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JP3244087B2 - Heat pump for mixed media - Google Patents
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JP3244087B2 - Heat pump for mixed media - Google Patents

Heat pump for mixed media

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Publication number
JP3244087B2
JP3244087B2 JP07471592A JP7471592A JP3244087B2 JP 3244087 B2 JP3244087 B2 JP 3244087B2 JP 07471592 A JP07471592 A JP 07471592A JP 7471592 A JP7471592 A JP 7471592A JP 3244087 B2 JP3244087 B2 JP 3244087B2
Authority
JP
Japan
Prior art keywords
condenser
heat medium
heat
liquid
absorber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP07471592A
Other languages
Japanese (ja)
Other versions
JPH05280813A (en
Inventor
博之 住友
起男 山崎
章 堀口
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.)
Hisaka Works Ltd
Original Assignee
Hisaka Works 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 Hisaka Works Ltd filed Critical Hisaka Works Ltd
Priority to JP07471592A priority Critical patent/JP3244087B2/en
Publication of JPH05280813A publication Critical patent/JPH05280813A/en
Application granted granted Critical
Publication of JP3244087B2 publication Critical patent/JP3244087B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、熱媒体の相変化を利
用し、低温側から汲み上げた熱を高温側で利用する目的
で使用されるヒートポンプに関し、熱媒体として二成分
系の混合媒体を使用する場合の性能向上を図るものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat pump which uses a phase change of a heat medium and uses heat pumped from a low temperature side at a high temperature side. It is intended to improve the performance when used.

【0002】[0002]

【従来の技術】ヒートポンプは、図3に示すように、蒸
発器(2)、圧縮機(4)、凝縮器(6)、膨張弁
(8)を直列に接続して閉ループ(10)を構成させ、こ
の閉ループ(10)内で熱媒体を循環させると、熱媒体は
まず蒸発器(2)で外部から熱を吸収して蒸発し、発生
した蒸気は圧縮機(4)で圧縮されて昇温・昇圧し、凝
縮器(6)でその熱を外部に放出し、凝縮して液相とな
った熱媒体は、膨張弁(8)で絞り膨張したうえで蒸発
器(2)に戻され、これによりサイクルを終える。
2. Description of the Related Art As shown in FIG. 3, a heat pump comprises an evaporator (2), a compressor (4), a condenser (6), and an expansion valve (8) connected in series to form a closed loop (10). When the heat medium is circulated in the closed loop (10), the heat medium first evaporates by absorbing heat from the outside in the evaporator (2), and the generated steam is compressed by the compressor (4) to rise. The temperature and pressure are increased, the heat is released to the outside in the condenser (6), and the heat medium condensed into a liquid phase is throttled and expanded by the expansion valve (8) and returned to the evaporator (2). This ends the cycle.

【0003】ところで、このようなヒートポンプ等の熱
サイクルでは、効率の向上のため熱媒体に非共沸の混合
媒体を用いてローレンツサイクルを構成させることがあ
る。図4は最も簡単な二成分の液体−蒸気系の温度−組
成の関係を横軸に低沸成分のモル分率をとって示したも
のである。GとLは単一相で、それぞれ気相と液相、L
+Gの領域は液体と蒸気が共存する二相領域である。も
し低沸成分の60モル%(モル分率=0.60)の液体混合物
の温度を、定圧下で上昇させたとすると、この系の変化
は直線ab'cd"e に沿って考えることができる。低温では
液相のみが存在するが、b'点で蒸気相が現われる。この
蒸気相の組成はb"点で与えられ、2つの共役相は図上の
平衡連結線b"b'で結ばれている。さらに温度を上げる
と、もっと多くの蒸気が生成するが、その場合、蒸気中
の低沸成分の濃度が高いので、液相ではこの成分が相対
的に減少し、液体の組成はb'c'd'に沿って変化し、一
方、蒸気の組成はb"c"d"に沿って変化する。温度t℃で
は、二相領域にある系の全組成はc点で表されるが、蒸
気組成、液体組成はそれぞれc点を通る平衡連結線の両
端、c"点とc'点で与えられる。二相の相対的な量は、物
理学のてこの原理から求められる。すなわち、蒸気と液
体のモル数の比はcc'と c"c の長さの比で表される。さ
らに温度を上げるとますます蒸気が生成し、d”点にな
ると液相はほとんどなくなり、これ以上温度が高くなる
と、液相が消えて蒸気相(d"点)のみが残る。
In such a heat cycle of a heat pump or the like, a Lorentz cycle may be constituted by using a non-azeotropic mixed medium as a heat medium in order to improve efficiency. FIG. 4 shows the relationship between the temperature and the composition of the simplest two-component liquid-vapor system in terms of the mole fraction of low boiling components on the horizontal axis. G and L are single phases, gas phase and liquid phase, L
The region of + G is a two-phase region where liquid and vapor coexist. If the temperature of a liquid mixture of 60 mol% (mol fraction = 0.60) of the low boiling components is increased under constant pressure, the change in this system can be considered along a straight line ab'cd "e. Has only a liquid phase, but a vapor phase appears at point b '. The composition of this vapor phase is given at point b ", and the two conjugate phases are connected by the equilibrium connection line b"b' in the figure. If the temperature is further increased, more vapor is generated, in which case the concentration of low-boiling components in the vapor is high, so that this component is relatively reduced in the liquid phase and the composition of the liquid is b ' varies along c'd ', while the composition of the vapor varies along b "c" d ". At the temperature t ° C., the total composition of the system in the two-phase region is represented by the point c, while the vapor composition and the liquid composition are respectively given at both ends of the equilibrium connection line passing the point c, the points c ″ and c ′. The relative amounts of the two phases can be determined from the principle of leverage in physics: the ratio of the moles of vapor to liquid is expressed as the ratio of the length of cc 'to c "c. When the temperature is further increased, more and more steam is generated, and at the point d ", almost no liquid phase is left. At a higher temperature, the liquid phase disappears and only the vapor phase (point d") remains.

【0004】[0004]

【発明が解決しようとする課題】凝縮器出口の熱媒体の
気相では低沸成分の濃度が系内で最も高く、凝縮伝熱面
付近にも低沸成分のガスが滞留する。このため、低沸成
分は凝縮器に対し物質移動および熱移動を妨げる不凝縮
ガスと同じような存在となり、伝熱性能を低下させる。
In the gas phase of the heat medium at the outlet of the condenser, the concentration of the low-boiling component is the highest in the system, and the low-boiling component gas also stays near the condensation heat transfer surface. For this reason, low-boiling components are present in the same manner as non-condensable gas that hinders mass transfer and heat transfer to the condenser, and reduce the heat transfer performance.

【0005】そこで、この発明の課題は、二成分系の混
合媒体を熱媒体として使用するヒートポンプにおいて、
凝縮器における未凝縮の低沸成分ガスの濃度を下げ、不
凝縮ガスを排除することと同じ効果を上げることにあ
る。
Therefore, an object of the present invention is to provide a heat pump using a two-component mixed medium as a heat medium.
The purpose of the present invention is to reduce the concentration of uncondensed low-boiling gas in the condenser and to achieve the same effect as eliminating non-condensable gas.

【0006】[0006]

【課題を解決するための手段】この発明は、凝縮器の熱
媒体出口側に吸収器を設け、蒸発器の熱媒体出口側の蒸
発残液に凝縮器出口付近の未凝縮ガスを吸収させること
により、課題を解決した。
According to the present invention, an absorber is provided on a heat medium outlet side of a condenser, and uncondensed gas in the vicinity of the condenser outlet is absorbed by an evaporation residue on the heat medium outlet side of the evaporator. Solved the problem.

【0007】[0007]

【課題を解決するための手段】 この発明は、蒸発器
と、圧縮機と、凝縮器と、膨張弁を直列に接続して閉ル
ープを構成させ、この閉ループ内で熱媒体を循環させる
ようにした、二成分系の混合媒体を熱媒体として使用す
るヒートポンプにおいて、凝縮器の熱媒体出口側に吸収
器を設け、蒸発器の熱媒体出口側の蒸発残液を前記吸収
器を介して膨張弁上流側の閉ループに導くことにより、
前記吸収器において前記蒸発残液に凝縮器出口付近の未
凝縮ガスを吸収させることにより、課題を解決した。
Means for Solving the Problems According to the present invention, an evaporator, a compressor, a condenser, and an expansion valve are connected in series to form a closed loop, and a heat medium is circulated in the closed loop. In a heat pump using a two-component mixed medium as a heat medium, an absorber is provided on the heat medium outlet side of the condenser, and the evaporation residue on the heat medium outlet side of the evaporator is upstream of the expansion valve via the absorber. By leading to the closed loop on the side
The problem was solved by allowing the unreacted gas in the vicinity of the outlet of the condenser to be absorbed by the residual liquid in the absorber.

【0008】このようにして低濃度低沸点媒体液に未凝
縮低沸成分ガスが吸収される結果、凝縮器出口付近にお
ける未凝縮低沸成分濃度が下がるので、物質移動および
熱移動が容易になり凝縮器伝熱性能が向上する。
As a result of the absorption of the uncondensed low-boiling component gas in the low-concentration low-boiling-point medium liquid in this manner, the concentration of the uncondensed low-boiling component near the outlet of the condenser decreases, so that mass transfer and heat transfer are facilitated. The condenser heat transfer performance is improved.

【0009】また、吸収器における冷却作用は上述のよ
うに吸収効果を高めることのみならず、液温(飽和温
度)を下げ、それに伴って圧力を低下させるはたらきを
する。したがって、凝縮圧力を下げることによる圧縮機
動力の軽減が可能となる。
Further, the cooling action in the absorber not only enhances the absorption effect as described above, but also lowers the liquid temperature (saturation temperature) and thereby lowers the pressure. Therefore, the compressor power can be reduced by lowering the condensing pressure.

【0010】[0010]

【実施例】図1に示すように、熱媒体通路(14a)と冷
却水通路(14b)を具備した一種の熱交換器である吸収
器(14)を設け、蒸発器(2)の熱媒体出口側に設けた
ミストセパレータ(18)の液相を、液戻り配管(20)で
吸収器(14)の熱媒体通路(14a)に接続する。液戻り
配管(20)は途中にポンプ(22)を有し、かつ、吸収器
(14)に至る前に予熱器(24)を経る。吸収器(14)の
熱媒体通路(14a)の下部出口は、予熱器(24)の上流
側の閉ループ(10)に接続する。凝縮器(6)の熱媒体
出口側に未凝縮ガスを分離するためのドレンポット(1
6)を設け、ドレンポット(16)の下部の液相は予熱器
(24)を経て膨張弁(8)に至り、上部の気相は吸収器
(14)の熱媒体通路(14a)の入口側に接続する。吸収
器(14)の冷却水通路(14b)に供給する冷却水として
は、たとえば、凝縮器(6)のものと共用することがで
きるが、別系統とすることもできる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG. 1, an absorber (14) which is a kind of heat exchanger having a heat medium passage (14a) and a cooling water passage (14b) is provided, and a heat medium of an evaporator (2) is provided. The liquid phase of the mist separator (18) provided on the outlet side is connected to the heat medium passage (14a) of the absorber (14) by the liquid return pipe (20). The liquid return pipe (20) has a pump (22) on the way and passes through a preheater (24) before reaching the absorber (14). The lower outlet of the heat medium passage (14a) of the absorber (14) is connected to a closed loop (10) upstream of the preheater (24). A drain pot (1) for separating uncondensed gas is provided at the heat medium outlet side of the condenser (6).
6), the lower liquid phase of the drain pot (16) reaches the expansion valve (8) via the preheater (24), and the upper gas phase is the inlet of the heat medium passage (14a) of the absorber (14). To the side. As the cooling water supplied to the cooling water passage (14b) of the absorber (14), for example, the cooling water can be shared with that of the condenser (6), but may be provided in another system.

【0011】蒸発器(2)で発生した熱媒体の蒸気は、
ミストセパレータ(18)で液と分離された上で、圧縮機
(4)に供給されて仕事をし、その後凝縮器(6)に進
み冷却水に熱を奪われて凝縮する。ミストセパレータ
(18)で蒸気から分離された蒸発残液つまり蒸発しきれ
なかった液相の熱媒体は、ポンプ(22)により液戻り配
管(20)を通じて吸収器(14)の熱媒体通路(14a)に
送り込まれる。
The heat medium vapor generated in the evaporator (2) is
After being separated from the liquid by the mist separator (18), it is supplied to the compressor (4) to perform work, and then proceeds to the condenser (6) to be deprived of heat by the cooling water and condensed. The evaporation residual liquid separated from the vapor by the mist separator (18), that is, the liquid-phase heat medium that has not been completely evaporated, is pumped by the pump (22) through the liquid return pipe (20) to the heat medium passage (14a) of the absorber (14). ).

【0012】この場合の蒸発器(2)、凝縮器(6)の
低沸成分濃度は図2のようになる。図中の○付き数字は
それぞれ次の事項を示している。凝縮器出口液、蒸
発器入口液、蒸発器出口液、蒸発器出口ガス、凝
縮器入口(または全体平均)ガス、凝縮器出口ガス。
図2から理解されるとおり、蒸発器出口液すなわち蒸
発残液は系内で最も低い低沸成分濃度を示す。一方、凝
縮器6の出口ではで示される状態の低沸成分ガスの濃
度が非常に高い。したがって、吸収器(14)に送り込ま
れた蒸発残液に低沸成分ガスが吸収される。なお、凝縮
器(6)内には〜の種々状態のガスが存在するが、
凝縮器(6)の熱媒体出口の低沸成分濃度が最も高い
の状態のガスが選択的に吸収されることとなる。このよ
うに、低沸成分濃度が系内で最も低い蒸発器出口の蒸発
残液を凝縮器出口側に送り込むことによって、この蒸発
残液に低沸成分ガスが吸収され、その結果、未凝縮低沸
成分ガス濃度が下がり、凝縮器伝熱性能が向上する。
In this case, the low-boiling component concentrations in the evaporator (2) and the condenser (6) are as shown in FIG. The circled numbers in the figure indicate the following items, respectively. Condenser outlet liquid, evaporator inlet liquid, evaporator outlet liquid, evaporator outlet gas, condenser inlet (or overall average) gas, condenser outlet gas.
As can be understood from FIG. 2, the evaporator outlet liquid, that is, the evaporation residual liquid, has the lowest low-boiling component concentration in the system. On the other hand, at the outlet of the condenser 6, the concentration of the low-boiling component gas in the state indicated by is very high. Therefore, the low-boiling component gas is absorbed by the evaporation residue sent to the absorber (14). In the condenser (6), there are gases in various states of
The gas having the highest concentration of low boiling components at the outlet of the heat medium of the condenser (6) is selectively absorbed. As described above, the low-boiling component gas is absorbed in the evaporating residue by sending the evaporating residue at the evaporator outlet having the lowest low-boiling component concentration in the system to the condenser outlet side. The boiling component gas concentration is reduced, and the condenser heat transfer performance is improved.

【0013】[0013]

【発明の効果】以上のように、この発明は、二成分系の
混合媒体を熱媒体として使用するヒートポンプにおい
て、凝縮器の熱媒体出口側に吸収器を設け、蒸発器の熱
媒体出口側の蒸発残液に凝縮器出口付近の未凝縮ガスを
吸収させるようにしたものであるから、系内で最も低い
低沸成分濃度を示す蒸発器出口の蒸発残液が低沸成分ガ
スを容易に吸収して凝縮器出口付近の未凝縮低沸成分ガ
ス濃度を下げ、凝縮器伝熱性能を向上させる。吸収器に
おける冷却作用により、吸収効果がさらに高まり、加え
て、液温(飽和温度)を下げてそれに伴って圧力を低下
させるはたらきをする。したがって、この発明によれ
ば、凝縮圧力を下げることによる圧縮機動力の軽減が可
能となるという効果も得られ、総じて当該ヒートポンプ
の性能が向上する。
As described above, according to the present invention, in a heat pump using a two-component mixed medium as a heat medium, an absorber is provided on the heat medium outlet side of the condenser and the heat medium outlet side of the evaporator is provided. Because the uncondensed gas near the condenser outlet is absorbed by the evaporation residue, the evaporation residue at the evaporator outlet showing the lowest low boiling component concentration in the system easily absorbs the low boiling component gas. To reduce the concentration of uncondensed low-boiling gas near the outlet of the condenser to improve the heat transfer performance of the condenser. The cooling effect in the absorber further enhances the absorption effect, and in addition, serves to lower the liquid temperature (saturation temperature) and thereby reduce the pressure. Therefore, according to the present invention, the effect that the power of the compressor can be reduced by lowering the condensing pressure is obtained, and the performance of the heat pump is generally improved.

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

【図1】この発明の実施例を示すブロック図である。FIG. 1 is a block diagram showing an embodiment of the present invention.

【図2】熱媒体の気液平衡線図である。FIG. 2 is a vapor-liquid equilibrium diagram of a heat medium.

【図3】従来例を示すブロック図である。FIG. 3 is a block diagram showing a conventional example.

【図4】二成分系混合媒体の温度−組成の関係を示す気
液平衡線図である。
FIG. 4 is a vapor-liquid equilibrium diagram showing the relationship between temperature and composition of a binary mixed medium.

【符号の説明】[Explanation of symbols]

2 蒸発器 4 圧縮機 6 凝縮器 8 膨張弁 10 閉ループ 12 電動機 14 吸収器 16 ドレンポット 18 ミストセパレータ 20 液戻り配管 22 ポンプ 24 予熱器 2 Evaporator 4 Compressor 6 Condenser 8 Expansion valve 10 Closed loop 12 Motor 14 Absorber 16 Drain pot 18 Mist separator 20 Liquid return pipe 22 Pump 24 Preheater

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭63−210565(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 7/00 F25B 1/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-63-210565 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F25B 7/00 F25B 1/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 蒸発器と、圧縮機と、凝縮器と、膨張弁
を直列に接続して閉ループを構成させ、この閉ループ内
で熱媒体を循環させるようにした、二成分系の混合媒体
を熱媒体として使用するヒートポンプにおいて、凝縮器
の熱媒体出口側に吸収器を設け、蒸発器の熱媒体出口側
の蒸発残液を前記吸収器を介して膨張弁上流側の閉ルー
プに導くことにより、前記吸収器において前記蒸発残液
に凝縮器出口付近の未凝縮ガスを吸収させることを特徴
とする混合媒体用ヒートポンプ。
1. An evaporator, a compressor, a condenser, and an expansion valve.
Are connected in series to form a closed loop.
In was such that the heat medium is circulated, the heat pump using a mixed medium of two-component as a heat medium, the absorber provided in the heat medium outlet side of the condenser, evaporation residual liquid of the heat medium outlet side of the evaporator Closed loop upstream of the expansion valve via the absorber
A heat pump for a mixed medium , wherein the non-condensed gas near the outlet of the condenser is absorbed by the evaporating residual liquid in the absorber by being guided to the pump.
JP07471592A 1992-03-30 1992-03-30 Heat pump for mixed media Expired - Fee Related JP3244087B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07471592A JP3244087B2 (en) 1992-03-30 1992-03-30 Heat pump for mixed media

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07471592A JP3244087B2 (en) 1992-03-30 1992-03-30 Heat pump for mixed media

Publications (2)

Publication Number Publication Date
JPH05280813A JPH05280813A (en) 1993-10-29
JP3244087B2 true JP3244087B2 (en) 2002-01-07

Family

ID=13555201

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07471592A Expired - Fee Related JP3244087B2 (en) 1992-03-30 1992-03-30 Heat pump for mixed media

Country Status (1)

Country Link
JP (1) JP3244087B2 (en)

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EP1422486A3 (en) * 2002-11-25 2004-11-17 Tempia Co., Ltd. Combined regeneration heating and cooling system
CN110822755B (en) * 2019-11-27 2024-06-28 江苏天舒电器有限公司 A heat pump system using a non-azeotropic refrigerant mixture
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