JPH065146B2 - Absorption heat pump device - Google Patents
Absorption heat pump deviceInfo
- Publication number
- JPH065146B2 JPH065146B2 JP15172084A JP15172084A JPH065146B2 JP H065146 B2 JPH065146 B2 JP H065146B2 JP 15172084 A JP15172084 A JP 15172084A JP 15172084 A JP15172084 A JP 15172084A JP H065146 B2 JPH065146 B2 JP H065146B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant liquid
- condenser
- evaporator
- heat pump
- amount
- 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
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 21
- 239000007788 liquid Substances 0.000 claims description 89
- 239000003507 refrigerant Substances 0.000 claims description 79
- 239000006096 absorbing agent Substances 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 10
- 239000012809 cooling fluid Substances 0.000 claims description 2
- 230000007423 decrease Effects 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 230000007257 malfunction Effects 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
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、発生器および凝縮器を蒸発器および吸収器よ
りも低温低圧で作動させ、吸収器において吸収液が冷媒
を吸収する際に発生する熱により被加熱流体を熱源流体
の温度以上に昇温して取出す吸収ヒートポンプ装置(以
下、この種の吸収ヒートポンプ装置という)に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention operates a generator and a condenser at a temperature lower than that of an evaporator and an absorber, and when the absorbing liquid absorbs the refrigerant in the absorber. The present invention relates to an absorption heat pump device (hereinafter, referred to as an absorption heat pump device of this kind) that heats a fluid to be heated to a temperature equal to or higher than a temperature of a heat source fluid and extracts the heated fluid.
(ロ)従来の技術 この種の吸収ヒートポンプ装置は、凝縮器を蒸発器より
も低温で作動させるため、凝縮器から蒸発器へ送られる
冷媒液の量が急激に変動すると蒸発器内の冷媒液温およ
び圧力が急激に変化し、吸収器から取出される被加熱流
体の熱量も大きく変動して不安定になる。それ故、この
種の吸収ヒートポンプ装置においては、凝縮器から蒸発
器へ送られる冷媒液の量を調節して吸収器から取出され
る熱量を安定化させる必要がある。(B) Conventional technology Since this type of absorption heat pump device operates the condenser at a temperature lower than that of the evaporator, if the amount of refrigerant liquid sent from the condenser to the evaporator fluctuates rapidly, the refrigerant liquid in the evaporator The temperature and pressure change abruptly, and the heat quantity of the heated fluid taken out of the absorber also fluctuates greatly and becomes unstable. Therefore, in this type of absorption heat pump device, it is necessary to stabilize the amount of heat taken out from the absorber by adjusting the amount of the refrigerant liquid sent from the condenser to the evaporator.
そして、凝縮器から蒸発器へ送られる冷媒液の量を調節
する従来の技術としては、凝縮器の冷媒液溜めに備えた
液面検出器の信号により制御器を介して凝縮器から蒸発
器へ至る冷媒液の管の途中に設けた制御弁の開度を制御
する手段(例えば、特開昭58−136956号公報)
がある。Then, as a conventional technique for adjusting the amount of the refrigerant liquid sent from the condenser to the evaporator, as a signal from the liquid level detector provided in the refrigerant liquid reservoir of the condenser, the condenser to the evaporator is transmitted through the controller. Means for controlling the opening degree of a control valve provided in the middle of the refrigerant liquid pipe (for example, Japanese Patent Laid-Open No. 58-136956)
There is.
(ハ)発明が解決しようとする問題点 上記の従来技術においては、冷媒液中に混入した吸収液
や不純物などにより、液面検出器のセンサー部が汚され
てその性能が悪くなり、制御動作が不正確になりやすい
欠点をもち、また、精密に製作されたモーターや空気圧
のなどの力によって高い精度で作動させる高価な制御
弁、高価な制御器が必要であり、コストも高くなる欠点
を有している。(C) Problems to be Solved by the Invention In the above-mentioned conventional techniques, the sensor part of the liquid level detector is polluted by the absorbing liquid and impurities mixed in the refrigerant liquid, and the performance thereof deteriorates, and the control operation is Has the drawback that it tends to be inaccurate, and that it requires an expensive control valve and an expensive controller that operate with high precision by means of a precisely manufactured motor and air pressure. Have
本発明は、従来技術のこれら問題点に鑑み、簡単な構造
でほぼ正確な制御動作が行なわれて凝縮器から蒸発器へ
の冷媒液の流量を凝縮器内の冷媒液量に応じて調節する
ことのできる安価な冷媒液の流量制御器を備えたこの種
の吸収ヒートポンプの提供を目的としたものである。In view of these problems of the prior art, the present invention adjusts the flow rate of the refrigerant liquid from the condenser to the evaporator according to the amount of the refrigerant liquid in the condenser by performing a substantially accurate control operation with a simple structure. It is an object of the present invention to provide an absorption heat pump of this kind provided with a low-cost refrigerant liquid flow controller that can be used.
(ニ)問題点を解決するための手段 本発明は、この種の吸収ヒートポンプにおいて、上記問
題点を解決する手段として、凝縮器の冷媒液溜めに備え
た浮子の上下動に連動して蒸発器側への冷媒液の出口面
積を増減する弁機構の設けられた流量制御器を凝縮器の
冷媒液溜めの冷媒液中に配備する構成とし、かつ、浮子
に取付けたアームと弁体とを連結しているステムを制御
器の弁箱に取付けたスリーブ内壁に対して下方へ末広に
形成したものである。(D) Means for Solving the Problems The present invention relates to an absorption heat pump of this type, and as means for solving the above problems, the evaporator is interlocked with the vertical movement of the float provided in the refrigerant liquid reservoir of the condenser. The flow rate controller with a valve mechanism that increases or decreases the outlet area of the refrigerant liquid to the side is arranged in the refrigerant liquid in the refrigerant liquid reservoir of the condenser, and the arm attached to the float and the valve body are connected. The stem is formed divergent downward with respect to the inner wall of the sleeve attached to the valve box of the controller.
(ホ)作用 本発明による手段においては、凝縮器内の冷媒液量が増
え始めたとき、浮子と連動する弁体が蒸発器側への冷媒
液の出口面積を広げるよう動作すると共に浮子と連動す
るステムが凝縮器内の冷媒液中に配備した流量制御器の
弁箱に取付けたスリーブ内壁とステムとの間隙を狭める
よう動作して、凝縮器から蒸発器へ送られる量を次第に
増やすと共に凝縮器へ還流される冷媒液の量を次第に減
らすように作用する。また、凝縮器内の冷媒液量が逆に
減り始めたとき、浮子と連動する弁体およびステムが逆
に動作して、凝縮器から蒸発器へ送られる冷媒液の量を
次第に減らすと共に凝縮器へ還流される冷媒液の量を次
第に増やすように作用する。本発明による手段はこのよ
うな作用(働き)をもつものであるから、凝縮器から蒸
発器への冷媒液の流量を凝縮器内の冷媒液量に応じて確
実に調節することができ、蒸発器に送られる冷媒液量の
急激な変動を防ぐことができる。(E) Action In the means according to the present invention, when the amount of the refrigerant liquid in the condenser starts to increase, the valve body interlocking with the float operates to widen the outlet area of the refrigerant liquid to the evaporator side and interlocks with the float. The stem operates to narrow the gap between the inner wall of the sleeve attached to the valve box of the flow controller deployed in the refrigerant liquid in the condenser and the stem, gradually increasing the amount sent from the condenser to the evaporator and condensing. It acts to gradually reduce the amount of refrigerant liquid returned to the vessel. When the amount of refrigerant liquid in the condenser begins to decrease, the valve body and the stem that interlock with the float operate in reverse, gradually decreasing the amount of refrigerant liquid sent from the condenser to the evaporator, and It works so as to gradually increase the amount of the refrigerant liquid that is returned to the. Since the means according to the present invention has such an action, it is possible to reliably adjust the flow rate of the refrigerant liquid from the condenser to the evaporator in accordance with the amount of the refrigerant liquid in the condenser, and It is possible to prevent a rapid change in the amount of the refrigerant liquid sent to the container.
また、本発明による手段においては、浮子に連動する弁
機構を有する流量制御器が凝縮器内の冷媒液中に配備さ
れた簡単な構造のものであるから、高精度で動作する高
価な制御弁や制御器を必要とする従来の手段にくらべ、
故障が少なく、かつ、コストも安い。Further, in the means according to the present invention, since the flow rate controller having the valve mechanism interlocked with the float has a simple structure provided in the refrigerant liquid in the condenser, an expensive control valve that operates with high accuracy is provided. And conventional means that require a controller,
There are few breakdowns and the cost is low.
(ヘ)実施例 第1図は本発明によるこの種の吸収ヒートポンプ装置の
一実施例を示した概略構成説明図であり、また、第2図
は本発明吸収ヒートポンプ装置の一部を切欠して拡大し
た説明図で、第1図に示した構成機器と同じものには同
一の番号を付している。(F) Embodiment FIG. 1 is a schematic configuration explanatory view showing an embodiment of an absorption heat pump device of this kind according to the present invention, and FIG. 2 is a partial cutaway view of the absorption heat pump device of the present invention. In the enlarged explanatory view, the same components as those shown in FIG. 1 are designated by the same reference numerals.
第1図において、(1)は発生器、(2)は凝縮器、(3)は蒸
発器、(4)は吸収器、(5)は溶液熱交換器、(6)は吸収液
用のポンプ、(7)、(8)は冷媒液用のポンプで、これら機
器は冷媒蒸気の流れるダクト(9)、(10)、冷媒液の流れ
る管(11)、(12)、(13)、冷媒液の還流する管(14)、(1
5)、吸収液の流れる管(16)、(17)、(18)および吸収液の
流下する管(19)、(20)により接続されて従来のこの種の
吸収ヒートポンプ(例えば特開昭58−69372号公
報)と同様の冷媒(水)および吸収液(臭化リチウム水
溶液)の循環路を構成している。なお、(21)は溶液熱交
換器(5)に内蔵した熱交換用コイルである。In FIG. 1, (1) is a generator, (2) is a condenser, (3) is an evaporator, (4) is an absorber, (5) is a solution heat exchanger, and (6) is for absorbing liquid. Pumps, (7), (8) are pumps for refrigerant liquid, these devices are ducts (9), (10) through which the refrigerant vapor flows, pipes (11), (12), (13) through which the refrigerant liquid flows, Refrigerant liquid return pipe (14), (1
5), absorption liquid flow pipes (16), (17), (18) and absorption liquid flow-down pipes (19), (20), which are connected to each other to obtain a conventional absorption heat pump of this type (for example, JP-A-58). -69372) and a circulation path for the refrigerant (water) and the absorbing liquid (lithium bromide aqueous solution) similar to Incidentally, (21) is a heat exchange coil built in the solution heat exchanger (5).
(22)は発生器(1)に内蔵した加熱器、(23)は凝縮器(2)に
内蔵した冷却器、(24)は蒸発器(3)に内蔵した給熱器、
(25)は吸収器(4)に内蔵した被加熱器であり、(26)、(2
7)は加熱器(22)と接続した排温水や廃蒸気などの熱源流
体を流す管、(28)、(29)は冷却器(23)と接続した冷却水
や冷却用空気などの冷却流体を流す管、(30)、(31)は給
熱器(24)と接続した排温水や廃蒸気などの熱源流体を流
す管、(32)、(33)は被加熱器(25)と接続した温水や蒸気
などの被加熱流体を流す管である。(22) is a heater built in the generator (1), (23) is a cooler built in the condenser (2), (24) is a heat source built in the evaporator (3),
(25) is a device to be heated built in the absorber (4), and (26), (2
(7) is a pipe for flowing a heat source fluid such as waste hot water or waste steam connected to the heater (22), and (28) and (29) are cooling fluid such as cooling water and cooling air connected to the cooler (23). , (30) and (31) are pipes for flowing heat source fluid such as waste hot water and waste steam connected to the heat supply device (24), and (32) and (33) are connected to the heater (25). It is a pipe through which heated fluid such as hot water or steam flows.
(34)、(35)はそれぞれ発生器(1)、吸収器(4)内に備えた
吸収液の散布器、(36)は蒸発器(3)内に備えた冷媒液の
散布器、(37)、(38)はそれぞれ発生器(1)、吸収器(4)の
溶液溜め、(39)、(40)はそれぞれ凝縮器(2)、蒸発器(3)
の冷媒液溜め、(41)、(42)はエリミネーターである。(34) and (35) are respectively a generator (1), a sprayer of the absorbing liquid provided in the absorber (4), (36) is a sprayer of the refrigerant liquid provided in the evaporator (3), 37) and (38) are the reservoirs of the generator (1) and the absorber (4), and (39) and (40) are the condenser (2) and evaporator (3), respectively.
And (41) and (42) are eliminators.
(SW1)は溶液溜め(37)に備えた液面スイッチ、(S
W2)、(SW3)はそれぞれ冷媒液溜め(39)、(40)に
備えた液面スイッチで、これらスイッチによりポンプ
(6)、(7)、(8)がそれぞれ発停制御されて液面が上下限
レベル間に保たれるようになっている。(SW 1 ) is a liquid level switch provided in the solution reservoir (37), (S 1
W 2 ) and (SW 3 ) are liquid level switches provided in the refrigerant liquid reservoirs (39) and (40), respectively.
(6), (7), and (8) are controlled to start and stop, respectively, so that the liquid level is maintained between the upper and lower limit levels.
(43)は開閉弁(V)を有する冷媒液のブロー用の管で、
運転を停止するに先立って開閉弁(V)を開き、冷媒液
溜め(40)内の冷媒液をポンプ(8)により液面の下限レベ
ルまでブローするようにしている。なお、(44)、(45)は
それぞれ管(17)、(20)に備えたダンパーである。(43) is a pipe for blowing the refrigerant liquid having an on-off valve (V),
The on-off valve (V) is opened before the operation is stopped, and the refrigerant liquid in the refrigerant liquid reservoir (40) is blown to the lower limit level of the liquid level by the pump (8). Incidentally, (44) and (45) are dampers provided in the pipes (17) and (20), respectively.
そして、(46)は冷媒液溜め(39)に備えた浮子であり、(4
7)は浮子(46)と連動する弁機構の設けられた流量制御器
で、この流量制御器は冷媒液溜め(39)の冷媒液中に配備
されている。また、流量制御器(47)の弁機構は、冷媒液
の出口(48)の広さを調節する弁体(49)、この弁体と浮子
(46)に取付けた回転用のアーム(50)とを連結するステム
(51)、流量制御器(47)の弁箱(52)に取付けたスリーブ(5
3)等で構成されており、かつ、ステム(51)はスリーブ(5
3)内壁に対して下方へ末広に形成されている(第2図参
照)。かつまた、(54)は流量制御器(47)における冷媒液
の入口である。なお、第2図において、(55)は弁箱(52)
に固着した支持体、(56)はアーム(50)が回転できるよう
にこのアームと支持体(55)とを支えている軸、(57)はア
ーム(50)とステム(51)とを連接している軸である。And, (46) is a float provided in the refrigerant liquid reservoir (39),
Reference numeral 7) is a flow rate controller provided with a valve mechanism interlocking with the float (46), and this flow rate controller is arranged in the refrigerant liquid in the refrigerant liquid reservoir (39). Further, the valve mechanism of the flow rate controller (47) includes a valve body (49) for adjusting the width of the refrigerant liquid outlet (48), the valve body and the float.
Stem that connects with the rotating arm (50) attached to (46)
(51), sleeve (5) attached to the valve box (52) of the flow controller (47)
3) etc., and the stem (51) has a sleeve (5
3) It is divergent downward from the inner wall (see Fig. 2). Moreover, (54) is an inlet of the refrigerant liquid in the flow rate controller (47). In Fig. 2, (55) is the valve box (52).
The support fixed to the, (56) the shaft supporting the arm (50) so that the arm (50) can rotate, and (57) connecting the arm (50) and the stem (51). It is the axis.
次に、このように構成された吸収ヒートポンプ装置(以
下、本機という)の動作と併せて本機に備えた流量制御
器の動作の一例を説明する。Next, an example of the operation of the flow rate controller provided in this machine will be described together with the operation of the absorption heat pump device (hereinafter referred to as this machine) configured as described above.
本機においては、例えば化学プラントその他の設備(図
示せず)からの約90℃の廃蒸気が発生器(1)および蒸
発器(3)に供給されると共に約26℃の冷却水が凝縮器
(2)に供給され、吸収器(4)内で吸収液が冷媒蒸気を吸収
する際に発生する熱により被加熱器(25)内の水が約13
3℃に昇温されて負荷側(図示せず)へ供給される。な
お、この運転例の定常時、発生器(1)および凝縮器(2)の
気相部における温度、圧力はおよそ35℃、42mmHg
となり、また、蒸発器(3)および吸収器(4)の気相部にお
ける温度、圧力はおよそ85℃、434mmHgとなる。
そして、運転中に負荷や廃蒸気の熱エネルギーあるいは
冷却水の熱エネルギーが変化した場合、冷媒蒸気の発生
量や凝縮量あるいは吸収液の冷媒吸収量などが変化する
と共に凝縮器(2)や蒸発器(3)などの機器内の圧力、温度
も変化し、また、これら機器間の圧力差も変化する。こ
のため、ポンプ(7)により凝縮器(2)から蒸発器(3)へ送
られる冷媒液の量が変化し、また、凝縮器(2)の冷媒液
溜め(39)内の冷媒液量が変化する。In this machine, for example, waste steam of about 90 ° C from a chemical plant or other equipment (not shown) is supplied to the generator (1) and the evaporator (3), and cooling water of about 26 ° C is condensed.
About 13% of the water in the heated device (25) is supplied to the (2) and the heat generated when the absorbing liquid absorbs the refrigerant vapor in the absorber (4).
The temperature is raised to 3 ° C. and supplied to the load side (not shown). In the steady state of this operation example, the temperature and pressure in the gas phase part of the generator (1) and the condenser (2) are approximately 35 ° C and 42 mmHg.
Further, the temperature and pressure in the vapor phase part of the evaporator (3) and the absorber (4) are about 85 ° C. and 434 mmHg.
If the load, the heat energy of the waste steam, or the heat energy of the cooling water changes during operation, the amount of refrigerant vapor generated or condensed, or the amount of refrigerant absorbed by the absorbing liquid changes, and the condenser (2) or evaporation The pressure and temperature inside the device such as the device (3) also change, and the pressure difference between these devices also changes. Therefore, the amount of the refrigerant liquid sent from the condenser (2) to the evaporator (3) is changed by the pump (7), and the amount of the refrigerant liquid in the refrigerant liquid reservoir (39) of the condenser (2) is changed. Change.
このように冷媒液溜め(39)内の冷媒液量が変化する場合
における流量制御器(47)の動作について第2図を参照し
つつ説明する。The operation of the flow rate controller (47) when the amount of the refrigerant liquid in the refrigerant liquid reservoir (39) changes in this way will be described with reference to FIG.
冷媒液溜め(39)内の冷媒液量が減り始めた場合、液面が
低下し始め、浮子(46)が下方へ動き、アーム(50)が反時
計方向に回転する。そして、ステム(51)が下方へ動くと
共に弁体(49)が弁箱(52)の出口(48)を閉塞する方向に降
下し、スリーブ(53)内壁とステム(51)との隙間が広がる
と共に出口(48)が狭くなる。このため、ポンプ(7)によ
り入口(54)を介して弁箱(52)内に送られた冷媒液のう
ち、出口(48)から流出して蒸発器(3)側へ送られる冷媒
液の分量が減り、スリーブ(53)内壁とステム(51)との隙
間を介して冷媒液溜め(39)へ戻される冷媒液の分量が増
す。それ故、冷媒液溜め(39)内の冷媒液量の急激な減少
を防ぐことができ、従来のこの種の吸収ヒートポンプ装
置のようにポンプ(7)を頻繁に発停する必要がなく、ま
た、凝縮器(2)から蒸発器(3)へ送られる冷媒液の量が、
ポンプ(7)を頻繁に発停制御する従来のこの種の吸収ヒ
ートポンプ装置のように、大きく変動することもない。When the amount of the refrigerant liquid in the refrigerant liquid reservoir (39) starts to decrease, the liquid surface starts to decrease, the float (46) moves downward, and the arm (50) rotates counterclockwise. Then, as the stem (51) moves downward, the valve body (49) descends in the direction of closing the outlet (48) of the valve box (52), and the gap between the inner wall of the sleeve (53) and the stem (51) widens. Along with that, the exit (48) becomes narrower. Therefore, of the refrigerant liquid sent to the valve box (52) through the inlet (54) by the pump (7), the refrigerant liquid that flows out from the outlet (48) and is sent to the evaporator (3) side The amount is reduced, and the amount of the refrigerant liquid returned to the refrigerant liquid reservoir (39) through the gap between the inner wall of the sleeve (53) and the stem (51) is increased. Therefore, it is possible to prevent a sharp decrease in the amount of the refrigerant liquid in the refrigerant liquid reservoir (39), it is not necessary to frequently start and stop the pump (7) unlike the conventional absorption heat pump device of this type, and , The amount of refrigerant liquid sent from the condenser (2) to the evaporator (3),
Unlike the conventional absorption heat pump device of this type in which the pump (7) is frequently started and stopped, it does not fluctuate significantly.
一方、冷媒液溜め(39)内の冷媒液量が増え始めた場合に
は、浮子(46)、アーム(50)、ステム(51)、弁体(49)が冷
媒液量の減り始めた場合と逆に動作し、冷媒液溜め(39)
内の冷媒液量の急激な増大を防止してポンプ(7)を頻繁
に発停させないで済むようにしている。On the other hand, when the amount of refrigerant liquid in the refrigerant liquid reservoir (39) begins to increase, when the amount of refrigerant liquid in the float (46), arm (50), stem (51), valve body (49) begins to decrease. Reverse operation, refrigerant sump (39)
The sudden increase in the amount of refrigerant liquid in the inside is prevented so that the pump (7) is not frequently started and stopped.
(ト)発明の効果 以上のように、本発明によるこの種の吸収ヒートポンプ
装置においては、凝縮器の冷媒液溜めに備えた浮子と連
動するステムを下方へ末広に形成してこのステムの上下
動により冷媒液の冷媒液溜めへの戻し口となるスリーブ
内壁とステムとの隙間の広さを調節すると共に冷媒液の
流出口の広さを調節する簡単な構造の流量制御器を凝縮
器の冷媒液溜めに配備しているので、高精度で動作する
高価な制御弁、制御器、液面検出器を備えた従来のこの
種の吸収ヒートポンプ装置にくらべ、故障や誤動作のお
それが少なく、凝縮器内の冷媒液量に応じて蒸発器側へ
の冷媒液の送り量をほぼ確実に調節することができ、蒸
発器側へ送られる冷媒液量の急激な変動を安いコストで
防ぎ得る。(G) Effect of the Invention As described above, in the absorption heat pump device of this type according to the present invention, the stem interlocking with the float provided in the refrigerant liquid reservoir of the condenser is formed downwardly and divergently to move the stem vertically. Adjusts the size of the gap between the stem and the inner wall of the sleeve, which is the return port of the refrigerant liquid to the refrigerant liquid reservoir, and adjusts the width of the outlet of the refrigerant liquid. Since it is installed in the liquid reservoir, there is less risk of malfunction or malfunction than the conventional absorption heat pump device of this type equipped with an expensive control valve, controller and liquid level detector that operate with high accuracy, and a condenser The amount of the refrigerant liquid sent to the evaporator side can be adjusted almost surely according to the amount of the refrigerant liquid inside, and a sudden change in the amount of the refrigerant liquid sent to the evaporator side can be prevented at a low cost.
第1図は本発明によるこの種の吸収ヒートポンプ装置の
一実施例を示した概略構成説明図、第2図は本発明によ
るこの種の吸収ヒートポンプ装置に用いた流量制御器の
配備部分の拡大説明図である。 (1)…発生器、(2)…凝縮器、(3)…蒸発器、(4)…吸収
器、(7)…ポンプ、(11)、(12)、(13)…管、(39)…冷媒
液溜め、(46)…浮子、(47)…流量制御器、(48)…出口、
(49)…弁体、(50)…アーム、(51)…ステム、(52)…弁
箱、(53)…スリーブ、(54)…出口、(56)、(57)…軸。FIG. 1 is a schematic configuration explanatory view showing an embodiment of an absorption heat pump device of this type according to the present invention, and FIG. 2 is an enlarged description of a portion where a flow rate controller used in the absorption heat pump device of this type according to the present invention is arranged. It is a figure. (1) ... Generator, (2) ... Condenser, (3) ... Evaporator, (4) ... Absorber, (7) ... Pump, (11), (12), (13) ... Pipe, (39 ) ... Refrigerant reservoir, (46) ... Float, (47) ... Flow controller, (48) ... Outlet,
(49) ... valve body, (50) ... arm, (51) ... stem, (52) ... valve box, (53) ... sleeve, (54) ... outlet, (56), (57) ... shaft.
Claims (1)
蒸発器に熱源流体を供給して吸収器から熱源流体温度以
上の被加熱流体を取出すように発生器、凝縮器、蒸発
器、吸収器などの機器を配管接続した吸収ヒートポンプ
において、凝縮器の冷媒液溜めからポンプにより吐出さ
れる冷媒液の流入口と、蒸発器側への冷媒液の流出口
と、凝縮器の冷媒液溜めに備えた浮子に連動して蒸発器
側への冷媒液の流出口の広さを調節する弁機構とが設け
られ、かつ、浮子に取付けた回転用のアームと弁体とを
連結したステムが弁箱に取付けたスリーブ内壁に対して
下方へ末広に形成されている冷媒液の流量制御器を凝縮
器の冷媒液溜めの冷媒液中に配備したことを特徴とする
吸収ヒートポンプ装置。1. A generator, a condenser, an evaporator, and an absorber for supplying a heat source fluid to a generator and an evaporator while flowing a cooling fluid to the condenser to extract a heated fluid having a temperature higher than the heat source fluid temperature from the absorber. In an absorption heat pump in which equipment such as a condenser is connected by piping, the inlet of the refrigerant liquid discharged from the refrigerant liquid reservoir of the condenser by the pump, the outlet of the refrigerant liquid to the evaporator side, and the refrigerant liquid reservoir of the condenser A valve mechanism that adjusts the width of the outlet of the refrigerant liquid to the evaporator side is provided in conjunction with the provided float, and the stem that connects the rotating arm attached to the float and the valve body is a valve. An absorption heat pump device, characterized in that a flow controller for a refrigerant liquid, which is formed so as to be divergent downward with respect to an inner wall of a sleeve attached to a box, is arranged in the refrigerant liquid in a refrigerant liquid reservoir of a condenser.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15172084A JPH065146B2 (en) | 1984-07-20 | 1984-07-20 | Absorption heat pump device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15172084A JPH065146B2 (en) | 1984-07-20 | 1984-07-20 | Absorption heat pump device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6129663A JPS6129663A (en) | 1986-02-10 |
| JPH065146B2 true JPH065146B2 (en) | 1994-01-19 |
Family
ID=15524808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15172084A Expired - Lifetime JPH065146B2 (en) | 1984-07-20 | 1984-07-20 | Absorption heat pump device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH065146B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4852331B2 (en) * | 2006-03-17 | 2012-01-11 | 株式会社荏原製作所 | Absorption heat pump device and operation method thereof |
-
1984
- 1984-07-20 JP JP15172084A patent/JPH065146B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6129663A (en) | 1986-02-10 |
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