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JPS6112184B2 - - Google Patents
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JPS6112184B2 - - Google Patents

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Publication number
JPS6112184B2
JPS6112184B2 JP7807881A JP7807881A JPS6112184B2 JP S6112184 B2 JPS6112184 B2 JP S6112184B2 JP 7807881 A JP7807881 A JP 7807881A JP 7807881 A JP7807881 A JP 7807881A JP S6112184 B2 JPS6112184 B2 JP S6112184B2
Authority
JP
Japan
Prior art keywords
cooled condenser
air
water
pressure
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
JP7807881A
Other languages
Japanese (ja)
Other versions
JPS57192773A (en
Inventor
Akiji Suwabe
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.)
SHINNIPPON KUCHO KK
Original Assignee
SHINNIPPON KUCHO KK
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 SHINNIPPON KUCHO KK filed Critical SHINNIPPON KUCHO KK
Priority to JP7807881A priority Critical patent/JPS57192773A/en
Publication of JPS57192773A publication Critical patent/JPS57192773A/en
Publication of JPS6112184B2 publication Critical patent/JPS6112184B2/ja
Granted legal-status Critical Current

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  • Air Conditioning Control Device (AREA)

Description

【発明の詳細な説明】 本発明は、電子計算機室用などの年間を通して
冷房負荷と再熱用の暖房負荷が同時に発生する空
気調和装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air conditioner for a computer room or the like in which a cooling load and a heating load for reheating are generated simultaneously throughout the year.

従来に、一般にこの種の空気調和装置における
再熱コイル(ヒータ)としては、電気ヒータ、蒸
気ヒータもしくは温水ヒータなどが用いられてい
る。しかし、こうした方式では外部から大量の熱
源を必要とするものであるから、その運転費はか
なり膨大なものとなる。近年、空気調和装置外部
から排熱を利用する方式も開発されてはいるが、
空気調和装置との組合せに当つて運転上、あるい
は制御などの点で複雑な点が多い。一方、たとえ
ば実公昭53−28285号公報記載のように、コンデ
ンサーから外気に放出していた冷凍機の排熱を冷
却塔と組合せた水冷コンデンサーを経て温水ヒー
タの熱源とすることも行なわれているが、冷却塔
の使用および屋外配管を使用せざるを得ないた
め、冷却水の水質に起因する管内の腐食、冬期の
外気温度の低下による冷却水の凍結、降雪による
冷却塔の機能低下、地震時における補給水の入手
困難等、保守、運転管理上のみならず、経済的に
も技術的にも困難な問題が多い。
Conventionally, an electric heater, a steam heater, a hot water heater, or the like has been generally used as a reheating coil (heater) in this type of air conditioner. However, since these systems require a large amount of external heat source, the operating costs are quite high. In recent years, methods have been developed that utilize exhaust heat from outside the air conditioner.
When combined with an air conditioner, there are many complicated points in terms of operation and control. On the other hand, as described in Japanese Utility Model Publication No. 53-28285, for example, exhaust heat from a refrigerator, which was released into the outside air from a condenser, is used as a heat source for a hot water heater through a water-cooled condenser combined with a cooling tower. However, since it is necessary to use a cooling tower and outdoor piping, there are many problems such as corrosion inside the pipes due to the quality of the cooling water, freezing of the cooling water due to the drop in outside air temperature in winter, decreased functionality of the cooling tower due to snowfall, and earthquakes. There are many problems not only in terms of maintenance and operation management, but also economically and technically, such as difficulty in obtaining make-up water at times.

そこで、本発明者は、実開昭55−130168号公報
記載のように、冷凍機からの高圧ガス冷媒を水冷
コンデンサーに通し、この水冷コンデンサーにお
いて熱せられた温水を再熱コイルの熱源とし、ま
た高圧ガス冷媒は空冷コンデンサーに導き、凝縮
した高圧液冷媒と前記水冷コンデンサーからの高
圧液冷媒と合流させた後、空気冷却器に与える方
式を創案し、冷凍機自体の排熱を有効に利用する
とともに、従来の水配管上の難点を一挙に解決し
た。
Therefore, the present inventor passed the high-pressure gas refrigerant from the refrigerator through a water-cooled condenser, and used the hot water heated in the water-cooled condenser as a heat source for the reheating coil, as described in Japanese Utility Model Application No. 55-130168. The high-pressure gas refrigerant is led to an air-cooled condenser, where the condensed high-pressure liquid refrigerant is combined with the high-pressure liquid refrigerant from the water-cooled condenser, and then fed to the air cooler, making effective use of the exhaust heat of the refrigerator itself. At the same time, the problems with conventional water piping were solved in one fell swoop.

ところが、水冷コンデンサーと空冷コンデンサ
ーの設置高さが異なることと、2つのコンデンサ
ーの凝縮圧力がそれぞれ異なることとが原因し
て、冷媒の循環が円滑に行かず、冷凍能力の極端
な低下、もしくは冷凍サイクルの停止が発生する
問題があり、このような方式は実用化が困難であ
るとされていた。
However, because the installation heights of the water-cooled condenser and the air-cooled condenser are different, and the condensing pressures of the two condensers are different, the refrigerant does not circulate smoothly, resulting in an extreme drop in refrigeration capacity or This method has been considered difficult to put into practical use due to the problem of cycle stoppage.

本発明は前記問題点を解決したもので、主たる
特徴とするところは、第1に水冷コンデンサーと
空冷コンデンサーとの設置レベル差等に基づく液
冷媒の圧力差を考慮して差圧制御弁を設けた点、
第2に水冷コンデンサーの出口冷却水温度を制御
して高精度の空気加熱を行うために空冷コンデン
サーの凝縮圧力を制御する制御装置を設けた点に
ある。
The present invention has solved the above-mentioned problems, and its main features are: firstly, a differential pressure control valve is provided in consideration of the pressure difference of the liquid refrigerant based on the difference in installation level between the water-cooled condenser and the air-cooled condenser; The point,
Second, a control device is provided to control the condensing pressure of the air-cooled condenser in order to control the temperature of the cooling water at the outlet of the water-cooled condenser and perform highly accurate air heating.

以下本発明を図面に示す具体例によつてその作
用とともに説明する。
The present invention will be explained below along with its operation using specific examples shown in the drawings.

符号1はパツケージP内に設けられた冷凍機、
2は水冷コンデンサー、3は水冷コンデンサー2
よりHm高位に配設された空冷コンデンサー、4
は空気冷却器、5は空気加熱器である。
Reference numeral 1 is a refrigerator installed in the package P;
2 is water-cooled condenser, 3 is water-cooled condenser 2
Air-cooled condenser placed higher than Hm, 4
is an air cooler, and 5 is an air heater.

冷凍機1より吐出された高圧ガス冷媒は、管路
6および逆止弁7を通り分流点8に至り、2つの
方向に分流する。一方は管路9、差圧制御弁1
0、管路11、止弁12および管路13を通り、
空冷コンデンサー3に至る。他方は管路14を通
り、並列の第1電磁弁15および第2電磁弁16
を通り水冷コンデンサー2に至る。また空冷コン
デンサー3で凝縮した高圧液冷媒は、管路17、
止弁18および逆止弁19を通り合流点20に至
り、他方水冷コンデンサー2で凝縮した高圧液冷
媒も管路21および逆止弁22を通り合流点20
に至る。
The high-pressure gas refrigerant discharged from the refrigerator 1 passes through a pipe line 6 and a check valve 7, reaches a dividing point 8, and is divided into two directions. One side is pipe line 9, differential pressure control valve 1
0, passes through the pipe line 11, the stop valve 12 and the pipe line 13,
Leads to air-cooled condenser 3. The other one passes through a conduit 14 and connects a first solenoid valve 15 and a second solenoid valve 16 in parallel.
and reaches water-cooled condenser 2. In addition, the high-pressure liquid refrigerant condensed in the air-cooled condenser 3 is transferred to the pipe line 17,
The high-pressure liquid refrigerant that has been condensed in the water-cooled condenser 2 also passes through the conduit 21 and the check valve 22 and reaches the confluence point 20 through the stop valve 18 and the check valve 19.
leading to.

かくして、合流点20において合流した高圧液
冷媒は、管路23、ドライヤーストレーナー2
4、管路25および電磁弁26を通り膨張弁27
に達し、そこで膨張した後、空気冷却器4の内部
で蒸発し、低圧ガス冷媒となり、管路28、蒸発
圧力制御弁29および管路30を通り、冷凍機1
に戻る。
Thus, the high-pressure liquid refrigerant that has merged at the confluence point 20 flows through the pipe line 23 and the dryer strainer 2.
4. Expansion valve 27 through pipe line 25 and solenoid valve 26
It expands there, evaporates inside the air cooler 4, becomes a low-pressure gas refrigerant, passes through the pipe 28, the evaporation pressure control valve 29, and the pipe 30, and is supplied to the refrigerator 1.
Return to

通常、空冷コンデンサー3は水冷コンデンサー
2より高位置に設置される。そして、合流点20
の直前の冷媒圧力Pa,Pwは、各コンデンサーの
設置高さの差異に起因する静水頭の差異、各コン
デンサーの液冷媒管の差異に起因する配管抵抗の
差異、ならびに各コンデンサーの凝縮圧力の差異
などの要因により異なる。この相異のままだと、
合流点20手前の冷媒圧力の低い側のコンデンサ
ー内部に冷媒が溜り込み、最終的に系全体の冷媒
の分布バランスが失なわれ、冷凍機の運転が不可
能となる。たとえば、Pw>Paで、冷媒圧力の低
い側のコンデンサー、すなわち空冷コンデンサー
3に液冷媒が溜り込み空冷コンデンサー3が機能
しなくなると、空気冷却器4への冷媒供給量が少
くなり、冷凍機1の吸入圧力が低下し冷凍機1が
停止することすらある。他方、Pw<Paの場合
は、水冷コンデンサー2に液冷媒が溜り込み水冷
コンデンサー2が機能しなくなり、温水が製造で
きず、加熱能力が極端に不足することになる。
Usually, the air-cooled condenser 3 is installed at a higher position than the water-cooled condenser 2. And confluence point 20
The refrigerant pressures Pa and Pw immediately before are determined by the difference in static head due to the difference in the installation height of each condenser, the difference in piping resistance due to the difference in the liquid refrigerant pipes of each condenser, and the difference in condensation pressure of each condenser. It varies depending on factors such as. If this difference remains,
Refrigerant accumulates inside the condenser on the side where the refrigerant pressure is low before the confluence point 20, and eventually the refrigerant distribution balance in the entire system is lost, making it impossible to operate the refrigerator. For example, when Pw > Pa, if liquid refrigerant accumulates in the condenser with lower refrigerant pressure, that is, air-cooled condenser 3, and air-cooled condenser 3 stops functioning, the amount of refrigerant supplied to air cooler 4 decreases, and The suction pressure of the refrigerator 1 may even drop and the refrigerator 1 may even stop. On the other hand, when Pw<Pa, liquid refrigerant accumulates in the water-cooled condenser 2 and the water-cooled condenser 2 ceases to function, making it impossible to produce hot water and resulting in an extremely insufficient heating capacity.

ところで、上述のPaおよびPwは次式で表わさ
れる。
By the way, the above-mentioned Pa and Pw are expressed by the following formula.

Pa=CTa+{(h+H)×γ}−△Pa ……(1) Pw=CTw+(h×γ)−△Pw ………(2) ここで、 Pa:空冷コンデンサーから冷媒の合流点20直
前の圧力(Kg/cm2) Pw:水冷コンデンサーから冷媒の合流点20直
前の圧力(Kg/cm2) CTa:空冷コンデンサーの凝縮圧力(Kg/cm2) CTw:水冷コンデンサーの凝縮圧力(Kg/cm2) h:混合点20よりの水冷コンデンサーの高さ
(m) H:水冷コンデンサーよりの空冷コンデンサーの
高さ(m) γ:液冷媒の1m当りの圧力(Kg/cm2・m) △Pa:空冷コンデンサーより合流点20までの
抵抗損失(Kg/cm2) △Pw:水冷コンデンサーより合流点20までの
抵抗損失(Kg/cm2) そして、合流点20において、2つのコンデン
サーよりの液冷媒が混合合流するためには、Pa
=Pwである必要がある。よつて(3)式の必要があ
る。
Pa=CTa+{(h+H)×γ}−△Pa……(1) Pw=CTw+(h×γ)−△Pw……(2) Here, Pa: Just before the refrigerant confluence point 20 from the air-cooled condenser Pressure (Kg/cm 2 ) Pw: Pressure just before the refrigerant confluence point 20 from the water-cooled condenser (Kg/cm 2 ) CTa: Condensation pressure of the air-cooled condenser (Kg/cm 2 ) CTw: Condensation pressure of the water-cooled condenser (Kg/cm 2 ) h: Height of water-cooled condenser from mixing point 20 (m) H: Height of air-cooled condenser from water-cooled condenser (m) γ: Pressure of liquid refrigerant per 1 m (Kg/cm 2 m) △Pa : Resistance loss from the air-cooled condenser to the confluence point 20 (Kg/cm 2 ) △Pw: Resistance loss from the water-cooled condenser to the confluence point 20 (Kg/cm 2 ) Then, at the confluence point 20, the liquid refrigerant from the two condensers In order to mix and merge, Pa
=Pw must be. Therefore, equation (3) is necessary.

CTw+hγ−△Pw=CTa+hγ+Hγ−△Pa CTw=CTa+Hγ+△Pw−△Pa ………(3) また、ここで△Pwおよび△Paは、CTwおよび
CTaに比較し、値が小さいので配管抵抗を無視す
れば、上記(3)式は、(4)式として表わすことができ
る。
CTw+hγ−△Pw=CTa+hγ+Hγ−△Pa CTw=CTa+Hγ+△Pw−△Pa……(3) Here, △Pw and △Pa are CTw and
Since the value is smaller than CTa, if piping resistance is ignored, the above equation (3) can be expressed as equation (4).

CTw=CTa+Hγ ………(4) この(4)式から、水冷コンデンサー2の凝縮圧力
CTwを、空冷コンデンサー3の凝縮圧力より、
各コンデンサーの設置高さの差によつて生ずる静
水頭Hγだけ昇圧すればよいことが判明する。こ
のために、本発明においては、差圧制御弁10を
設けてあり、静水頭Hγ分を昇圧して(4)式を満す
ようにしており、合流点20において各液冷媒が
確実に混合合流するようにしてある。
CTw=CTa+Hγ……(4) From this equation (4), the condensing pressure of water-cooled condenser 2
Ctw from the condensing pressure of air-cooled condenser 3,
It turns out that it is sufficient to increase the pressure by the hydrostatic head Hγ caused by the difference in the installation height of each capacitor. For this purpose, in the present invention, a differential pressure control valve 10 is provided to increase the pressure of the hydrostatic head Hγ to satisfy equation (4), and to ensure that each liquid refrigerant is mixed at the confluence point 20. It is designed to merge.

次に高圧ガス冷媒の排熱を利用した空気加熱回
路について説明すると、冷却水循環ポンプ31に
よつて加圧された冷却水は、管路32を通り水冷
コンデンサー2に至る。このコンデンサー2の内
部で高圧ガス冷媒より熱を吸収し、温水となり、
管路33、接続具36aおよび管路34を通り、
空気加熱器5に至る。そして空気加熱器5におい
て、空気流Aを加熱する。空気加熱器5を通つた
冷却水は、管路35、3方電動弁36、密閉膨張
タンク37の接続具37aを通り、循環ポンプ3
1に吸入される。38は空気流Aの温度に対する
サーモスタツトで、空気流Aの温度を3方電動弁
36の操作を介して制御している。
Next, an explanation will be given of the air heating circuit that utilizes the exhaust heat of the high-pressure gas refrigerant. Cooling water pressurized by the cooling water circulation pump 31 passes through the pipe line 32 and reaches the water-cooled condenser 2. Inside this condenser 2, heat is absorbed from the high-pressure gas refrigerant and becomes hot water.
Passing through the conduit 33, the connector 36a and the conduit 34,
The air heater 5 is reached. The air stream A is then heated in the air heater 5. The cooling water that has passed through the air heater 5 passes through the pipe line 35, the three-way electric valve 36, and the connector 37a of the sealed expansion tank 37, and then reaches the circulation pump 3.
1 is inhaled. 38 is a thermostat for the temperature of the air flow A, which controls the temperature of the air flow A through operation of the three-way electric valve 36.

ところで、空気加熱器5で空気を加熱する際
に、空気流Aの空気温度の制御精度を高めるため
には、空気加熱器5の入口温水温度、すなわち水
冷コンデンサー2の出口冷却水温度を一定に制御
する必要がある。前述のように、水冷コンデンサ
ー2の凝縮圧力CTwは(4)式で表わされるから、
空冷コンデンサー3の凝縮圧力CTaを一定に保持
するならば、CTwも一定となる。したがつて、
水冷コンデンサー2の内部の冷媒の凝縮温度も、
その圧力に対応する飽和温度となり一定となる。
そして、水冷コンデンサー2の内部で一定温度に
おいて凝縮しており、冷媒に管壁を介して接触し
ている冷却水はある温度範囲内において一定とな
る。この温度範囲は、加熱負荷、水冷コンデンサ
ー2への入口冷却水温度、水量および凝縮温度が
一定とすれば、水冷コンデンサー2の容量によつ
て定まる。したがつて、たとえば、水冷コンデン
サー2の凝縮温度が40℃のときに、最大加熱負荷
時において35℃の温水が得られるように、空気加
熱器5、冷却水量、および水冷コンデンサー2を
選定すればよい。また、加熱負荷の減少に対して
は、水冷コンデンサー2の出口冷却水温度を一定
に保持するために、サーモスタツト39を設け、
電磁弁15,16を台数制御して、水冷コンデン
サー2へ流入する高圧ガス冷媒量を段階的に加減
するようにすればよい。
By the way, in order to improve the control accuracy of the air temperature of the air flow A when heating the air with the air heater 5, it is necessary to keep the inlet hot water temperature of the air heater 5, that is, the outlet cooling water temperature of the water-cooled condenser 2 constant. need to be controlled. As mentioned above, the condensing pressure CTw of the water-cooled condenser 2 is expressed by equation (4), so
If the condensing pressure CTa of the air-cooled condenser 3 is kept constant, CTw will also be constant. Therefore,
The condensation temperature of the refrigerant inside the water-cooled condenser 2 is also
The saturation temperature corresponds to that pressure and remains constant.
The cooling water, which is condensed at a constant temperature inside the water-cooled condenser 2 and is in contact with the refrigerant through the pipe wall, remains constant within a certain temperature range. This temperature range is determined by the capacity of the water-cooled condenser 2, assuming that the heating load, the temperature of the inlet cooling water to the water-cooled condenser 2, the amount of water, and the condensation temperature are constant. Therefore, for example, if the air heater 5, the amount of cooling water, and the water-cooled condenser 2 are selected so that when the condensation temperature of the water-cooled condenser 2 is 40°C, hot water of 35°C can be obtained at the maximum heating load. good. In addition, in order to keep the cooling water temperature at the outlet of the water-cooled condenser 2 constant in response to a decrease in heating load, a thermostat 39 is provided.
The number of electromagnetic valves 15 and 16 may be controlled to adjust the amount of high-pressure gas refrigerant flowing into the water-cooled condenser 2 in stages.

以上の説明によつて明らかであるように、空冷
コンデンサー3の凝縮圧力CTaは一定である必要
がある。すなわち、年間を通しての外気温変化、
および空冷コンデンサー3の凝縮量の変化に対し
て所定の凝縮圧力を保持する必要がある。通常、
外気温を零下20℃よりプラス45℃の範囲、凝縮負
荷の変動巾は100%〜10%の範囲を考えて設計す
ればよい。
As is clear from the above explanation, the condensing pressure CTa of the air-cooled condenser 3 needs to be constant. In other words, changes in outside temperature throughout the year,
It is also necessary to maintain a predetermined condensing pressure against changes in the amount of condensation in the air-cooled condenser 3. usually,
When designing, the outside temperature should be in the range of -20°C to +45°C, and the condensing load fluctuation range should be in the range of 100% to 10%.

かかる要請に適い、空気流Aの空気温度の制御
精度を高めることを目的として水冷コンデンサー
2出口冷却水温度を一定に制御するために、空冷
コンデンサー3の凝縮圧力を一定に制御するため
の凝縮圧力制御装置は次のような構成である。
In order to meet such requirements and to control the cooling water temperature at the outlet of the water-cooled condenser 2 to a constant level in order to improve the control accuracy of the air temperature of the air flow A, the condensing pressure for controlling the condensing pressure of the air-cooled condenser 3 to a constant level is determined. The control device has the following configuration.

実施例での空冷コンデンサー3は、間仕切4
0,41により3室に区分され、各室に電動機直
結のプロペラフアン42,43,44が設けられ
ている。空冷コンデンサー3の能力は、風量おに
よびその凝縮圧力を一定とすれば、凝縮温度と入
口空気温度の差に正比例する特性があり、そこで
サーモスタツト45により外気温度(=入口空気
温度)に応じてフアン43,44を台数制御する
ことにより、空冷コンデンサー3の能力を一定に
保持している。ここで、立上り運転時を除き、定
常運転中は常時運転しておく。
The air-cooled condenser 3 in the embodiment has a partition 4
It is divided into three chambers by 0 and 41, and each chamber is provided with a propeller fan 42, 43, and 44 directly connected to an electric motor. The capacity of the air-cooled condenser 3 is directly proportional to the difference between the condensing temperature and the inlet air temperature, assuming that the air volume and condensation pressure are constant. By controlling the number of fans 43 and 44, the capacity of the air-cooled condenser 3 is kept constant. Here, except during start-up operation, it is operated at all times during steady operation.

またフアン42,43,44の吐出側には風量
制御装置46,47,48が設けられており、こ
れらは内部に設けられたサーモスタツト49によ
り空冷コンデンサー3のコイル内部の常に凝縮し
ている点の冷媒温度が検出され、これに基づいて
電動モータ50により開閉され、風向Bなる風量
を制御することにより空冷コンデンサー3の凝縮
温度、すなわち凝縮圧力が制御されるようになつ
ている。ここで、本発明にかかる空気調和装置
は、前述のように外気温−20℃〜+45℃、凝縮負
荷100%〜10%の範囲内で、かつ凝縮圧力を一定
に保持させようとするものであるため、通常のボ
リユームダンパーでは不適当であり、風量制御装
置46,47,48はその開度に応じて100%〜
0%まで無段階に風量を変化させる構造とすべき
である。なお、52はチヤージ弁である。
Further, air volume control devices 46, 47, and 48 are provided on the discharge side of the fans 42, 43, and 44, and these devices are controlled by a thermostat 49 provided inside to ensure that condensation is always maintained inside the coil of the air-cooled condenser 3. The refrigerant temperature of the air-cooled condenser 3 is detected, and the refrigerant temperature of the air-cooled condenser 3, that is, the condensation pressure, is controlled by opening and closing the refrigerant by the electric motor 50 and controlling the air volume in the wind direction B. Here, as mentioned above, the air conditioner according to the present invention is intended to keep the outside temperature within the range of -20°C to +45°C, the condensing load within the range of 100% to 10%, and the condensing pressure constant. Therefore, a normal volume damper is not suitable, and the air volume control devices 46, 47, and 48 can be adjusted from 100% to 100% depending on their opening degree.
The structure should be such that the air volume can be changed steplessly down to 0%. Note that 52 is a charge valve.

次に冬期、室内の暖房負荷における始動時の立
上り運転方法の説明をする。一般に電子計算機室
を対象とする場合、電子計算機の停止時は、冬期
においては、室内は暖房負荷となつている。室内
温度を約16℃まで上昇させてから、電子計算機を
パワーオンし、以後室内を冷房負荷に変えてい
る。
Next, we will explain the start-up operation method at the time of starting an indoor heating load in winter. Generally, when a computer room is targeted, when the computers are stopped, the room is under heating load in winter. After raising the indoor temperature to approximately 16°C, the computer was powered on, and from then on the room was turned into an air-conditioner.

本発明の加熱装置は、前記のように高圧ガス冷
媒より、水冷コンデンサー2を介して温水を取り
出しているため、立上りに際し、速かに所定温度
の温水を取り出すよう、凝縮圧力を速かに所定圧
力以上に昇圧させる必要がある。しかし、外気温
度が低い場合、空冷コンデンサー3全体は、外気
温と同じ温度に冷却されていることと、室内が暖
房負荷のため、パツケージ内部の空気冷却器4に
負荷がかからないため、通常の方法では所定の凝
縮圧力に昇圧せず、所定温水が得られないため、
電子計算機のパワーオン条件である室内温度が得
られない。その結果、立上り不能となる。
Since the heating device of the present invention extracts hot water from the high-pressure gas refrigerant via the water-cooled condenser 2 as described above, the condensing pressure is quickly set to a predetermined value so that hot water at a predetermined temperature can be quickly taken out at the time of startup. It is necessary to increase the pressure above the pressure. However, when the outside air temperature is low, the entire air-cooled condenser 3 is cooled to the same temperature as the outside air temperature, and because the room is under heating load, there is no load on the air cooler 4 inside the package, so the normal method is not used. In this case, the pressure cannot be increased to the specified condensing pressure and the specified hot water cannot be obtained.
The indoor temperature, which is the power-on condition for the computer, cannot be obtained. As a result, it becomes impossible to stand up.

そこで次のような操作を採る。すなわち立上り
の際、フアン43,44をサーモスタツト45に
より自動停止させておき、フアン42は圧力スイ
ツチ51により自動停止にし、風量制御装置4
6,47,48をサーモスタツト49および電動
モータ50により全閉としておく。これによつて
空冷コンデンサー3の凝縮圧力は速かに上昇し、
所定の圧力に達するようになる。その結果、水冷
コンデンサー2の凝縮圧力も所定の圧力に達す
る。したがつて、水冷コンデンサー2からの出口
冷却水温度は所定温度に上昇し、加熱器5が働
き、室内の温度が速かに16℃まで昇温する。な
お、空冷コンデンサー3の凝縮圧力が所定圧力に
達すると、圧力スイツチ51が動作し、フアン4
2が運転し始め、立上り運転終了の指令が発生せ
られ、以後定常運転に入る。
Therefore, take the following steps. That is, at the time of startup, the fans 43 and 44 are automatically stopped by the thermostat 45, the fan 42 is automatically stopped by the pressure switch 51, and the air volume control device 4 is automatically stopped.
6, 47, and 48 are kept fully closed by a thermostat 49 and an electric motor 50. As a result, the condensing pressure in the air-cooled condenser 3 increases rapidly,
A predetermined pressure is reached. As a result, the condensation pressure of the water-cooled condenser 2 also reaches a predetermined pressure. Therefore, the temperature of the outlet cooling water from the water-cooled condenser 2 rises to a predetermined temperature, the heater 5 works, and the indoor temperature quickly rises to 16°C. Note that when the condensation pressure of the air-cooled condenser 3 reaches a predetermined pressure, the pressure switch 51 operates and the fan 4
2 begins to operate, a command to end the start-up operation is issued, and from then on, steady operation begins.

ところで、上記例は空冷コンデンサーをたとえ
ば屋上に設置する例であるが、本発明では水平方
向に遠方である場合及び下方方向の遠方である場
合も含む。
By the way, although the above example is an example in which the air-cooled condenser is installed, for example, on a rooftop, the present invention also includes cases where the air-cooled condenser is installed far away in the horizontal direction and far away in the downward direction.

以上の通り、本発明は、従来の直列接続方式と
異なり水冷コンデンサーと空冷コンデンサーとを
並列接続するに当り、差圧制御弁を設けたので、
確実に各コンデンサーからの液冷媒を混合合流で
き、したがつて冷凍機の円滑な運転を行うことが
できる。また冷却水回路の温度制御に当つて、空
冷コンデンサーの凝縮圧力(温度)を制御するか
ら、精度の高い空気加熱を行うことができる。
As described above, unlike the conventional series connection system, the present invention provides a differential pressure control valve when connecting a water-cooled condenser and an air-cooled condenser in parallel.
The liquid refrigerant from each condenser can be reliably mixed and merged, so that the refrigerator can operate smoothly. Furthermore, since the condensing pressure (temperature) of the air-cooled condenser is controlled in controlling the temperature of the cooling water circuit, highly accurate air heating can be performed.

なお、空冷コンデンサーの凝縮圧力の制御とと
もに、冷却水より熱を吸収する加熱負荷の変動に
対して、高圧ガス冷媒量を制御弁15,16等に
より制御すると一層高精度の制御が可能となる。
In addition to controlling the condensing pressure of the air-cooled condenser, even more precise control is possible by controlling the amount of high-pressure gas refrigerant using the control valves 15, 16, etc. in response to fluctuations in the heating load that absorbs heat from the cooling water.

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

図面は本発明装置の一例を示すフロー図であ
る。 1……冷凍機、2……水冷コンデンサー、3…
…空冷コンデンサー、4……空気冷却機、5……
空気加熱器、8……分流点、10……差圧制御
弁、20……合流点。
The drawing is a flow diagram showing an example of the apparatus of the present invention. 1... Refrigerator, 2... Water-cooled condenser, 3...
...Air-cooled condenser, 4...Air cooler, 5...
Air heater, 8... Diversion point, 10... Differential pressure control valve, 20... Merging point.

Claims (1)

【特許請求の範囲】[Claims] 1 冷凍機と、これから吐出された高圧ガス冷媒
が供給される水冷コンデンサーと、これと並列に
配されかつ遠方位置に配された空冷コンデンサー
と、前記水冷コンデンサーおよび空冷コンデンサ
ーにおいて凝縮した高圧液冷媒を合流させながら
空気冷却器を介して冷凍機へ戻す冷媒循環手段と
をそなえた空気調和装置であつて、前記高圧液冷
媒の合流点において水冷コンデンサー側の高圧液
冷媒圧力と空冷コンデンサー側の高圧液冷媒圧力
とを等しくするよう作動するように冷凍機から水
冷コンデンサーおよび空冷コンデンサーへの高圧
ガス冷媒系統の分流点以後の空冷コンデンサーへ
の高圧ガス冷媒系統に設けられた差圧制御弁と、
前記水冷コンデンサーにおいて、冷却水が温水化
され、この温水が空気加熱器に通される冷却水回
路と、空冷コンデンサーの凝縮圧力制御装置とを
設けたことを特徴とする空気調和装置。
1. A refrigerator, a water-cooled condenser to which the high-pressure gas refrigerant discharged from the refrigerator is supplied, an air-cooled condenser placed in parallel with this and located far away, and a high-pressure liquid refrigerant condensed in the water-cooled condenser and the air-cooled condenser. The air conditioner is equipped with a refrigerant circulation means that returns the refrigerant to the refrigerator via an air cooler while merging the high-pressure liquid refrigerant, and the pressure of the high-pressure liquid refrigerant on the water-cooled condenser side and the high-pressure liquid on the air-cooled condenser side are reduced at the confluence point of the high-pressure liquid refrigerant. A differential pressure control valve provided in the high-pressure gas refrigerant system from the refrigerator to the water-cooled condenser and the air-cooled condenser after the branch point of the high-pressure gas refrigerant system to the air-cooled condenser so as to operate to equalize the refrigerant pressure;
An air conditioner characterized in that the water-cooled condenser is provided with a cooling water circuit in which the cooling water is heated and the hot water is passed through an air heater, and a condensation pressure control device for the air-cooled condenser.
JP7807881A 1981-05-25 1981-05-25 Air conditioner Granted JPS57192773A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7807881A JPS57192773A (en) 1981-05-25 1981-05-25 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7807881A JPS57192773A (en) 1981-05-25 1981-05-25 Air conditioner

Publications (2)

Publication Number Publication Date
JPS57192773A JPS57192773A (en) 1982-11-26
JPS6112184B2 true JPS6112184B2 (en) 1986-04-07

Family

ID=13651803

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7807881A Granted JPS57192773A (en) 1981-05-25 1981-05-25 Air conditioner

Country Status (1)

Country Link
JP (1) JPS57192773A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07109333B2 (en) * 1984-08-20 1995-11-22 新日本空調株式会社 Heat recovery air conditioner
JP2616762B2 (en) * 1985-11-19 1997-06-04 トヨタ自動車株式会社 Rear wheel steering device

Also Published As

Publication number Publication date
JPS57192773A (en) 1982-11-26

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