Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0411779B2 - - Google Patents
[go: Go Back, main page]

JPH0411779B2 - - Google Patents

Info

Publication number
JPH0411779B2
JPH0411779B2 JP62212560A JP21256087A JPH0411779B2 JP H0411779 B2 JPH0411779 B2 JP H0411779B2 JP 62212560 A JP62212560 A JP 62212560A JP 21256087 A JP21256087 A JP 21256087A JP H0411779 B2 JPH0411779 B2 JP H0411779B2
Authority
JP
Japan
Prior art keywords
temperature
refrigerant
heater
hot water
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 - Lifetime
Application number
JP62212560A
Other languages
Japanese (ja)
Other versions
JPS6454180A (en
Inventor
Toshuki Kaneko
Shigenori Tateshita
Norio Sawada
Yoshiki Iwatani
Hisao Pponda
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP21256087A priority Critical patent/JPS6454180A/en
Publication of JPS6454180A publication Critical patent/JPS6454180A/en
Publication of JPH0411779B2 publication Critical patent/JPH0411779B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、冷媒と吸収液の循環路を形成すると
共に温水器を発生器に付設してこれら機器間に冷
媒循環路を形成し、冷温水を同時に取出すことの
可能な型式の吸収冷温水機の改良に関する。
[Detailed description of the invention] (a) Industrial application field The present invention forms a refrigerant circulation path for a refrigerant and an absorption liquid, and also attaches a water heater to a generator to form a refrigerant circulation path between these devices. This invention relates to an improvement in an absorption chiller/heater that is capable of taking out cold and hot water at the same time.

(ロ) 従来の技術 上記型式の吸収冷温水機の従来の技術として、
例えば特公昭52−584号公報にみられるように、
冷水温度または温水温度により発生器の加熱量制
御あるいはこの加熱量制御と冷媒流量制御などと
の組合せ制御を行なう容量制御装置〔調温能力制
御機器〕を備えると共に冷水管路に保護サーモを
備え、このサーモにより特定の冷水温度〔例えば
3℃〕で冷媒液用ポンプの作動を停止し、この特
定の冷水温度よりも低い温度で前記容量制御装置
により発生器の加熱を止めるものが知られてい
る。
(b) Conventional technology The conventional technology of the above type of absorption chiller/heater is as follows:
For example, as seen in Special Publication No. 52-584,
Equipped with a capacity control device (temperature control capacity control device) that controls the heating amount of the generator or a combination of this heating amount control and refrigerant flow rate control based on the chilled water temperature or hot water temperature, and is equipped with a protective thermostat in the cold water pipe, It is known that this thermostat stops the operation of the refrigerant liquid pump at a specific chilled water temperature (for example, 3°C), and the capacity control device stops heating the generator at a temperature lower than this specific chilled water temperature. .

(ハ) 発明が解決しようとする問題点 冷温水同時取出しの可能な前述の型式の吸収冷
温水機においては、温水負荷が大きくて冷水負荷
が小さい場合に発生器の加熱量を温水負荷に見合
うよう調節する必要があるため、冷水負荷に対す
る冷水出力すなわち蒸発器での冷媒の蒸発能力言
い代えれば吸収器での吸収液の冷媒吸収能力つま
り発生器での吸収液の濃縮の度合が過大になりや
すく、蒸発器での冷媒の凍結や冷水の凍結などを
生じやすい傾向がある。
(c) Problems to be solved by the invention In the above-mentioned type of absorption chiller/heater that can take out hot and cold water at the same time, when the hot water load is large and the cold water load is small, it is difficult to adjust the heating amount of the generator to match the hot water load. As a result, the chilled water output for the chilled water load, that is, the refrigerant evaporation capacity in the evaporator, or in other words, the refrigerant absorption capacity of the absorption liquid in the absorber, that is, the degree of concentration of the absorption liquid in the generator, may become excessive. This tends to cause freezing of the refrigerant in the evaporator and freezing of the cold water.

このため、上記した従来の吸収冷温水機におい
ては、冷水管路に備えた保護サーモにより冷媒液
用ポンプの作動を冷水の特定温度で停止させ、さ
らにこの特定温度よりも低い温度で発生器の加熱
を断ち吸収液の濃縮を止め、冷水の凍結を防ぐ方
法が採られている。しかし、この方法は吸収器に
おける吸収液の濃度降下言い代えれば蒸発器およ
び吸収器における飽和温度の正常値までの上昇に
時間を要するために、例えば冷却水の低下時には
冷媒凍結や冷水凍結あるいは吸収液の結晶などの
弊害を継ぎきれない問題点があつた。また、凍結
を防ぐためにしばしば発生器の加熱を断つことに
なり、温水負荷に対する温水出力が不安定かつ不
十分となりやすい問題点もあつた。
For this reason, in the above-mentioned conventional absorption chiller/heater, a protective thermometer provided in the chilled water pipe stops the operation of the refrigerant liquid pump at a specific temperature of the chilled water, and furthermore, the generator stops operating at a temperature lower than this specific temperature. A method is used to prevent the cold water from freezing by cutting off the heating and stopping the concentration of the absorption liquid. However, with this method, it takes time for the concentration of the absorption liquid in the absorber to drop, or in other words, for the saturation temperature in the evaporator and absorber to rise to its normal value. Problems such as liquid crystallization could not be overcome. In addition, in order to prevent freezing, the heating of the generator was often cut off, which caused the problem that the hot water output for the hot water load was likely to be unstable and insufficient.

本発明は、このような問題点に鑑み、従来のも
のよりも冷媒や冷水の凍結および吸収液の結晶な
どの弊害を確実に防ぎ得、かつ、温水出力もより
安定的に得ることの可能な吸収冷温水機の提供を
目的としたものである。
In view of these problems, the present invention has been developed to more reliably prevent harmful effects such as freezing of refrigerant and cold water and crystallization of absorption liquid than conventional methods, and also to obtain hot water output more stably. The purpose is to provide an absorption chiller/heater.

(ニ) 問題点を解決するための手段 本発明は、上記の問題点を解決するために、蒸
発器から吸収器に至り冷媒液ブロー用ポンプを有
した管路を備えると共に、発生器の加熱量を蒸発
器の冷水出口温度または温水器の温水出口温度に
より制御する温度調節器(制御器)と、冷媒液ブ
ロー用ポンプの作動と冷媒液用ポンプの作動とを
蒸発器の冷水出口温度により制御するコントロー
ラー(制御器)とを備えた吸収冷温水機を提供す
るものである。
(d) Means for Solving the Problems In order to solve the above problems, the present invention provides a pipe line that extends from the evaporator to the absorber and has a pump for blowing the refrigerant liquid, and also provides a pipe line for heating the generator. A temperature regulator (controller) that controls the amount by the cold water outlet temperature of the evaporator or hot water outlet temperature of the water heater, and a temperature regulator (controller) that controls the operation of the refrigerant liquid blowing pump and the refrigerant liquid pump depending on the cold water outlet temperature of the evaporator. The present invention provides an absorption chiller/heater equipped with a controller for controlling the water.

(ホ) 作 用 本発明の吸収冷温水機においては、その冷水出
口側温度が、設定値〔例えば5.0℃〕になるとコ
ントローラー40が冷媒液用ポンプの作動を停止
させたり、冷媒液ブロー用ポンプを作動させる制
御を行なうことにより、蒸発器を流通する冷水と
冷媒との熱交換を断つ作用および吸収器での吸収
液の濃度を速やかに低下させる作用を発揮する。
これらの作用により、従来のものにくらべ、蒸発
器および吸収器内の飽和温度が短時間で正常値
〔例えば6〜8℃〕に回復し、温水負荷が冷水負
荷に対して著しく大きい場合に発生器の加熱停止
の頻度を大幅に少なくして冷水や冷媒の凍結およ
び吸収液の結晶をより確実に防ぐことができ、か
つ、温水負荷に対する温水出力も安定的に得るこ
とができる。また、この場合に、吸収器側から発
生器へ戻される吸収液の濃度が低下して発生器を
循環する吸収液の沸騰温度の降下作用も発揮され
るため、発生器における顕熱消費量が節約される
効果がもたらされることになり、効率の良い温水
出力を得ることができる。さらに、冷媒液の吸収
器へのブロー及び冷媒液の蒸発器への散布の停止
を冷媒液ブロー用ポンプの作動及び冷媒用ポプの
停止によつて、漏れが発生し易い三方弁などを用
いないで確実に行うことができ、三方弁などを用
いて冷媒の流路を切換える構成の吸収冷温水機と
比較して機器内への外気の漏れを防止することが
でき、運転を長期間にわたつて安定することがで
きる。
(e) Function In the absorption chiller/heater of the present invention, when the temperature at the outlet side of the chilled water reaches a set value (for example, 5.0°C), the controller 40 stops the operation of the refrigerant liquid pump, and stops the operation of the refrigerant liquid blowing pump. By controlling the operation of the evaporator, it is possible to cut off heat exchange between the cold water flowing through the evaporator and the refrigerant, and to quickly reduce the concentration of the absorption liquid in the absorber.
Due to these effects, the saturation temperature in the evaporator and absorber recovers to normal values (e.g. 6 to 8 degrees Celsius) in a shorter time than in conventional systems, and this occurs when the hot water load is significantly larger than the cold water load. It is possible to significantly reduce the frequency of stopping the heating of the vessel, thereby more reliably preventing freezing of the cold water and refrigerant and crystallization of the absorption liquid, and also stably obtaining hot water output for hot water loads. In addition, in this case, the concentration of the absorption liquid returned from the absorber side to the generator decreases, and the boiling temperature of the absorption liquid circulating in the generator is lowered, so the sensible heat consumption in the generator is reduced. This results in a saving effect and allows efficient hot water output to be obtained. Furthermore, the blowing of refrigerant liquid to the absorber and the dispersion of refrigerant liquid to the evaporator are stopped by operating the refrigerant liquid blowing pump and stopping the refrigerant pop, thereby avoiding the use of three-way valves that are prone to leaks. Compared to absorption chiller-heating machines that use a three-way valve to switch the refrigerant flow path, leakage of outside air into the equipment can be prevented, and operation can be carried out over long periods of time. It can be stabilized.

(ヘ) 実施例 以下に第1図に従い吸収冷温水機について説明
すると、1は蒸発器2と吸収器3とを内蔵する蒸
発吸収胴、4は凝縮器5と低圧発生器6とを内蔵
する凝縮発生胴、7は加熱器8を有する高圧発生
器であり、加温制御弁9を介して接続される温水
器10に入口管11から水を導入して温水を製造
し、温水出口管12から温水を取り出すと同時
に、冷水は、入口管13から蒸発器2内に水を導
入して、熱交換器14で冷水を製造し、冷水出口
管15から冷水を取り出すようにしたものであ
る。
(F) Embodiment The absorption chiller/heater will be explained below according to Fig. 1. 1 is an evaporator/absorption shell that has a built-in evaporator 2 and an absorber 3, and 4 has a built-in condenser 5 and a low-pressure generator 6. The condensation generating cylinder 7 is a high pressure generator having a heater 8, which produces hot water by introducing water from an inlet pipe 11 to a water heater 10 connected via a heating control valve 9, and a hot water outlet pipe 12. At the same time as hot water is taken out, cold water is introduced into the evaporator 2 from an inlet pipe 13, cold water is produced in a heat exchanger 14, and cold water is taken out from a cold water outlet pipe 15.

すなわち、高圧発生器7の稀液を燃焼炎等の加
熱器8で加熱することにより吸収液から分離され
た冷媒は、温水器10で凝縮して潜熱を循環する
水に与えて温水を作る。一方、低圧発生器6にお
いても熱を与えて未分離冷媒を更に加熱分離して
凝縮器5に流入させ、両発生器7,6からの冷媒
が凝縮器5で混合して蒸発器2に流入し、冷媒ポ
ンプ16で循環されつつ、熱交換器14で気化潜
熱を得て入口管13からの水を冷却し冷水を製造
する。蒸発器2で蒸発した冷媒は吸収器3におい
て吸収液で吸収され、吸収液制御弁17、熱交換
器18,18′を経て高圧発生器7で再び吸収液
と冷媒とに分離される。
That is, the refrigerant separated from the absorption liquid by heating the diluted liquid in the high-pressure generator 7 with a heater 8 such as a combustion flame is condensed in a water heater 10 and gives latent heat to circulating water to produce hot water. On the other hand, heat is also applied in the low pressure generator 6 to further heat and separate the unseparated refrigerant, causing it to flow into the condenser 5, and the refrigerants from both generators 7 and 6 are mixed in the condenser 5 and flow into the evaporator 2. While being circulated by the refrigerant pump 16, latent heat of vaporization is obtained by the heat exchanger 14 to cool the water from the inlet pipe 13 to produce cold water. The refrigerant evaporated in the evaporator 2 is absorbed by the absorption liquid in the absorber 3, passes through the absorption liquid control valve 17 and the heat exchangers 18, 18', and is again separated into the absorption liquid and the refrigerant in the high pressure generator 7.

尚、19は吸収液を吸収器3に循環させるポン
プ、20,21は吸収器3、凝縮器5を冷却水で
冷却する熱交換器である。
Note that 19 is a pump that circulates the absorption liquid to the absorber 3, and 20 and 21 are heat exchangers that cool the absorber 3 and condenser 5 with cooling water.

而して、温水出口管12には温水温度検出器2
2、冷水出口管15には冷水温度検出器23が取
付けられそれぞれの検出器22,23は、冷温切
替スイツチ24,25を介して、いずれかの検出
器で吸収液循環量を制御する吸収液制御弁17、
更には加熱器8への供給熱源である例えば燃料制
御弁26等吸収式冷温水機全体の容量制御装置を
蒸発器2の冷水出口温度(以下、冷水温度とい
う)又は温水器10の温水口温度(以下、温水温
度という)のいずれかで選択制御できるようにす
ると共に温水温度、加温容量単独では、温度調節
器27を介して加温制御弁9で、温水器10内冷
媒液面により伝熱面積を変えて制御する。又、冷
水温度、冷却容量単独では温度調節器28を介し
て冷媒制御弁29の開度で制御される。
Therefore, the hot water temperature detector 2 is installed in the hot water outlet pipe 12.
2. A cold water temperature detector 23 is attached to the cold water outlet pipe 15, and each of the detectors 22, 23 controls the amount of absorption liquid circulated by one of the detectors via cold/temperature changeover switches 24, 25. control valve 17,
Furthermore, the capacity control device for the entire absorption type water chiller/heater, such as the fuel control valve 26, which is the heat source supplied to the heater 8, is adjusted to the cold water outlet temperature of the evaporator 2 (hereinafter referred to as cold water temperature) or the hot water inlet temperature of the water heater 10. (hereinafter referred to as hot water temperature).In addition, the hot water temperature and heating capacity alone can be controlled by the heating control valve 9 via the temperature regulator 27 by the refrigerant liquid level in the water heater 10. Control by changing the heat area. Further, the chilled water temperature and the cooling capacity alone are controlled by the opening degree of the refrigerant control valve 29 via the temperature regulator 28.

30は冷水出口温度検出器31、冷水入口温度
検出器32、切替制御比較器33等から構成され
た負荷検出器であり、冷水負荷が設定値より大き
いときは冷水温度により、逆に、冷水負荷が設定
値より小さいときは温水温度により前記容量制御
装置が制御されるよう、冷温切替スイツチ24,
25を冷接点C又は温接点Hに自動的に切替える
ようにしたものである。
30 is a load detector composed of a chilled water outlet temperature detector 31, a chilled water inlet temperature detector 32, a switching control comparator 33, etc. When the chilled water load is larger than a set value, the chilled water temperature is changed; is smaller than the set value, a cold/temperature changeover switch 24,
25 is automatically switched to cold junction C or hot junction H.

斯る構成による制御の作動を具体的に説明する
と、冷水負荷が一定量(例えば全体の冷温水負荷
の30%)以上の場合、冷温切替スイツチ24,2
5が共に冷接点Cに入つており、冷水出口温度を
冷水温度検出器23で検出し、冷水側の温度調節
器(制御器)34によつて吸収液制御弁17を比
例制御し、更には燃料制御弁26を操作し、冷水
能力を制御する。一方、温水は、温水出口温度を
検出器22で検出し、温度調節器27によつて加
温制御弁9を操作し、温水器10内の冷媒液面を
増減させ、温水器中の温水管の伝熱面積を変えて
一定温度の温水を得る。
To explain the operation of the control by such a configuration in detail, when the chilled water load exceeds a certain amount (for example, 30% of the total chilled/hot water load), the cold/hot temperature changeover switch 24, 2
5 are both connected to the cold junction C, the cold water outlet temperature is detected by the cold water temperature detector 23, and the absorption liquid control valve 17 is proportionally controlled by the cold water side temperature regulator (controller) 34. The fuel control valve 26 is operated to control the chilled water capacity. On the other hand, the hot water is supplied by detecting the hot water outlet temperature with the detector 22, operating the heating control valve 9 with the temperature regulator 27, increasing or decreasing the refrigerant liquid level in the water heater 10, and controlling the hot water pipes in the water heater. Obtain hot water at a constant temperature by changing the heat transfer area.

次に、冷水負荷が一定量以下の場合、負荷検出
器30によつて、自動的に冷温切替スイツチ24
を温接点Hに切替え温水出口温度を検出器22で
検出し、温度調節器(制御器)34′によつて吸
収液制御弁17、更には燃料制御弁26を操作
し、温水側を主に冷温水機の調温能力が制御され
ることとなる。
Next, when the chilled water load is below a certain level, the load detector 30 automatically switches the cold/temperature changeover switch 24.
is switched to the hot junction H, the hot water outlet temperature is detected by the detector 22, and the temperature regulator (controller) 34' operates the absorption liquid control valve 17 and further the fuel control valve 26 to mainly control the hot water side. The temperature control ability of the water cooler/heater will be controlled.

この場合に、負荷検出器30は例えば冷水の出
入口温度を検出器31,32で検出し、予め設定
温を定めた比較器35,36に伝達し、冷水出口
温度、入口温度が共にそれぞれの比較器の設定値
t1,t2(t2>t1)より低くなつたとき冷水負荷が少
なく、又逆に、設定値t1+α、t2+βより高くな
つたとき冷水負荷が大きいとして切替スイツチを
作動する。
In this case, the load detector 30 detects, for example, the temperature at the inlet and outlet of the chilled water with detectors 31 and 32, and transmits the detected temperature to the comparators 35 and 36, which have preset temperatures, so that both the outlet and inlet temperatures of the chilled water are detected by the respective comparisons. instrument settings
When it becomes lower than t 1 , t 2 (t 2 > t 1 ), the chilled water load is small, and conversely, when it becomes higher than the set values t 1 +α, t 2 +β, the chilled water load is assumed to be large and the changeover switch is activated. .

温水側を主に制御しているときの冷水側の制御
は冷水温度検出器により冷媒制御弁29を制御し
て低圧発生器6への冷媒蒸気による加熱量を制御
して低圧発生器からの冷媒蒸気量を制御し、一定
温度幅内に冷水温度を維持する。
When the hot water side is mainly controlled, the cold water side is controlled by controlling the refrigerant control valve 29 using the chilled water temperature sensor to control the amount of heating by refrigerant vapor to the low pressure generator 6, and controlling the amount of refrigerant from the low pressure generator. Controls the amount of steam and maintains the chilled water temperature within a certain temperature range.

また、37は三方弁38を介して冷媒ポンプ1
6の吐出側の管路と吸収器3の液溜とを結んだ冷
媒ブロー用管路であり、この管路の三方弁38の
開閉と冷媒ポンプ16の発停とが温度検出器39
の接続されているコントローラ(制御器)40例
えば次のようなスケジユールで制御されるように
なつている。すなわち、制御スケジユールの一例
として、温度検出器39の感知温度がコントロー
ラー40の温度設定部の下限設定温度5℃まで降
下すると、このコントローラーにより、三方弁3
8の開閉が切換えられて冷媒液が吸収液中にブロ
ーされつつ吸収液の濃度が急速に低められる一方
で熱交換器14への冷媒液の散布が断たれ、その
後に冷媒ポンプの作動が停止されるようになつて
いる。なお、温度検出器39の感知温度がコント
ローラー40の設定温度5.5℃に復帰すると三方
弁38の開閉が元の状態に切換えられ、その後、
冷媒ポンプ16が再び稼働されるようになつてい
る。なおまた、図示していないが、コントローラ
ー40には遅延リレーあるいはタイマーなどの回
路が内蔵されている。
Further, 37 is connected to the refrigerant pump 1 via the three-way valve 38.
This is a refrigerant blowing conduit connecting the discharge side conduit 6 and the liquid reservoir of the absorber 3, and the temperature sensor 39 controls the opening and closing of the three-way valve 38 of this conduit and the start/stop of the refrigerant pump 16.
The connected controller 40 is controlled, for example, according to the following schedule. That is, as an example of the control schedule, when the temperature sensed by the temperature detector 39 drops to the lower limit set temperature of 5° C. of the temperature setting section of the controller 40, the controller controls the three-way valve 3.
8 is switched to open and close, the refrigerant liquid is blown into the absorption liquid, and the concentration of the absorption liquid is rapidly lowered, while the distribution of the refrigerant liquid to the heat exchanger 14 is cut off, and then the operation of the refrigerant pump is stopped. It is becoming more and more common. Note that when the temperature detected by the temperature detector 39 returns to the set temperature of the controller 40 of 5.5°C, the opening and closing of the three-way valve 38 is switched to the original state, and thereafter,
Refrigerant pump 16 is now in operation again. Although not shown, the controller 40 has a built-in circuit such as a delay relay or a timer.

第2図は本発明による吸収冷温水機の一実施例
を示した概略構成説明図であり、この図において
第1図の吸収冷温水機の構成機器と同様のものに
は同一の符号を付している。第2図において、
CCは吸収冷温水機の冷水主制御時の制御器で、
これは第1図に示した温度調節器28,34,4
0の機能を具備しており、CHは温水主制御時の
制御器で、これは第1図に示した温度調節器2
7,34′の機能を具備している。すなわち、こ
の実施例では検出器22,23、制御器CC,CH
加温制御弁9、燃料制御弁26および冷媒制御弁
29で吸収冷温水機の容量制御装置が構成されて
いるのである。なお、この容量制御装置に制御器
CCおよび/またはCHによるポンプ19の吐出量
制御を組み込んで良いことは勿論である。
FIG. 2 is a schematic structural explanatory diagram showing one embodiment of the absorption chiller/heater according to the present invention, and in this figure, the same components as those of the absorption chiller/heater shown in FIG. 1 are given the same reference numerals. are doing. In Figure 2,
C C is the controller for main cold water control of the absorption chiller/heater.
This is the temperature controller 28, 34, 4 shown in FIG.
C H is the controller for hot water main control, and this is the temperature controller 2 shown in Figure 1.
It has the functions of 7 and 34'. That is, in this embodiment, the detectors 22, 23, the controllers C C , C H ,
The heating control valve 9, the fuel control valve 26, and the refrigerant control valve 29 constitute a capacity control device for the absorption chiller/heater. In addition, this capacity control device is equipped with a controller.
Of course, control of the discharge amount of the pump 19 using C C and/or C H may be incorporated.

また、制御器CCは第1図に示したコントロー
ラー40の機能も具備しており、この制御器によ
り管路37の冷媒液ブロー用ポンプPおよび冷媒
ポンプ16の発停〔ON・OFF〕が例えば第3図
に示すように制御される。そして、吸収冷温水機
の温水主制御時、すなわち、温水出口温度の検出
器22の信号で制御器CHを介して燃料制御弁2
6の開度を制御している時、冷水出口温度が5℃
まで降下した際に第3図に示すように冷媒ポンプ
16の作動が停止されると同時に冷媒液ブロー用
ポンプPの作動が開始されることにより、熱交換
器14への冷媒液の散布が断たれてこの気化に伴
なう冷水の降温が防止されると同時に吸収器3内
の吸収液が希釈されてその飽和蒸気圧、飽和温度
の上昇が促進される結果、この際に冷却水温が通
常よりもやゝ低くなつても、高温発生器1の加熱
を止めることなく冷媒および冷水の凍結と吸収液
の結晶を防ぐことができ、かつ、負荷に見合う温
水出口を安定的に得ることが可能となる。また、
この際、高温発生器1に戻される吸収液の濃度が
低くなるため、この発生器内での吸収液の沸騰温
度が降下し、その降下分だけ吸収液の顕熱消費量
が減り、温水出力の熱効率も向上する。さらに、
冷媒液の吸収器3へのブローを冷媒液ブロー用ポ
ンプPと冷媒ポンプ16の発停によつて行つてい
るので、三方弁などを用いて冷媒液のブローを行
う場合に発生し易い機器内への外気の漏れを回避
することができこの結果、冷媒液のブローを行つ
た場合にも、吸収冷温水機の運転を長期間にわた
つて安定することができる。なお、41は液面制
御器で、これによつてもポンプ16、Pの作動が
制御されるようになつている。
In addition, the controller C C also has the functions of the controller 40 shown in FIG. For example, it is controlled as shown in FIG. During the main control of the hot water of the absorption chiller/heater, in other words, the signal from the hot water outlet temperature detector 22 is sent to the fuel control valve 2 via the controller CH .
When controlling the opening degree of 6, the cold water outlet temperature is 5℃
As shown in FIG. 3, the operation of the refrigerant pump 16 is stopped and the operation of the refrigerant liquid blowing pump P is started at the same time as shown in FIG. At the same time, the absorption liquid in the absorber 3 is diluted and its saturated vapor pressure and saturation temperature are promoted to rise. Even if the temperature is slightly lower than the above, it is possible to prevent freezing of the refrigerant and cold water and crystallization of the absorption liquid without stopping the heating of the high temperature generator 1, and it is also possible to stably obtain a hot water outlet commensurate with the load. becomes. Also,
At this time, the concentration of the absorption liquid returned to the high-temperature generator 1 becomes lower, so the boiling temperature of the absorption liquid in this generator drops, the sensible heat consumption of the absorption liquid decreases by the amount of the drop, and the hot water output It also improves thermal efficiency. moreover,
Since the refrigerant liquid is blown into the absorber 3 by turning on and off the refrigerant liquid blowing pump P and the refrigerant pump 16, problems within the equipment that are likely to occur when blowing the refrigerant liquid using a three-way valve, etc. As a result, even when the refrigerant liquid is blown, the operation of the absorption chiller/heater can be stabilized over a long period of time. Note that 41 is a liquid level controller, which also controls the operation of the pumps 16 and P.

そして、冷水出口温度が上昇して5.5℃に復帰
すると再び冷媒ポンプ16が稼働されると同時に
冷媒液ブロー用ポンプPの作動が停止されて温水
主制御時の通常の容量制御による冷温水同時取出
し運転へ戻る。なお、ポンプP、16の制御は発
停制御に限らず、吐出量制御であつても良い。な
おまた、この実施例においては、冷水の調温能力
制御の温度域は6〜8℃、温水のそれは48〜52℃
に設定されている。
Then, when the cold water outlet temperature rises and returns to 5.5°C, the refrigerant pump 16 is operated again, and at the same time, the operation of the refrigerant liquid blowing pump P is stopped, and cold and hot water are simultaneously taken out by normal capacity control during hot water main control. Back to driving. Note that the control of the pumps P and 16 is not limited to ON/OFF control, but may also be discharge amount control. Furthermore, in this example, the temperature range of cold water temperature control ability control is 6 to 8 degrees Celsius, and that of hot water is 48 to 52 degrees Celsius.
is set to .

また、第3図に示した制御は温水主制御時に限
らず、冷水主制御時の運転あるいは冷水のみを取
出す運転の時にも行なわれることも無論である。
なお、この実施例での冷温切替スイツチ24,2
5は手動による接点切替が行なわれるようになつ
ている。尤も、この実施例においても、制御器
CCおよびCHに例えばマイクロコンピユータを内
蔵させて検出器22,23の信号により温水負荷
と冷水負荷の大きさを演算させると共にその割合
を演算させ、この割合の設定値を基準にしてスイ
ツチ24,25の接点を自動的に切換える機能を
具備させても良い。
It goes without saying that the control shown in FIG. 3 is performed not only during hot water main control, but also during cold water main control or when only cold water is taken out.
In this embodiment, the cold/hot selector switches 24, 2
5, the contacts are switched manually. However, in this embodiment as well, the controller
For example, a microcomputer is built into C C and C H to calculate the magnitude of the hot water load and the cold water load based on the signals from the detectors 22 and 23, as well as to calculate their ratio. , 25 may be provided with a function of automatically switching the contacts.

(ト) 発明の効果 以上のとおり、本発明は、蒸発器から吸収器に
至り冷媒液ブロー用ポンプを有した管路を備える
と共に、冷水温度または温水温度により発生器の
加熱量を制御する制御器と、冷水出口温度により
冷媒液ブロー用ポンプと冷媒ポンプとの作動を制
御する制御器を備えたものであるから、冷水出口
温度が低下したときには冷媒と冷水との熱交換を
断つて冷媒の気化による冷水の温度降下の進行を
防ぐと共に蒸発器および吸収器内の飽和蒸気圧お
よび飽和温度の過度の低下を防ぐ効果言い代えれ
ば冷媒や冷水の凍結防止効果をもたらし、特に、
温水温度で発生器の加熱量制御を行なう温水主制
御時に発生器の加熱を継続したまま温水負荷に見
合う温水出力を安定的に得つつ冷媒凍結および冷
水凍結ならびに吸収液の結晶の防止効果を上記型
式の吸収冷温水機にもたらすことができると共
に、吸収冷温水機の機器内への外気の漏れを回避
することができ、運転を長期間にわたつて安定す
ることができ、実用的価値の高いものである。
(G) Effects of the Invention As described above, the present invention includes a pipe line that extends from the evaporator to the absorber and has a pump for blowing refrigerant liquid, and also provides control for controlling the heating amount of the generator based on the cold water temperature or hot water temperature. This system is equipped with a controller that controls the operation of the refrigerant liquid blowing pump and the refrigerant pump depending on the chilled water outlet temperature, so when the chilled water outlet temperature drops, the heat exchange between the refrigerant and the chilled water is cut off and the refrigerant is turned off. The effect of preventing the temperature drop of chilled water due to vaporization as well as the excessive decrease of the saturated vapor pressure and saturation temperature in the evaporator and absorber In other words, it has the effect of preventing freezing of the refrigerant and chilled water, and in particular,
During main hot water control, which controls the heating amount of the generator based on the hot water temperature, the generator continues to be heated and a stable hot water output commensurate with the hot water load is obtained while preventing refrigerant freezing, cold water freezing, and crystallization of the absorption liquid as described above. It can be applied to various types of absorption chiller/heater, and can also avoid leakage of outside air into the equipment of the absorption chiller/heater, ensuring stable operation over a long period of time, and has high practical value. It is something.

なお、本発明を三重効用の吸収冷温水機に適用
するに限らず、一重効用の吸収冷温水機に適用し
得ることは勿論である。
It should be noted that the present invention is not limited to application to a triple-effect absorption chiller/heater, but can of course be applied to a single-effect absorption chiller/heater.

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

第1図は吸収冷温水機の概略構成説明図、第2
図は本発明による吸収冷温水機の一実施例を示し
た概略構成説明図であり、第3図は第2図の実施
例における冷媒ポンプと冷媒液ブロー用ポンプの
動作例を示した説明図である。 1…蒸発吸収胴、2…蒸発器、3…吸収器、5
…凝縮器、7…高圧発生器、9…加温制御弁、1
0…温水器、14…熱交換器、16…冷媒ポン
プ、18,18′…熱交換器、19…ポンプ、2
2,23…検出器、24,25…冷温切替スイツ
チ、26…燃料制御弁、27,28…温度調節
器、34,34′…温度調節器、37…管路、3
8…三方弁、39…温度検出器、40…コントロ
ーラー、CC,CH…制御器、P…冷媒液ブロー用
ポンプ。
Figure 1 is an explanatory diagram of the general structure of the absorption chiller/heater, Figure 2
The figure is a schematic structural explanatory diagram showing one embodiment of the absorption chiller/heater according to the present invention, and FIG. 3 is an explanatory diagram showing an example of the operation of the refrigerant pump and the refrigerant liquid blowing pump in the embodiment of FIG. 2. It is. 1... Evaporative absorption shell, 2... Evaporator, 3... Absorber, 5
...Condenser, 7...High pressure generator, 9...Heating control valve, 1
0... Water heater, 14... Heat exchanger, 16... Refrigerant pump, 18, 18'... Heat exchanger, 19... Pump, 2
2, 23...Detector, 24, 25...Cold/hot selector switch, 26...Fuel control valve, 27, 28...Temperature regulator, 34, 34'...Temperature regulator, 37...Pipe line, 3
8...Three-way valve, 39...Temperature detector, 40...Controller, C C , C H ...Controller, P...Refrigerant liquid blowing pump.

Claims (1)

【特許請求の範囲】[Claims] 1 発生器、凝縮器、蒸発器、吸収器、溶液熱交
換器、冷媒液用ポンプ、溶液用ポンプなどの機器
を配管接続して冷媒と吸収液との循環路を形成す
ると共に発生器に温水器を付設した吸収冷温水機
において、蒸発器から吸収器に至り冷媒液ブロー
用ポンプを有した管路を備えると共に、発生器の
加熱量を蒸発器の冷水出口温度または温水器の温
水出口温度により制御する制御器と、冷媒液ブロ
ー用ポンプの作動と冷媒液用ポンプの作動とを蒸
発器の冷水出口温度により制御する制御器とを備
えたことを特徴とする吸収冷温水機。
1 Connect equipment such as the generator, condenser, evaporator, absorber, solution heat exchanger, refrigerant liquid pump, and solution pump with piping to form a circulation path for the refrigerant and absorption liquid, and also supply hot water to the generator. In an absorption chiller/heater equipped with a water heater, a pipe line from the evaporator to the absorber is equipped with a pump for blowing refrigerant liquid, and the heating amount of the generator is adjusted to the cold water outlet temperature of the evaporator or the hot water outlet temperature of the water heater. 1. An absorption chiller/heater comprising: a controller that controls the operation of a refrigerant liquid blowing pump and an operation of a refrigerant liquid pump based on the chilled water outlet temperature of an evaporator.
JP21256087A 1987-08-26 1987-08-26 Absorption water chiller and heater Granted JPS6454180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21256087A JPS6454180A (en) 1987-08-26 1987-08-26 Absorption water chiller and heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21256087A JPS6454180A (en) 1987-08-26 1987-08-26 Absorption water chiller and heater

Publications (2)

Publication Number Publication Date
JPS6454180A JPS6454180A (en) 1989-03-01
JPH0411779B2 true JPH0411779B2 (en) 1992-03-02

Family

ID=16624715

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21256087A Granted JPS6454180A (en) 1987-08-26 1987-08-26 Absorption water chiller and heater

Country Status (1)

Country Link
JP (1) JPS6454180A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101852521B (en) * 2010-06-10 2012-09-12 大连三洋制冷有限公司 Load adjusting method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5687758A (en) * 1979-12-18 1981-07-16 Ebara Mfg Absorption type heat pump
JPS586228U (en) * 1981-07-03 1983-01-14 三輪精機株式会社 Economic fuel consumption driving indicator
JPS5811361A (en) * 1981-07-10 1983-01-22 株式会社日立製作所 absorption refrigerator
JPS58160270A (en) * 1982-03-04 1983-09-22 ダイセル化学工業株式会社 Novel plastics tray

Also Published As

Publication number Publication date
JPS6454180A (en) 1989-03-01

Similar Documents

Publication Publication Date Title
KR920003906B1 (en) Absorption cold and hot water machine
JP2560550B2 (en) Absorption cooling / heating device and control method thereof
KR100337209B1 (en) Method of stopping an absorption refrigerator
JP2006343042A (en) Operation method of single double effect absorption refrigerator
JP2985513B2 (en) Absorption cooling and heating system and its control method
JPH0411779B2 (en)
JP4090135B2 (en) Control method of absorption refrigerator
JP2918665B2 (en) Operation stop method and stop control device for absorption chiller / chiller / heater
JP3075944B2 (en) Absorption chiller / heater
JP3999893B2 (en) Absorption chiller / heater controller
JP4077973B2 (en) Operation method of exhaust heat absorption cold water heater
JP3831425B2 (en) Control method of absorption chiller / heater
JP2823266B2 (en) Regenerator control device
JP4149653B2 (en) Operation method of absorption chiller using exhaust heat
JP3735745B2 (en) Cooling operation control method for absorption air conditioner
JP4115020B2 (en) Control method of absorption refrigerator
JP2885637B2 (en) Absorption refrigeration apparatus and control method thereof
JP3157349B2 (en) Absorption refrigerator control device
JP3143251B2 (en) Absorption refrigerator
JP3735744B2 (en) Cooling operation control method for absorption air conditioner
JP3081490B2 (en) Absorption refrigerator
JP2858931B2 (en) Control device for absorption refrigerator
JPS58160780A (en) Controller for absorption refrigerator
JP3157668B2 (en) Absorption chiller / heater
JP2981560B2 (en) Absorption chiller / heater with cooling / heating switching function