JP3383898B2 - Absorption type cold heat generator - Google Patents

Absorption type cold heat generator

Info

Publication number
JP3383898B2
JP3383898B2 JP02360297A JP2360297A JP3383898B2 JP 3383898 B2 JP3383898 B2 JP 3383898B2 JP 02360297 A JP02360297 A JP 02360297A JP 2360297 A JP2360297 A JP 2360297A JP 3383898 B2 JP3383898 B2 JP 3383898B2
Authority
JP
Japan
Prior art keywords
cooling
refrigerant
water
abnormal
circulation pump
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
Application number
JP02360297A
Other languages
Japanese (ja)
Other versions
JPH10220903A (en
Inventor
哲也 山田
雅巳 仁藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yazaki Corp
Original Assignee
Yazaki Corp
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 Yazaki Corp filed Critical Yazaki Corp
Priority to JP02360297A priority Critical patent/JP3383898B2/en
Publication of JPH10220903A publication Critical patent/JPH10220903A/en
Application granted granted Critical
Publication of JP3383898B2 publication Critical patent/JP3383898B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、吸収冷温水機に係
り、特に相変化する二次冷媒を用いた吸収式冷熱発生装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller-heater, and more particularly to an absorption-type cold heat generator using a secondary refrigerant that changes phase.

【0002】[0002]

【従来の技術】従来、吸収式冷熱発生装置として図2に
示す吸収冷温水機を用いた空調装置が知られている。図
示の装置は、冷熱を発生する吸収冷温水機100と、こ
の吸収冷温水機100に冷却水管40,41で接続され
冷却水を冷却するクーリングタワー(冷却塔水槽)42
と、吸収冷温水機100に冷温水管43,44で接続さ
れ空調対象空間に配置されて空間の空気との熱交換を行
う図示されていない空調用の室内機と、冷却水管41に
介装され冷却水をクーリングタワー42から吸収冷温水
機100に循環させる冷却水循環ポンプ14と、冷温水
管43に介装され冷温水管43,44に充填された二次
冷媒を吸収冷温水機100と空調用の室内機との間で循
環させる冷温水循環ポンプ15とを含んで構成されてい
る。
2. Description of the Related Art Conventionally, an air conditioner using an absorption chiller-heater shown in FIG. 2 is known as an absorption type cold heat generator. The illustrated apparatus includes an absorption chiller-heater 100 that generates cold heat, and a cooling tower (cooling tower water tank) 42 that is connected to the absorption chiller-heater 100 by cooling water pipes 40 and 41 to cool the cooling water.
And an unillustrated air conditioning indoor unit that is connected to the absorption chiller / heater 100 by cold / hot water pipes 43 and 44 and is arranged in the air-conditioned space to exchange heat with the air in the space, and is installed in the cooling water pipe 41. A cooling water circulation pump 14 that circulates the cooling water from the cooling tower 42 to the absorption chiller-heater 100, and an absorption chiller-heater 100 and an air-conditioning room that absorbs the secondary refrigerant that is interposed in the cold-hot water pipe 43 and filled in the cold-hot water pipes 43 and 44. It is configured to include a cold / hot water circulation pump 15 that circulates between the machine and the machine.

【0003】前記室内機に対して、吸収冷温水機100
は、通常、室外機と呼ばれ、燃料を燃焼させその熱で希
溶液を加熱する高温再生器1と、この高温再生器1で加
熱された希溶液から冷媒蒸気と中間濃溶液を分離する分
離器2と、分離された冷媒蒸気を熱源として前記中間濃
溶液を加熱してさらに冷媒蒸気を発生させる低温再生器
3と、低温再生器3を通過した冷媒蒸気及び低温再生器
3で発生した冷媒蒸気を冷却して凝縮液化させ液冷媒を
生成する凝縮器4と、凝縮器4で生成された液冷媒を内
装した冷媒分配器6Bから同じく内装した蒸発コイル上
に滴下蒸発させ蒸発コイル中の二次冷媒を冷却する蒸発
器6と、蒸発器6で蒸発した冷媒蒸気を濃溶液に吸収さ
せ希溶液を生成する吸収器5と、希溶液を加圧し低温溶
液熱交換器8及び高温溶液熱交換器7の被加熱流体側を
経て高温再生器1に送りこむ溶液循環ポンプ9と、分離
器2の底部と蒸発器6の底部を冷暖切換弁10を介して
連通する管路10Aと、低温溶液熱交換器8の加熱流体
出側を吸収器5の上部に接続する濃溶液管8Aと、濃溶
液管8Aと吸収器5の下部を溶液バイパス弁13を介し
て接続する管路13Aと、濃溶液管8Aと蒸発器5に内
装された冷媒分配器を凍結防止弁12を介して連通する
管路12Aと、冷媒分配器に装着され冷媒分配器6B内
の冷媒の温度を検知する蒸発器温度センサ17と、凝縮
器4から冷媒分配器6Bに液冷媒を導く管路に並列に接
続され水冷媒比例弁11を介装する管路11Aとを含ん
で構成されている。
In contrast to the indoor unit, the absorption chiller / heater 100
Is usually called an outdoor unit, and is a high temperature regenerator 1 that burns fuel and heats the dilute solution with the heat, and a separation that separates the refrigerant vapor and the intermediate concentrated solution from the dilute solution heated by the high temperature regenerator 1. 2, a low-temperature regenerator 3 that heats the intermediate concentrated solution using the separated refrigerant vapor as a heat source to further generate refrigerant vapor, a refrigerant vapor that has passed through the low-temperature regenerator 3 and a refrigerant generated in the low-temperature regenerator 3. A condenser 4 that cools and condenses and liquefies the vapor to produce a liquid refrigerant, and a liquid refrigerant produced in the condenser 4 is dropped and evaporated from the refrigerant distributor 6B in which it is installed onto an evaporation coil that is also installed, and An evaporator 6 for cooling the next refrigerant, an absorber 5 for absorbing the refrigerant vapor evaporated in the evaporator 6 into a concentrated solution to produce a dilute solution, a low temperature solution heat exchanger 8 and a high temperature solution heat exchange by pressurizing the dilute solution. High-temperature regenerator 1 through the heated fluid side of vessel 7. A solution circulation pump 9 for feeding in, a pipe 10A for communicating the bottom of the separator 2 and the bottom of the evaporator 6 via a cooling / heating switching valve 10, and a heating fluid outlet side of the low temperature solution heat exchanger 8 at an upper part of the absorber 5. A concentrated solution pipe 8A, a conduit 13A connecting the concentrated solution pipe 8A and the lower part of the absorber 5 via the solution bypass valve 13, and a concentrated solution pipe 8A and a refrigerant distributor installed in the evaporator 5. A pipeline 12A communicating through the antifreezing valve 12, an evaporator temperature sensor 17 mounted on the refrigerant distributor to detect the temperature of the refrigerant in the refrigerant distributor 6B, and a liquid refrigerant from the condenser 4 to the refrigerant distributor 6B. And a pipe line 11A that is connected in parallel to the pipe line that guides the water refrigerant and that has the water-refrigerant proportional valve 11 interposed therebetween.

【0004】また、分離器2で分離された中間濃溶液
は、高温溶液熱交換器7の加熱流体側を経て低温再生器
3に導かれ、低温再生器3で冷媒を蒸発させて濃溶液と
なったのち、低温溶液熱交換器8の加熱流体側を経て濃
溶液管8Aに導かれるように管路が構成されている。吸
収器5及び凝縮器4にはそれぞれ冷却水コイルが内装さ
れ、吸収器5の冷却水コイルの出口は凝縮器4の冷却水
コイルの入り口に接続されていて、吸収器5の冷却水コ
イルの入り口は冷却水管41に、凝縮器4の冷却水コイ
ルの出口は冷却水管40に、それぞれ接続されている。
冷温水管43は蒸発器6の蒸発コイルの入り側に、冷温
水管44は蒸発器6の蒸発コイルの出側に、それぞれ接
続され、冷温水管44の蒸発コイル出口近傍には二次冷
媒の温度を検知する冷水出口温度センサ16が装着され
ている。
The intermediate concentrated solution separated in the separator 2 is introduced into the low temperature regenerator 3 via the heating fluid side of the high temperature solution heat exchanger 7, and the refrigerant is evaporated in the low temperature regenerator 3 to form a concentrated solution. After that, the pipe line is configured so as to be guided to the concentrated solution pipe 8A via the heating fluid side of the low temperature solution heat exchanger 8. A cooling water coil is installed in each of the absorber 5 and the condenser 4, the outlet of the cooling water coil of the absorber 5 is connected to the inlet of the cooling water coil of the condenser 4, and the cooling water coil of the absorber 5 is The inlet is connected to the cooling water pipe 41, and the outlet of the cooling water coil of the condenser 4 is connected to the cooling water pipe 40.
The cold / hot water pipe 43 is connected to the inlet side of the evaporator coil of the evaporator 6, and the cold / hot water pipe 44 is connected to the outlet side of the evaporator coil of the evaporator 6, respectively, and the temperature of the secondary refrigerant is provided near the outlet of the evaporator coil of the cold / hot water pipe 44. A cold water outlet temperature sensor 16 for detecting is mounted.

【0005】近年、二次冷媒に相変化を行わせることに
より、単位流量あたりの熱搬送量を増加させるものが考
案されている。図3はそのような構成の例を示すもの
で、図2に示す構成のうち、冷温水管43,44に代え
て冷媒液管50、冷媒蒸気管51が蒸発コイルの下端、
上端にそれぞれ接続されている。冷媒回路を形成する冷
媒液管50,冷媒蒸気管51の他端は、蒸発コイルより
も下方に配置された室内機52,53の数だけ分岐して
おり、冷媒液管50の分岐端は、室内機にそれぞれ内装
された熱交換器の下側入り口に膨張弁54,55を介し
て接続され、冷媒蒸気管51の分岐端は、熱交換器の上
側入り口にそれぞれ接続されている。冷媒液管50の蒸
発コイルとの接続部近傍には、二次冷媒の温度を検出し
て電気信号としてコントローラー(制御手段)59に出
力する冷媒液温度センサ21が装着されている。
In recent years, there has been devised a method of increasing the amount of heat transfer per unit flow rate by causing a secondary refrigerant to undergo a phase change. FIG. 3 shows an example of such a configuration. In the configuration shown in FIG. 2, instead of the cold / hot water pipes 43 and 44, a refrigerant liquid pipe 50 and a refrigerant vapor pipe 51 are the lower end of the evaporation coil.
Each is connected to the top. The other ends of the refrigerant liquid pipe 50 and the refrigerant vapor pipe 51 forming the refrigerant circuit are branched by the number of the indoor units 52 and 53 arranged below the evaporation coil, and the branched end of the refrigerant liquid pipe 50 is It is connected to the lower inlets of the heat exchangers respectively installed in the indoor units via expansion valves 54 and 55, and the branch ends of the refrigerant vapor pipes 51 are respectively connected to the upper inlets of the heat exchangers. A refrigerant liquid temperature sensor 21 that detects the temperature of the secondary refrigerant and outputs it as an electric signal to a controller (control means) 59 is mounted near the connection portion of the refrigerant liquid pipe 50 with the evaporation coil.

【0006】冷媒液管50は、途中に室内機52,53
よりも低い位置に配置された部分があり、そこに冷媒液
を加圧して蒸発コイルに送りこむ冷媒ポンプ57が装着
されている。冷媒循環ポンプ57の吐出側には、逆止弁
58が設けられ、この逆止弁58の出側と冷媒循環ポン
プ57の吸い込み側は、冷暖切換弁56を介して接続さ
れている。相変化する二次冷媒(以下単に冷媒ともい
う)として、例えばHFC−134aが冷媒液管に充填
されている。他の構成は図2の説明と同じであり説明を
省略する。
The refrigerant liquid pipe 50 is connected to the indoor units 52 and 53 on the way.
There is a portion arranged at a lower position than that, and a refrigerant pump 57 that pressurizes the refrigerant liquid and sends it to the evaporation coil is attached thereto. A check valve 58 is provided on the discharge side of the refrigerant circulation pump 57, and the outlet side of the check valve 58 and the suction side of the refrigerant circulation pump 57 are connected via a cooling / heating switching valve 56. For example, HFC-134a is filled in the refrigerant liquid pipe as a secondary refrigerant (hereinafter also simply referred to as a refrigerant) that undergoes a phase change. Other configurations are the same as those described with reference to FIG.

【0007】図3に示す空調装置の冷房時の動作は次の
通りである。冷房時には、冷暖切換弁56は開かれてい
る。冷媒蒸気(HFC−134a、R404A等)は、
蒸発器6の蒸発コイルで冷却凝縮されて冷媒液となり、
重力により、冷媒液管50を下方に流れ、膨張弁54,
55を経て各室内機52,53の熱交換器に流入する。
熱交換器に流入した冷媒液は、空調対象空間の空気の熱
を奪って蒸発し、冷媒蒸気となって冷媒蒸気管51を経
て上昇し蒸発器6の蒸発コイルに流入する。室外機(吸
収冷温水機)100は冷房モードで運転されているか
ら、蒸発器6の蒸発コイルは、その表面に滴下される水
冷媒の蒸発により冷却され、蒸発コイルに流入してきた
冷媒蒸気(HFC−134a、R404A等)は、凝縮
液化する。この凝縮液化により、蒸発コイル内部の圧力
が低下し、室内機の熱交換器で蒸発した冷媒蒸気は蒸発
器に吸引される。蒸発コイル内部で凝縮液化した冷媒液
は重力で室内機に流入するから、冷房時の冷媒(HFC
−134a、R404A等)は、自然循環し、ポンプに
よる冷媒の駆動を行う必要がない。
The operation of the air conditioner shown in FIG. 3 during cooling is as follows. The cooling / heating switching valve 56 is opened during cooling. Refrigerant vapor (HFC-134a, R404A, etc.)
It is cooled and condensed by the evaporation coil of the evaporator 6 to become a refrigerant liquid,
Due to gravity, the refrigerant liquid pipe 50 flows downward, and the expansion valve 54,
After passing through 55, it flows into the heat exchanger of each indoor unit 52, 53.
The refrigerant liquid that has flowed into the heat exchanger deprives the heat of the air in the air-conditioned space to evaporate, becomes refrigerant vapor, rises through the refrigerant vapor pipe 51, and flows into the evaporation coil of the evaporator 6. Since the outdoor unit (absorption cooling / heating machine) 100 is operated in the cooling mode, the evaporation coil of the evaporator 6 is cooled by the evaporation of the water refrigerant dropped on the surface thereof, and the refrigerant vapor (flowing into the evaporation coil ( HFC-134a, R404A, etc.) is condensed and liquefied. Due to this condensation and liquefaction, the pressure inside the evaporation coil is lowered, and the refrigerant vapor evaporated in the heat exchanger of the indoor unit is sucked into the evaporator. Since the refrigerant liquid condensed and liquefied inside the evaporation coil flows into the indoor unit by gravity, the refrigerant (HFC
-134a, R404A, etc.) naturally circulate, and it is not necessary to drive the refrigerant by a pump.

【0008】冷房運転が開始されると、前記のように、
蒸発コイル内部の圧力が低下し、冷媒蒸気管内の飽和冷
媒蒸気が圧力差により蒸発コイル内に流入する。蒸発コ
イル内で凝縮して生成された冷媒液は、冷媒液管50内
を自重で流下し、冷媒液のヘッド(液柱)が上昇してく
る。先に述べた冷媒の自然循環が成立するためには、
(冷媒の液ヘッド−冷媒ガスヘッド)が冷媒循環経路の
全圧力損失以上であればよい。つまり、この関係を満足
する液ヘッドが形成されるまでは冷媒の自然循環は開始
されない。このことは、冷房運転開始時点で蒸発器6に
供給される熱負荷が少ないことを意味する。
When the cooling operation is started, as described above,
The pressure inside the evaporation coil decreases, and the saturated refrigerant vapor in the refrigerant vapor pipe flows into the evaporation coil due to the pressure difference. The refrigerant liquid condensed and generated in the evaporation coil flows down in the refrigerant liquid pipe 50 by its own weight, and the head (liquid column) of the refrigerant liquid rises. In order to establish the natural circulation of the refrigerant described above,
It is sufficient that (refrigerant liquid head-refrigerant gas head) is equal to or greater than the total pressure loss of the refrigerant circulation path. That is, the natural circulation of the refrigerant is not started until the liquid head satisfying this relationship is formed. This means that the heat load supplied to the evaporator 6 at the start of the cooling operation is small.

【0009】上記構成の装置において、一般に遠方(二
次冷媒側)で冷暖の運転モードを切替える場合は、溶液
用の冷暖切換弁10が自動的に開閉する仕様になってお
り、冷房時は閉、暖房時は開とされる。また冷房運転立
上時は、冷却塔水槽42の水位を検出する制御機器(レ
ベルスイッチ及び給水圧力スイッチ等)61,62を用
い、水位があり冷却水循環ポンプ14が空転しないこと
を確認して立上り運転を開始する。水位が渇水レベルに
ある場合もしくは断水等により給水圧力が使用範囲以下
に低下した場合は、吸収冷温水機100の運転を即時停
止させている。しかしながら自然循環システムにおいて
は、図4に示す従来のような冷却水制御で、水位信号の
異常で瞬時に冷却水循環ポンプ14を停止させると、制
御機器61,62の誤動作等の場合であっても、システ
ム上、室内機側の膨張弁(電子膨張弁)54,55は一
旦全閉すると、吸収式冷熱発生装置が再起動する時にあ
る一定時間後に膨張弁54,55が作動するため、一定
時間は冷房サイクルを維持できない問題があった。
In the apparatus having the above-mentioned structure, generally, when the cooling / heating operation mode is switched at a distant place (on the side of the secondary refrigerant), the cooling / heating switching valve 10 for the solution is automatically opened and closed, and is closed during cooling. , It is opened during heating. When the cooling operation is started up, the control equipment (level switch and feed water pressure switch, etc.) 61 and 62 for detecting the water level in the cooling tower water tank 42 is used to confirm that the cooling water circulation pump 14 does not run idle due to the water level. Start driving. When the water level is at a drought level or when the water supply pressure falls below the usable range due to water interruption or the like, the operation of the absorption chiller-heater 100 is immediately stopped. However, in the natural circulation system, even if the cooling water circulation pump 14 is instantaneously stopped due to an abnormality in the water level signal in the conventional cooling water control shown in FIG. 4, even if the control devices 61 and 62 malfunction. In the system, once the expansion valves (electronic expansion valves) 54, 55 on the indoor unit side are fully closed, the expansion valves 54, 55 are activated after a certain period of time when the absorption-type cold heat generator is restarted. Had a problem that could not maintain the cooling cycle.

【0010】[0010]

【発明が解決しようとする課題】従来の吸収式冷熱発生
装置にあっては、冷房運転立上り時に、冷却塔水槽の水
位が渇水レベルにある場合、もしくは断水等により給水
圧力が使用範囲以下に低下した場合は、吸収冷温水機の
運転を即時停止させている。しかしながら制御機器の誤
動作等による水位異常により吸収冷温水機の運転が停止
された場合、コントローラーにより室内機側の膨張弁が
全閉に制御されるが、膨張弁が一旦全閉すると、吸収式
冷熱発生装置が再起動する時にある一定時間後に作動す
るため、その間に冷房サイクルが維持できない問題があ
った。特に加圧ポンプで冷却塔水槽へ補給水を送給する
場合は、冷却塔水槽内の圧力変動幅が大きく、瞬時に圧
力低下して吸収冷温水機の運転停止になり易く、冷房サ
イクルが維持できない時間が発生し易い問題があった。
In the conventional absorption type cold heat generator, when the cooling operation is started, the water level in the cooling tower water tank is at a drought level, or the water supply pressure falls below the usable range due to water interruption or the like. If so, the operation of the absorption chiller-heater is immediately stopped. However, when the operation of the absorption chiller / heater is stopped due to an abnormal water level due to malfunction of the control equipment, the controller controls the expansion valve on the indoor unit side to be fully closed, but once the expansion valve is fully closed, the absorption chiller There is a problem that the cooling cycle cannot be maintained because the generator operates after a certain period of time when it is restarted. Especially when supplying makeup water to the cooling tower water tank with a pressurizing pump, the fluctuation range of the pressure in the cooling tower water tank is large, the pressure drops instantly and it is easy to stop the operation of the absorption chiller-heater, and the cooling cycle is maintained. There was a problem that it was easy to occur when it was impossible.

【0011】本発明の課題は、冷却塔水槽の水位が異常
でも異常信号が設定時間連続しなければ誤作動と判断す
る吸収式冷熱発生装置を提供することにある。
An object of the present invention is to provide an absorption-type cold heat generating device that determines malfunction even if the water level in the cooling tower water tank is abnormal unless an abnormal signal continues for a set time.

【0012】[0012]

【課題を解決するための手段】前記の課題を達成するた
め、本発明に係る吸収式冷熱発生装置は、再生器、凝縮
器、蒸発器及び吸収器を含む機器を接続した吸収式冷温
水機と、貯水した冷却水を冷却水循環ポンプで吸収器を
経て凝縮器へ循環する冷却塔水槽と、蒸発器と少なくと
も一つの室内機との間相変化する冷媒循環する冷媒
液管と冷媒蒸気管を含んでなる冷媒回路と、冷却塔水槽
の水位異常の際に冷房運転を抑止する制御手段とを備え
た吸収式冷熱発生装置において、前記冷媒液管は室内機
に内装された熱交換器に膨張弁を介して接続され、制御
手段は、水位異常の場合前記冷却水循環ポンプの運転を
抑止し、前記冷却水循環ポンプの運転抑止保持が設定時
間以上連続した際に、装置の運転を停止させる冷房切替
異常信号を出力するものである構成とする。
In order to achieve the above-mentioned object, an absorption type cold heat generator according to the present invention is an absorption type cold and hot water machine in which devices including a regenerator, a condenser, an evaporator and an absorber are connected. When, water was cooling water and cooling tower water bath that circulates to the condenser through the absorber in the cooling water circulation pump, an evaporator and at least one refrigerant phase change to a refrigerant circulates between the indoor unit
In an absorption type cold heat generating device comprising a refrigerant circuit including a liquid pipe and a refrigerant vapor pipe, and a control means for suppressing a cooling operation when the water level of a cooling tower water tank is abnormal, the refrigerant liquid pipe is an indoor unit.
Is connected to a heat exchanger installed in the engine via an expansion valve, and the control means controls the operation of the cooling water circulation pump when the water level is abnormal.
When the operation of the cooling water circulation pump is suppressed and the operation of the cooling water circulation pump is continued for a set time or longer, a cooling switching abnormality signal for stopping the operation of the device is output .

【0013】そして制御手段は、冷却塔水槽の水位信号
異常に基づき冷却水循環ポンプを運転抑止するとともに
冷却塔水槽の水位が異常のとき、それに伴なって異常と
される冷房準備完了信号を異常とし、該冷房準備完了信
号の異常が設定時間以上連続して冷房準備開始設定時間
が経過した際に、冷房切替異常信号を出力し、前記冷房
準備完了信号の異常の連続が設定時間以内の際は、通常
制御に移行させるものである構成でもよい。
The control means inhibits the operation of the cooling water circulation pump based on the water level signal abnormality of the cooling tower water tank, and
When the water level in the cooling tower water tank is abnormal,
When the cooling preparation completion signal is abnormal, and the abnormality of the cooling preparation completion signal exceeds the set time continuously for the cooling preparation start set time, the cooling switching abnormality signal is output and the abnormality of the cooling preparation completion signal is output. When the continuation of is within the set time, the control may be shifted to the normal control.

【0014】本発明によれば、冷却塔水槽の水位異常に
より冷房準備完了信号が異常になっても、設定時間以上
連続しなければ、冷房切替異常信号が出力されないた
め、制御機器の誤作動による瞬時運転停止が回避され
る。
According to the present invention, even if the cooling preparation completion signal becomes abnormal due to the water level abnormality in the cooling tower water tank, the cooling switching abnormality signal is not output unless it continues for the set time or more, so that the control device malfunctions. Momentary outages are avoided.

【0015】[0015]

【発明の実施の形態】本発明の実施の形態を図1及び図
3を参照しながら説明する。図1及び図3に示すよう
に、高温再生器1、分離器2、低温再生器3、凝縮器
4、蒸発器6及び吸収器5を含む機器を接続した吸収式
冷温水機100と、貯水した冷却水を冷却水循環ポンプ
14で吸収器5を経て凝縮器4へ循環する冷却塔水槽
(クーリングタワー)42と、蒸発器6と一つ以上の室
内機52,53との間相変化する冷媒循環する冷媒
液管50と冷媒蒸気管51を含んでなる冷媒回路と、冷
却塔水槽42の水位異常の際に冷房運転を抑止する制御
手段(コントローラー)59とを備えた吸収式冷熱発生
装置であって、制御手段59は、冷却塔水槽42の水位
異常により冷却水循環ポンプ14の運転を抑止し、冷却
水循環ポンプ14の運転抑止保持が設定時間以上連続し
た際に、装置の運転を停止させ膨張弁を全閉させる
房切替異常信号を出力するものである構成とする。すな
わち制御手段59は、制御機器61,62で検知した冷
却塔水槽42の水位信号を入力し、水位信号の異常(O
FF)に基づき冷却水循環ポンプ14を運転抑止(OF
F)するとともに、冷房準備(CIR)完了信号を異常
(OFF)とする。そして、CIR完了信号の異常が設
定時間以上連続してCIR開始設定時間が経過した際
に、冷房切替異常信号を出力し、CIR完了信号の異常
の連続が設定時間以内の際は、つまりCIR完了信号の
異常が設定時間連続しなければ通常制御フローに移行さ
せるものである。冷房準備(CIR)完了信号は、冷却
塔水槽42の水位が異常(OFF)のとき、それに伴な
って異常(OFF)とされる信号で、この信号が設定時
間以上連続して異常とされている場合に、冷房切替異常
信号が出力される。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described with reference to FIGS. As shown in FIGS. 1 and 3, an absorption chiller-heater 100 to which equipment including a high temperature regenerator 1, a separator 2, a low temperature regenerator 3, a condenser 4, an evaporator 6 and an absorber 5 is connected, and water storage A cooling tower water tank (cooling tower) 42 in which the cooling water is circulated by the cooling water circulation pump 14 to the condenser 4 via the absorber 5, and a refrigerant that changes phases between the evaporator 6 and one or more indoor units 52, 53. refrigerant but circulating
An absorption type cold heat generating device comprising: a refrigerant circuit including a liquid pipe 50 and a refrigerant vapor pipe 51; and a control means (controller) 59 for suppressing a cooling operation when the water level in the cooling tower water tank 42 is abnormal, control means 59, the water level abnormally suppressed more operation of the cooling water circulation pump 14 of the cooling tower water tank 42, when the operation inhibiting retention of the cooling water circulation pump 14 are continuously set time or more, stops the operation of the apparatus, the expansion valve Is configured to output a cooling switching abnormality signal that completely closes . That is, the control means 59 inputs the water level signal of the cooling tower water tank 42 detected by the control devices 61 and 62, and the water level signal is abnormal (O
FF) based on the operation of the cooling water circulation pump 14 (OF)
At the same time as F), the cooling preparation (CIR) completion signal is set to abnormal (OFF) . When the abnormality of the CIR completion signal continues for the set time or more and the CIR start set time elapses, the cooling switching abnormality signal is output. If the signal abnormality does not continue for the set time, the normal control flow is entered. Cooling ready (CIR) completion signal is cooling
When the water level in the tower water tank 42 is abnormal (OFF),
It is a signal that is abnormal (OFF) and this signal is set
Abnormality of air-conditioning switching when it is abnormal for more than 1 consecutive period
The signal is output.

【0016】以上のように、冷却塔水槽の冷却水水位を
検知する制御手段において、タイマー、及び判定器等を
設け、水位信号の異常(OFF)で瞬時に装置を全停止
とせず、タイマー等に設定したある時間信号異常をキー
プした場合に、冷房切替異常信号を出力して装置を停止
することにより、制御機器の誤作動による装置停止で膨
張弁が全閉するのを防止しようとするものである。特に
加圧ポンプで冷却塔水槽へ補給水を送る場合は、圧力変
動巾が大きく、瞬時に圧力低下し運転停止になり易い。
冷却水水位が異常で冷房準備(CIR)完了信号が異常
になっても、経過時間を設定時間と比較し、冷房準備
(CIR)完了信号の異常(OFF)を設定時間以上連
続して保持しなければ、水位を検知する制御機器の誤作
動と判定器等により判断し、通常制御フローへ移行させ
るものである。
As described above, the control means for detecting the cooling water level in the cooling tower water tank is provided with a timer, a judging device, etc., and the apparatus is not stopped instantaneously when the water level signal is abnormal (OFF). Rise when keeping a certain time signal abnormality set, by stopping <br/> the device outputs a cooling switch abnormality signal, the apparatus stops due to malfunction of the control device to the
It is intended to prevent the tension valve from fully closing . Especially when sending makeup water to the cooling tower water tank with a pressurizing pump, the pressure fluctuation range is large, and the pressure is instantly lowered, and the operation is likely to be stopped.
Even if the cooling water level is abnormal and the cooling preparation (CIR) completion signal becomes abnormal, the elapsed time is compared with the set time and the cooling preparation (CIR) completion signal error (OFF) is maintained continuously for the set time or longer. If it is not, the control device for detecting the water level is judged to be malfunctioning by a judging device or the like, and the process is shifted to the normal control flow.

【0017】本発明によれば、誤作動が防止できるとと
もに、システムでの冷凍能力ダウン時間が短縮され、室
外機の冷却水水位(OFF)による装置の瞬時運転停止
を防止できる。
According to the present invention, malfunctions can be prevented, the refrigerating capacity down time in the system can be shortened, and instantaneous stoppage of operation of the device due to the cooling water level (OFF) of the outdoor unit can be prevented.

【0018】[0018]

【発明の効果】本発明によれば、冷却塔水槽の水位異常
により冷房準備完了信号の異常が設定時間以上連続した
際に、冷房切替異常信号が出力されるため、制御機器の
誤作動による瞬時運転停止が回避されるとともに、冷凍
能力のダウン時間が短縮される。
According to the present invention, when an abnormality in the cooling preparation completion signal continues for a set time or longer due to an abnormality in the water level of the cooling tower water tank, a cooling switching abnormality signal is output. The operation stop is avoided and the refrigerating capacity down time is shortened.

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

【図1】本発明の実施の形態を示す制御フローの図であ
る。
FIG. 1 is a control flow diagram showing an embodiment of the present invention.

【図2】従来技術の室外機を示す図である。FIG. 2 is a diagram showing a conventional outdoor unit.

【図3】近年の装置を示す図である。FIG. 3 is a diagram showing a recent device.

【図4】従来技術の制御フローを示す図である。FIG. 4 is a diagram showing a control flow of a conventional technique.

【符号の説明】[Explanation of symbols]

1 高温再生器 2 分離器 3 低温再生器 4 凝縮器 5 吸収器 6 蒸発器 7 高温溶液熱交換器 8 低温溶液熱交換器 9 溶液循環ポンプ 14 冷却水循環ポンプ 52,53 室内機 59 コントローラー 100 吸収冷温水機 1 High temperature regenerator 2 separator 3 low temperature regenerator 4 condenser 5 absorber 6 evaporator 7 High temperature solution heat exchanger 8 Low temperature solution heat exchanger 9 Solution circulation pump 14 Cooling water circulation pump 52,53 Indoor unit 59 controller 100 absorption cold water heater

フロントページの続き (56)参考文献 特開 平8−121894(JP,A) 特開 平7−229658(JP,A) 特開 平5−302770(JP,A) 特開 平8−247571(JP,A) 特開 平3−134441(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 15/00 306 Continuation of front page (56) Reference JP-A-8-121894 (JP, A) JP-A-7-229658 (JP, A) JP-A-5-302770 (JP, A) JP-A-8-247571 (JP , A) JP-A-3-134441 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) F25B 15/00 306

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 再生器、凝縮器、蒸発器及び吸収器を含
む機器を接続した吸収式冷温水機と、貯水した冷却水を
冷却水循環ポンプで前記吸収器を経て前記凝縮器へ循環
する冷却塔水槽と、前記蒸発器と少なくとも一つの室内
機との間に相変化する冷媒循環する冷媒液管と冷媒蒸
気管を含んでなる冷媒回路と、前記冷却塔水槽の水位異
常の際に冷房運転を抑止する制御手段とを備えた吸収式
冷熱発生装置において、前記冷媒液管は室内機に内装さ
れた熱交換器に膨張弁を介して接続され、前記制御手段
は、前記水位異常の場合前記冷却水循環ポンプの運転を
抑止し、前記冷却水循環ポンプの運転抑止保持が設定時
間以上連続した際に、装置の運転を停止させる冷房切替
異常信号を出力するものであることを特徴とする吸収式
冷熱発生装置。
1. An absorption chiller-heater connected to equipment including a regenerator, a condenser, an evaporator, and an absorber, and cooling in which stored cooling water is circulated to the condenser via a absorber by a cooling water circulation pump. and towers water tank, the evaporator and at least a refrigerant liquid pipe of one phase change refrigerant between the indoor unit circulates the refrigerant vapor
In an absorption type cold heat generating device provided with a refrigerant circuit including a trachea, and a control means for suppressing cooling operation when the water level of the cooling tower water tank is abnormal, the refrigerant liquid pipe is installed in an indoor unit.
Connected to the heat exchanger via an expansion valve, and the control means operates the cooling water circulation pump when the water level is abnormal.
Arresting, the when the cooling water circulation pump operation inhibiting retention successive set time or more, absorption cold generating apparatus, characterized in that outputs a cooling switch abnormality signal for stopping the operation of the apparatus.
【請求項2】 制御手段は、冷却塔水槽の水位信号異常
に基づき冷却水循環ポンプを運転抑止するとともに冷却
塔水槽の水位が異常のとき、それに伴なって異常とされ
冷房準備完了信号を異常とし、該冷房準備完了信号の
異常が設定時間以上連続して冷房準備開始設定時間が経
過した際に、冷房切替異常信号を出力し、前記冷房準備
完了信号の異常の連続が設定時間以内の際は、通常制御
に移行させるものであることを特徴とする請求項1記載
の吸収式冷熱発生装置。
Wherein the control means is cooled while operating deter water level signal abnormally based coolant circulation pump of the cooling tower water tank
If the water level in the tower tank is abnormal, it will be
The cooling preparation completion signal is abnormal, and when the abnormality of the cooling preparation completion signal exceeds the set time continuously for the cooling preparation start set time, the cooling switching abnormality signal is output, and the abnormality of the cooling preparation completion signal is output. The absorption cold heat generator according to claim 1, wherein when the continuation is within a set time, the control is shifted to a normal control.
JP02360297A 1997-02-06 1997-02-06 Absorption type cold heat generator Expired - Fee Related JP3383898B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02360297A JP3383898B2 (en) 1997-02-06 1997-02-06 Absorption type cold heat generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02360297A JP3383898B2 (en) 1997-02-06 1997-02-06 Absorption type cold heat generator

Publications (2)

Publication Number Publication Date
JPH10220903A JPH10220903A (en) 1998-08-21
JP3383898B2 true JP3383898B2 (en) 2003-03-10

Family

ID=12115163

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02360297A Expired - Fee Related JP3383898B2 (en) 1997-02-06 1997-02-06 Absorption type cold heat generator

Country Status (1)

Country Link
JP (1) JP3383898B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011202951A (en) * 2011-06-16 2011-10-13 Sanyo Electric Co Ltd Absorption type chiller and heater

Also Published As

Publication number Publication date
JPH10220903A (en) 1998-08-21

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