JPS5831264A - Absorption heat pump - Google Patents

Absorption heat pump

Info

Publication number
JPS5831264A
JPS5831264A JP12959881A JP12959881A JPS5831264A JP S5831264 A JPS5831264 A JP S5831264A JP 12959881 A JP12959881 A JP 12959881A JP 12959881 A JP12959881 A JP 12959881A JP S5831264 A JPS5831264 A JP S5831264A
Authority
JP
Japan
Prior art keywords
temperature
regenerator
hot water
absorption
heat source
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.)
Pending
Application number
JP12959881A
Other languages
Japanese (ja)
Inventor
「よし」井 一寛
雅裕 古川
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP12959881A priority Critical patent/JPS5831264A/en
Publication of JPS5831264A publication Critical patent/JPS5831264A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は吸収冷凍サイクル?使用して機外に温水や湯な
ど(以下温水等という)を供給するヒートポンプに関す
る。
[Detailed Description of the Invention] Is the present invention an absorption refrigeration cycle? It relates to a heat pump that is used to supply hot water, hot water, etc. (hereinafter referred to as hot water, etc.) to the outside of the machine.

一般に、吸収ヒートポンプは再生器に還流される吸収液
な加熱沸騰させて冷媒と吸収液と2二分離し、気化した
高温冷媒の熱ン凝縮器に与える一方、凝縮した液冷媒を
蒸発器(−供給し、蒸発器に与えられる熱#、副流体以
下熱源水という)から気化潜熱を得た冷媒を吸収器側に
流動させ、吸収液が冷媒?吸収下る際の熱と併せて冷媒
が得た熱を熱交換器(二与える構成乞有しており、再生
器に高温熱源乞供給し、蒸発器に熱源水ビ供給丁れば、
吸収器から凝縮器C二重れる温水回路から温水等が得ら
れるものである。
Generally, in an absorption heat pump, the absorption liquid returned to the regenerator is heated to boiling, separated into refrigerant and absorption liquid, and the vaporized high-temperature refrigerant is fed to the heat condenser, while the condensed liquid refrigerant is sent to the evaporator (- The refrigerant that has obtained the latent heat of vaporization from the heat supplied to the evaporator (subfluid, hereinafter referred to as heat source water) flows to the absorber side, and the absorption liquid becomes the refrigerant. The heat obtained by the refrigerant along with the heat absorbed by the refrigerant is supplied to a heat exchanger.
Hot water, etc. is obtained from a hot water circuit that runs from the absorber to the condenser C.

而して、−ヒ記吸収ヒートポンプ装置の再生器から凝縮
器に流れる冷媒量と蒸発器から吸収器に流れる冷媒量と
は1衡をとって流れているので1例えば、熱源水側の温
間条件が変動して蒸発器における冷媒気化微か変わると
、吸収ヒートポンプから得られる温水温間も変動し1機
外に一定温度の温水等を供給するようC二制御するのが
困難な欠点があった。
Therefore, since the amount of refrigerant flowing from the regenerator to the condenser and the amount of refrigerant flowing from the evaporator to the absorber of the absorption heat pump device described in (h) flow in balance, 1. If the conditions change and the refrigerant vaporization in the evaporator changes slightly, the temperature of the hot water obtained from the absorption heat pump will also change, making it difficult to control the supply of hot water, etc. at a constant temperature to the outside of the machine. .

特に、熱源水として太陽熱温水を使用するときは、水温
が日射槌によって変動しやすく、吸収ヒートポンプと組
み合わせて一定温度のt′晶水等を継続して供給しにく
いものであった。
In particular, when solar hot water is used as the heat source water, the water temperature tends to fluctuate due to solar radiation, making it difficult to continuously supply t' crystal water or the like at a constant temperature in combination with an absorption heat pump.

本発明は、これら従来の吸収ヒートポンプの欠点を解決
し、熱源水温度が変動しても、比較的安定して一定温度
の温水が取り出せるよう、再生器ン低温再生器と高温再
生器とから構成し、熱源水温度が低くなったときは低温
再生器の作動馨休止する一重効用運転、熱源水温度が一
定温度以上のときは二重効用のヒートポンプ運転となる
ように切替えて運転できるようにし、かつ、蒸発器へ。
The present invention solves the drawbacks of these conventional absorption heat pumps, and is composed of a regenerator, a low-temperature regenerator, and a high-temperature regenerator, so that hot water at a constant temperature can be obtained relatively stably even when the heat source water temperature fluctuates. However, when the heat source water temperature becomes low, the operation of the low-temperature regenerator is switched to single-effect operation where the operation is stopped, and when the heat source water temperature is above a certain temperature, the operation is switched to dual-effect heat pump operation. And to the evaporator.

温度変動の少ない熱源水が供給可能なときは、温度レベ
ルの異なる温水等を適宜切替えて取り吊子ことができる
吸収ヒートポンプを提供しようとするものである。
The present invention aims to provide an absorption heat pump that can appropriately switch and suspend hot water or the like having different temperature levels when heat source water with little temperature fluctuation can be supplied.

第1図において、(1)はガスバーナ、オイルバーナや
水蒸気などの高温熱源全加熱源とする加熱器(2)ヲ有
し、該加熱器(2)で臭化リテクム水溶液などの吸収液
を加熱沸騰させて吸収液中の冷媒(水)を気化分離する
高温再生器、(31は高温再生器(1)で気イヒした高
温冷媒の熱乞加熱源とする加熱器(4)を有し、該加熱
器(4)で吸収液中の冷媒を気化分離する低mL杓生器
、(5)は再生器(11(31から流入する冷媒から熱
を奮う熱交換器(6)を有し、冷媒乞液化凝集して蒸発
器f7+c送る凝縮器、(7)は液冷媒を低圧条件下で
気化させること(二よりPA交換器(9)に供給される
熱源水力熱暑器内に取り込む蒸発器、 +101は再生
器+11(311−おいて濃縮された吸収液ポンプする
ことにより蒸発器(7)で気化した冷媒乞吸収させ、冷
媒ガスの熱および冷媒ガスを吸収液か吸収する際の反応
熱ン熱交換器ill)im与える吸収器、 +121は
蒸発器(7)での未−気化冷J4Y循環、散布するよう
にした冷媒ポンプ、u3は冷媒乞吸収して稀釈された補
液を再生器(1)に還流する吸収液ポンプ、(1釘まP
1生器flli31から吸収器(10)に流入する吸収
液と稀液と2熱交換する低温熱変換器、(回は高温再生
器(1)から低温再生器(31に供給される中間液と7
TJ述の補液と2熱交換する高温熱交換器であり、夫々
冷媒液管(l眠開閉弁0η(18)乞有する冷媒管0翅
と冷媒側路管(2G、開閉弁開I2り娶荷する補液管(
ハ)と稀液側路管(ロ)、開閉弁+25)、 12(i
)Y有する中間液管taと中間液側路管(2&等で接続
されて吸収冷凍サイクルン構成し、吸収器および凝縮器
に内蔵された熱交換器u1J(6)ン直列に流れる管路
(シ(支)から温水2得るよう(二構成されている。
In Figure 1, (1) has a heater (2) that uses a high-temperature heat source such as a gas burner, oil burner, or steam as the total heating source, and the heater (2) heats an absorbing liquid such as an aqueous solution of lytecum bromide. A high-temperature regenerator that vaporizes and separates the refrigerant (water) in the absorption liquid by boiling it, (31 has a heater (4) that serves as a heat source for the high-temperature refrigerant stale in the high-temperature regenerator (1), The heater (4) vaporizes and separates the refrigerant in the absorption liquid, the low mL ladle generator (5) has a heat exchanger (6) that extracts heat from the refrigerant flowing from the regenerator (11 (31), The condenser (7) liquefies and condenses the refrigerant and sends it to the evaporator f7+c. , +101 absorbs the refrigerant vaporized in the evaporator (7) by pumping the concentrated absorption liquid in the regenerator +11 (311-), and absorbs the heat of the refrigerant gas and the reaction heat when the refrigerant gas is absorbed by the absorption liquid. +121 is a refrigerant pump that circulates un-vaporized cold J4Y in the evaporator (7) and distributes it; u3 is a regenerator ( 1) Absorbent pump that returns to (1 nail P)
1 low-temperature heat converter that exchanges heat with the absorption liquid and diluted liquid flowing into the absorber (10) from the generator full 31; 7
It is a high-temperature heat exchanger that exchanges heat with the replacement liquid described by TJ. Replacement fluid tube (
c) and diluted liquid side pipe (b), on-off valve +25), 12 (i
)Y, the intermediate liquid pipe ta and the intermediate liquid side pipe (2& etc. are connected to form an absorption refrigeration cycle, and the heat exchanger u1J (6) built in the absorber and condenser flows in series ( It consists of 2 parts, so that 2 parts of hot water can be obtained from 2 parts.

また、上記の開閉弁面(l均I211Q卸ω(20は熱
源水の入口温変音検知する温度検出器C30)により、
或いは。
In addition, due to the above opening/closing valve surface (I211Q wholesale ω (20 is the temperature detector C30 that detects the temperature change at the inlet of the heat source water),
Or.

温度検出器110)+1lO)からの熱源水出入口温度
を入力信号とする制御器6j)3二より後述するような
開閉制御が行なわれ、かつ、1li6温再生器の加熱器
(21での加熱献制仰は温水管路(2■に設けられた温
度検出器(53つからの入力信号により開度調整される
燃料制御弁(3唱二より調整される。
Opening/closing control as described later is performed from the controller 6j) 32, which receives the temperature at the inlet and outlet of the heat source water from the temperature detector 110) + 1lO) as an input signal, and The control is adjusted by the fuel control valve (3) whose opening is adjusted by input signals from the temperature detector (53) installed in the hot water pipe (2).

このような構成の吸収ヒートポンプの蒸発器(7)シー
熱源水として太陽熱温水を供給する場合、この熱源水温
度が高い(例えば25℃以上)ときは。
When solar hot water is supplied as heat source water to the evaporator (7) of an absorption heat pump having such a configuration, when the temperature of this heat source water is high (for example, 25° C. or higher).

開閉弁面間Q51が閉止、開閉弁QI23+26)が開
放され。
The on-off valve Q51 is closed, and the on-off valve QI23+26) is opened.

高温再生器(1)で発生する冷媒ガスは冷媒管(1G、
低温再生器の加熱器(4)、開閉弁ti1を経て凝縮器
(5)に流入する一方、吸収液は高温内生器(1)およ
び低温町生器131で冷媒ガスが分離される、いわゆる
、二軍効用吸収ヒートポンプとして運転され、第2図の
臭化リテワムのデユーリング線図A−B−0−D−E−
F−Aのサイクルでみられるように設定11a度(図中
斜線で示す、例えば50℃削後)のl晶水等を収り吊子
ことができ、このような条件下での収り出し温水温度の
制御は高温再生器(1)での加熱祉制御等、従来から知
られている吸収ヒートポンプの運転制御が併用される。
The refrigerant gas generated in the high temperature regenerator (1) is passed through the refrigerant pipe (1G,
The absorbing liquid flows into the condenser (5) via the heater (4) of the low-temperature regenerator and the on-off valve ti1, while the refrigerant gas is separated from the absorption liquid in the high-temperature internal generator (1) and the low-temperature generator 131. , is operated as a dual-effect absorption heat pump, and the Dueling diagram of ritewam bromide shown in Fig. 2 A-B-0-D-E-
As seen in the F-A cycle, it is possible to store crystal water at a temperature of 11 degrees (indicated by diagonal lines in the figure, e.g. after cutting at 50 degrees Celsius), and it is difficult to collect it under such conditions. To control the hot water temperature, conventionally known operation control of an absorption heat pump, such as heating control in the high temperature regenerator (1), is used.

熱源水温度が低く(例えば25℃以下)なったときは、
蒸発器(7)での冷媒気化と循環tが減少し、吸収液の
濃度が濃くなり、低温再生器(3)の器内圧力も下がる
ためC二、上記した設定温度の温水等を収り吊子ことが
できなくなる。このようなときは。
When the heat source water temperature becomes low (for example, below 25℃),
The refrigerant vaporization and circulation in the evaporator (7) decrease, the concentration of the absorption liquid increases, and the internal pressure of the low-temperature regenerator (3) also decreases. You will not be able to use the hanger. At times like this.

熱源水の温度の低下ン温度検出器(列又はC(Olで検
知し、開閉弁f17)121R251を開放、開閉弁t
+a12り(ニジ0を閉止すると、高温再生器fllの
冷媒ガスは冷媒側路管+20) 。
Decrease in temperature of heat source water - Temperature detector (column or C (detected by Ol, open/close valve f17) 121R251 is opened, open/close valve t
+a12 (when Niji 0 is closed, the refrigerant gas in the high-temperature regenerator full flows through the refrigerant side pipe +20).

開閉弁r1nv経て凝縮器(5)に流入して凝縮器(5
)の圧カン尚め、熱源水温度が低くても設定温度の温水
全数り吊子ことができるようI:なり、吸収液は中間液
側1賂営(鳴、開閉弁(25)、低温熱交換器d41ケ
経て吸収器00)に流入し、吸収器(1111の稀吸収
液は吸収液ポンプ(13,低温M交換器11−11、開
閉弁1211乞経て高温円生器(1)に戻る循環(第2
図のA −8−0−D +7)サイクル)の−重効用吸
収ヒートボンブで運転および運転開側1が行なわれる。
It flows into the condenser (5) through the on-off valve r1nv.
), so that even if the heat source water temperature is low, the hot water at the set temperature can be fully pumped. The dilute absorption liquid in the absorber (1111) flows into the absorber (1111) through the exchanger (d41), and returns to the high-temperature generator (1) through the absorption liquid pump (13, low temperature M exchanger 11-11, on-off valve 1211). Circulation (second
The operation and operation opening side 1 are carried out in the heavy-effect absorption heat bomb of -A-8-0-D +7) cycle in the figure.

この上つぼニして5本発明では熱源水温度が高く。Above all, in the present invention, the temperature of the heat source water is high.

収り出し温水との温度差が一定温度以上のときは。When the temperature difference between the hot water and the hot water is more than a certain temperature.

、低副用生器と高温用止器とを作動させた二重効用ヒー
トポンプ運転によって効率良く設定温度の渦水乞取り吊
子一方、熱源水温jWが低く収り出し温水とのl昌度差
が一定温度以上のときは低温町生器の作m1乞休止し、
加熱温度rJ]q上げた二重効用ヒートポンプ運転によ
って設定温度の温水Z取り出すようl二し、熱源水の温
度の変動によって取り吊す温水の温度が大きく変動する
ことなく安定した温水等の供給ができるようにしている
By operating a dual-effect heat pump that operates a low secondary generator and a high-temperature stopper, the whirlpool water hanger efficiently maintains the set temperature.On the other hand, the heat source water temperature jW is kept low and the temperature difference between the temperature and the hot water is reduced. When the temperature is above a certain level, the production of low-temperature generators will be suspended.
By operating the double-effect heat pump with the heating temperature rJ]q raised, hot water Z at the set temperature is extracted, and a stable supply of hot water, etc. can be achieved without large fluctuations in the temperature of the hot water being drawn due to fluctuations in the temperature of the heat source water. That's what I do.

又、本発明の別の実施例として、熱源水V、地下戸 水や井7j(fx、ど、比較的安定した温度の熱源水が
使用できるときは、制1lll器によって開閉弁7切り
替えることにより、両温の温水と中程度の温水というよ
うな二つの温度領域の温水を、適宜、吸収ヒートポンプ
で製造できるものである。
In addition, as another embodiment of the present invention, when heat source water V, underground water, or well 7j (fx, etc.) can be used, the on-off valve 7 is switched by a controller when heat source water with a relatively stable temperature can be used. Hot water in two temperature ranges, such as double-temperature hot water and medium-temperature hot water, can be appropriately produced using an absorption heat pump.

すなわち、熱源水温度を例えば18℃とし、この熱源水
温度と取り出し温水温度との差が比較的小さい50℃程
度の温水を作るときは、二重効用ヒートポンプ運転とな
るよう(二重を開閉し、第6図の^−m−o−6−m−
p−^のようなサイクルヶもって図中に斜線で示すよう
な設定温jyの温水を製造する。父、熱源水温度と取り
出し温水温度との差が大きい70℃程度の温水2作ると
きは。
In other words, when the heat source water temperature is, for example, 18°C and the difference between this heat source water temperature and the hot water temperature taken out is relatively small, about 50°C, the temperature is set to 18°C, and the difference between the heat source water temperature and the hot water temperature taken out is relatively small, about 50°C. , ^-m-o-6-m- in Figure 6
After a cycle like p-^, hot water with a set temperature jy as shown by diagonal lines in the figure is produced. Father, when making hot water 2 at around 70 degrees Celsius, there is a large difference between the heat source water temperature and the hot water temperature taken out.

開閉弁を切替えて一重効用運転(第6図のサイクルA−
B−0−D−A)乞し、図中に二重斜線で示すようた設
定温度の温水を製造する。
Single-effect operation by switching the on-off valve (cycle A- in Figure 6)
B-0-D-A) Produce hot water at a set temperature as indicated by double hatching in the figure.

この場合において、取り出し温水温度の切替えは温水管
の出口に設けた温度検出器で行なうか又は、制碑器ン操
作して開閉弁の切替えン行なえば、適宜−重効用ヒート
ボンプ運転と二重効用ヒートポンプ運転の切り替えが行
なわれるものであり。
In this case, the temperature of the hot water taken out can be changed by using a temperature detector installed at the outlet of the hot water pipe, or by operating the control device and switching the on-off valve. The heat pump operation is switched.

簡単な構成でもって巾広い温度の熱源水を活用して安定
した温度の温水ン効率良く製造することができるもので
ある。
With a simple configuration, it is possible to efficiently produce hot water at a stable temperature by utilizing heat source water at a wide range of temperatures.

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

′第1図は本発明による吸収ヒートポンプの一実施例を
示す冷凍ザイクル図、第2図は本発明のヒートポンプの
一つの運転状態を説明するデユーリング線図、第3図は
同じく他の運転状態を説明するデユーリング線図である
。 1〜高温再生器、6〜低温再生器、5〜凝縮器、7〜蒸
発器、10〜吸収器、17.18%21゜22.25.
26〜開閉弁、29〜温水管路。 第1図
'Figure 1 is a refrigeration cycle diagram showing one embodiment of the absorption heat pump according to the present invention, Figure 2 is a Dueling diagram explaining one operating state of the heat pump of the present invention, and Figure 3 is a diagram showing another operating state. It is a Duering diagram for explanation. 1 - high temperature regenerator, 6 - low temperature regenerator, 5 - condenser, 7 - evaporator, 10 - absorber, 17.18% 21° 22.25.
26~opening/closing valve, 29~hot water pipe. Figure 1

Claims (1)

【特許請求の範囲】[Claims] (1)蒸発器、吸収器、凝縮器及び再生器で吸収冷凍サ
イクルを構成する吸収ヒートポンプにおいて、再生器を
高温再生器と、該高温再生器で発生した冷媒ガスヶ加熱
源とする低温再生器とから構成し、かつ、低温朽生器へ
の冷媒管と吸収液供給管とに切替弁を設けると共に、蒸
発器へ供給される熱源水と収り出し温水との温度差が一
定温度以上のときは低温病生器が作動を休止する一重効
用運転、同じく熱源水温度と取り出し温水との温度差が
一定温度以下のときは低温再生器と高温再生器が作動す
る二重効用運転をするように切替弁が切替えられること
を特徴とする吸収ヒートポンプ。
(1) In an absorption heat pump that configures an absorption refrigeration cycle with an evaporator, absorber, condenser, and regenerator, the regenerator is a high-temperature regenerator and a low-temperature regenerator that uses the refrigerant gas generated in the high-temperature regenerator as a heating source. and a switching valve is provided in the refrigerant pipe and the absorption liquid supply pipe to the low-temperature aging device, and when the temperature difference between the heat source water supplied to the evaporator and the discharged hot water is above a certain temperature. When the temperature difference between the heat source water temperature and the hot water taken out is below a certain temperature, the low temperature regenerator and the high temperature regenerator are activated. An absorption heat pump characterized by a switchable switching valve.
JP12959881A 1981-08-19 1981-08-19 Absorption heat pump Pending JPS5831264A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12959881A JPS5831264A (en) 1981-08-19 1981-08-19 Absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12959881A JPS5831264A (en) 1981-08-19 1981-08-19 Absorption heat pump

Publications (1)

Publication Number Publication Date
JPS5831264A true JPS5831264A (en) 1983-02-23

Family

ID=15013405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12959881A Pending JPS5831264A (en) 1981-08-19 1981-08-19 Absorption heat pump

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Country Link
JP (1) JPS5831264A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01134175A (en) * 1987-11-18 1989-05-26 Yazaki Corp Air-cooled absorption water cooler and heater
JPH05231739A (en) * 1991-03-14 1993-09-07 Tokyo Gas Co Ltd Absorption type hot and chilled water generator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01134175A (en) * 1987-11-18 1989-05-26 Yazaki Corp Air-cooled absorption water cooler and heater
JPH05231739A (en) * 1991-03-14 1993-09-07 Tokyo Gas Co Ltd Absorption type hot and chilled water generator

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