を行い、前記熱源過剰度検出器からの検出値を基に冷
媒蒸気弁の調節を行う機構としたことを特徴とする吸収
冷温水装置。4. An absorption chilled / hot water apparatus comprising a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger as main constituent devices, and connecting them with a solution pipe and a refrigerant pipe to form a cycle, A refrigerant vapor pipe for guiding the refrigerant vapor of the condenser to the absorber or the evaporator is provided, a refrigerant vapor valve is provided for the vapor pipe, and the absorber and the solution heat exchanger are connected from the refrigerant system of the condenser and the evaporator. , A refrigerant pipe for guiding a refrigerant to the solution circulation system of the generator is provided, a refrigerant valve is provided in the refrigerant pipe, a temperature detector is provided in an external fluid passage passing through the evaporator, and an external fluid passage passing through the generator is provided. Is a mechanism for providing a heat source excess degree detector, adjusting the refrigerant valve based on the detection value from the temperature detector, and adjusting the refrigerant vapor valve based on the detection value from the heat source excess degree detector. An absorption cold / hot water device characterized in that
場合は熱源温度計であり、熱源が蒸気の場合は、熱源温
度計又は熱源蒸気圧計であることを特徴とする請求項
1、2、3又は4記載の吸収冷温水装置。5. The heat source excess detector is a heat source thermometer when the heat source is hot water, and is a heat source thermometer or a heat source steam pressure gauge when the heat source is steam. The absorption cold water heater according to 2, 3 or 4.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2411960A JPH0758146B2 (en) | 1990-12-20 | 1990-12-20 | Absorption cold / hot water device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2411960A JPH0758146B2 (en) | 1990-12-20 | 1990-12-20 | Absorption cold / hot water device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04217756A JPH04217756A (en) | 1992-08-07 |
| JPH0758146B2 true JPH0758146B2 (en) | 1995-06-21 |
Family
ID=18520867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2411960A Expired - Fee Related JPH0758146B2 (en) | 1990-12-20 | 1990-12-20 | Absorption cold / hot water device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0758146B2 (en) |
-
1990
- 1990-12-20 JP JP2411960A patent/JPH0758146B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04217756A (en) | 1992-08-07 |
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