JPH0765827B2 - Dual heat pump that can take out cold water and steam simultaneously - Google Patents
Dual heat pump that can take out cold water and steam simultaneouslyInfo
- Publication number
- JPH0765827B2 JPH0765827B2 JP1297289A JP1297289A JPH0765827B2 JP H0765827 B2 JPH0765827 B2 JP H0765827B2 JP 1297289 A JP1297289 A JP 1297289A JP 1297289 A JP1297289 A JP 1297289A JP H0765827 B2 JPH0765827 B2 JP H0765827B2
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- Japan
- Prior art keywords
- cycle
- heat pump
- economizer
- boiling
- condenser
- 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
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- Engine Equipment That Uses Special Cycles (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は高温側ヒートポンプサイクルと低温側ヒートポ
ンプサイクルを組み合わせた冷水及び蒸気同時取出2元
ヒートポンプに係り、就中、蒸気取出に際して高沸点冷
媒の圧縮機出口温度を一定温度に調整可能ならしめ、高
沸点冷媒の高温劣化を防止せしめる上記2元ヒートポン
プに関するものである。Description: TECHNICAL FIELD The present invention relates to a cold water and steam simultaneous extraction dual heat pump that combines a high temperature side heat pump cycle and a low temperature side heat pump cycle, and in particular, a high boiling point refrigerant for steam extraction. The present invention relates to the binary heat pump described above, which allows the compressor outlet temperature to be adjusted to a constant temperature and prevents the high boiling point refrigerant from being deteriorated at high temperatures.
(従来の技術) 高沸点冷媒を使用する高温側ヒートポンプサイクルと低
沸点冷媒を使用する低温側ヒートポンプサイクルとを組
合わせ、高温の熱出力を高温側ヒートポンプサイクルか
ら、一方、低温の熱出力を低温側ヒートポンプサイクル
から取り出すようにした、いわゆる2元ヒートポンプは
公知であり、特開昭62−52376号公報、同62−52377号公
報、実開昭57−2364号公報及び実開昭63−2053号公報な
どにより数多く開示されている。(Prior art) A high temperature side heat pump cycle that uses a high boiling point refrigerant and a low temperature side heat pump cycle that uses a low boiling point refrigerant are combined so that the high temperature heat output is from the high temperature side heat pump cycle, while the low temperature heat output is low. A so-called binary heat pump adapted to be taken out from the side heat pump cycle is known, and is disclosed in JP-A-62-52376, JP-A-62-52377, JP-A-57-2364 and JP-A-63-2053. Many are disclosed in the gazette and the like.
第3図はかかる2元ヒートポンプの一般的なサイクル構
成を示す図であり、高温側サイクルとして圧縮機
(1)、凝縮器(2)、受液器(3)、膨張弁(4)、
アキュムレータ(6)、が順次、接続配管されていると
共に、一方の低温側サイクルは、圧縮機(7)、受液器
(8)、凝張弁(9)、蒸発器(10)、アキュムレータ
(11)、が順次、接続配管されて構成されており、低温
側サイクルの凝縮器と高温側サイクルの蒸発器とがカス
ケードコンデンサ(5)において熱交換が行われてい
る。そして、通常、上記高温側サイクルにはフロンR−
113,R−114等の高沸点冷媒が、一方、低温側サイクルに
はR−12,R−22等の低沸点冷媒が用いられている。FIG. 3 is a diagram showing a general cycle configuration of such a binary heat pump. As a high temperature side cycle, a compressor (1), a condenser (2), a liquid receiver (3), an expansion valve (4),
The accumulator (6) is sequentially connected and connected, and one of the low-temperature side cycles has a compressor (7), a liquid receiver (8), a coagulation valve (9), an evaporator (10), and an accumulator ( 11) are sequentially connected and connected, and the condenser of the low temperature side cycle and the evaporator of the high temperature side cycle perform heat exchange in the cascade condenser (5). And, normally, CFC R-
High boiling point refrigerants such as 113 and R-114 are used, while low boiling point refrigerants such as R-12 and R-22 are used in the low temperature side cycle.
次に上記第3図を参照し、それら2元ヒートポンプの作
動を説明すると、高温側サイクルにおいては、圧縮機
(1)から高温高圧の状態で吐出された高沸点冷媒は、
凝縮器(2)において冷却塔(T)を介し循環する冷却
水等により冷却されて液化した後、受液器(3)に一旦
溜まり、次いで膨張弁(4)で低圧の液ガス混合状態と
なり、後、カスケードコンデンサ(5)で低温側サイク
ルの冷媒から熱を得て蒸発しアキュムレータ(6)を経
て低圧のガス状となり、圧縮機(1)へもどるサイクル
となっている。一方、低温側サイクルにおいては圧縮機
(7)から吐出する低沸点冷媒は、高温・高圧の状態で
カスケードコンデンサ(5)を介し高沸点冷媒に熱を与
えるとともに自身は冷却されて凝縮液化し、受液器
(8)で一旦貯溜された後、膨張弁(9)により低圧の
液ガス混合状態となり、しかる後、蒸発器(10)におい
て、吸熱して周囲を冷却すると共に冷媒自身は蒸発し、
次のアキュムレータ(11)を経て、低圧のガス状となっ
て圧縮機(7)へ戻るサイクルになっている。Next, referring to FIG. 3 above, the operation of these binary heat pumps will be described. In the high temperature side cycle, the high boiling point refrigerant discharged from the compressor (1) in a high temperature and high pressure state is
In the condenser (2), after being cooled by cooling water or the like circulating through the cooling tower (T) and liquefied, it is temporarily stored in the liquid receiver (3), and then in the low pressure liquid-gas mixture state by the expansion valve (4). After that, the cascade condenser (5) obtains heat from the refrigerant of the low temperature side cycle, evaporates, becomes a low-pressure gaseous state through the accumulator (6), and returns to the compressor (1). On the other hand, in the low temperature side cycle, the low boiling point refrigerant discharged from the compressor (7) gives heat to the high boiling point refrigerant through the cascade condenser (5) in a high temperature and high pressure state, and is itself cooled and condensed and liquefied. After being temporarily stored in the liquid receiver (8), a low-pressure liquid-gas mixture state is set by the expansion valve (9). Then, in the evaporator (10), heat is absorbed to cool the surroundings and the refrigerant itself evaporates. ,
A cycle of returning to the compressor (7) through a next accumulator (11) into a low-pressure gas state.
(発明が解決しようとする課題) ところが、上記の如き2元ヒートポンプはそのサイクル
により低温側の温度を氷点以下に下げることを目的とし
ており、そのため高温側凝縮器は放熱のみを対象として
いることから圧縮機から吐出する高沸点冷媒の温度を極
端に大きくする必要がなかったが、この2元ヒートポン
プを用いて冷水及び蒸気を取り出そうとすれば圧縮機か
ら吐出する高沸点冷媒の温度及び圧力が異常に高くな
り、冷媒及び冷凍機油の熱分解を促し、劣化を招き、成
績係数の大幅な低下が起こる。そのため従前の上記2元
ヒートポンプは常温の熱源から蒸気を取り出そうとする
ことは事実上困難であった。(Problems to be Solved by the Invention) However, the above-described binary heat pump is intended to lower the temperature on the low temperature side to below the freezing point by its cycle, and therefore the high temperature side condenser is intended only for heat dissipation. It was not necessary to raise the temperature of the high boiling point refrigerant discharged from the compressor to an extremely high level. However, if cold water and steam were to be taken out using this dual heat pump, the temperature and pressure of the high boiling point refrigerant discharged from the compressor would be abnormal. It becomes very high, promotes thermal decomposition of the refrigerant and refrigerating machine oil, causes deterioration, and causes a significant decrease in the coefficient of performance. Therefore, it has been practically difficult for the above-mentioned binary heat pump to take out steam from a heat source at room temperature.
本発明は上述の如き実状に対処し、冷水及び蒸気同時取
り出し2元ヒートポンプシステムにおいて、高沸点冷媒
サイクルにおける圧縮機吐出温度を調整する手段を付与
することにより冷凍機油及び圧縮機から吐出する高沸点
冷媒が劣化しないように制御し、冷水及び蒸気同時取出
しを可能かつ安定ならしめることを目的とするものであ
る。The present invention copes with the above situation, and in a dual heat pump system for simultaneous extraction of cold water and steam, by providing a means for adjusting the compressor discharge temperature in the high boiling point refrigerant cycle, the high boiling point discharged from the refrigerating machine oil and the compressor. The purpose is to control so that the refrigerant does not deteriorate so that cold water and steam can be taken out simultaneously and stably.
(課題を解決するための手段) 即ち、上記目的に適合するための本発明2元ヒートポン
プの特徴とするところは、蒸発器を冷水取り出し用とす
る低沸点冷媒サイクルと、凝縮器を蒸気取り出し用とす
る高沸点冷媒サイクルを低沸点側サイクルの凝縮器と高
沸点側サイクルの蒸発器とが熱交換するカスケードコン
デンサーによって連結すると共に、高沸点側サイクルの
受液器と膨張弁の間と、蒸発器とアキュムレータの間と
で熱交換を行うエコノマイザを設置してなる2元ヒート
ポンプにおいて、前記両熱交換器を完全に対向流となす
と共に、凝縮器からエコノマイザに入る回路と並列に受
液器から直接膨張弁へ入り込むバイパスを設け、バイパ
ス回路及び受液器からエコノマイザに入る回路に高沸点
側サイクルの圧縮機から吐出する高沸点冷媒のガス温度
測定センサーと制御装置の信号で作動する流量調整バル
ブを設けた点にある。(Means for Solving the Problem) That is, the feature of the dual heat pump of the present invention to meet the above-mentioned object is that a low boiling point refrigerant cycle in which an evaporator is for taking out cold water and a condenser is for taking out steam. The high-boiling-point refrigerant cycle is connected by a cascade condenser that exchanges heat between the low-boiling-side cycle condenser and the high-boiling-side cycle evaporator, and the high-boiling-side cycle between the receiver and the expansion valve In a binary heat pump with an economizer installed for heat exchange between a condenser and an accumulator, both heat exchangers are completely opposed to each other, and a receiver is provided in parallel with a circuit from the condenser to the economizer. By providing a bypass that directly enters the expansion valve, the high boiling point cooling discharged from the compressor of the high boiling point cycle is used in the bypass circuit and the circuit that enters the economizer from the receiver. The point is that a gas temperature measuring sensor for the medium and a flow rate adjusting valve that operates by a signal from the control device are provided.
(作用) 上記の如き2元ヒートポンプを用いて冷水及び蒸気を同
時に取り出しする場合において、蒸気取り出し用凝縮器
には完全対向流となる熱交換器を用いていることにより
圧縮機から吐出する高沸点冷媒ガス温度付近まで蒸気を
加熱することが可能となり、その結果、凝縮温度以上の
蒸気温度を得て従来の2元ヒートポンプにおける低沸点
冷媒側蒸発器からの冷水取り出しと共に高沸点冷媒側凝
縮器より蒸気を取り出すことを可能とする。そして、上
記冷水及び蒸気取り出しに際し、高温側サイクルの圧縮
機から吐出する高沸点冷媒のガス温度を感知し、流量調
整バルブを作動させ、受液器からエコノマイザに流れる
冷媒流量を調整することによって、エコノマイザ出口の
過冷却度及び過熱度が変化し、高沸点冷媒サイクルの圧
縮機吐出ガス温度を一定温度に調整し、冷凍機油及び冷
媒の劣化を防止するとともに長期間連続運転が可能とな
る。(Operation) When cold water and steam are simultaneously taken out by using the binary heat pump as described above, a high-boiling point discharged from the compressor is used by using a heat exchanger which is a completely countercurrent flow for the steam taking-out condenser. It becomes possible to heat the steam up to near the refrigerant gas temperature, and as a result, the steam temperature above the condensation temperature is obtained, and cold water is taken out from the low boiling point refrigerant side evaporator in the conventional dual heat pump and from the high boiling point refrigerant side condenser. It is possible to take out steam. Then, when the cold water and the steam are taken out, by sensing the gas temperature of the high boiling point refrigerant discharged from the compressor of the high temperature side cycle, operating the flow rate adjusting valve, and adjusting the refrigerant flow rate flowing from the liquid receiver to the economizer, The degree of supercooling and the degree of superheat at the exit of the economizer change, the temperature of the gas discharged from the compressor in the high boiling point refrigerant cycle is adjusted to a constant temperature, deterioration of refrigerating machine oil and refrigerant can be prevented, and long-term continuous operation becomes possible.
なお、上記作用は冷水及び蒸気を同時に取り出す場合で
あるが別段、同時に取り出すことなく、、何れか一方の
みの取り出しとして使用しても何ら差支えなく、その作
用は上述するところと同様である。Note that the above-mentioned action is a case where cold water and steam are taken out at the same time. However, there is no problem even if the cold water and steam are taken out at the same time, and it is possible to use only one of them without taking out at the same time, and the action is the same as that described above.
(実施例) 以下、更に添付図面にもとづいて本発明の実施例を説明
する。(Example) Hereinafter, an example of the present invention will be described with reference to the accompanying drawings.
第1図は本発明による冷水及び蒸気取り出し2元ヒート
ポンプのサイクル系統図であり、第3図と同様に高温側
サイクルは、圧縮機(1)、凝縮器(2)、受液器
(3)、膨張弁(4)、カスケードコンデンサ(5)、
アキュムレータ(6)を順次接続配管して構成され、低
温側サイクルは、圧縮機(7)、カスケードコンデンサ
(5)、受液器(8)、膨張弁(9)、蒸発器(10)ア
キュムレータ(11)を順次接続配管して構成されてい
る。そして、上記構成回路において、本発明では第1図
に示すように前記高温側サイクルの受液器(3)と膨張
弁(4)の間と、カスケードコンデンサ(5)とアキュ
ムレータ(6)の間で熱交換を行うエコノマイザ(12)
が設けられており、かつ、受液器(3)からエコノマイ
ザ(12)に入る回路と並列に受液器(3)から直接膨張
弁(4)に入り込むバイパスが配設され、これに高温側
サイクルの圧縮機(1)から吐出する高沸点冷媒のガス
温度を測定するセンサー(15)と制御装置(16)の信号
によって作動する流量調整バルブ(13),(14)が設置
されている。FIG. 1 is a cycle system diagram of a dual heat pump for taking out cold water and steam according to the present invention. As in FIG. 3, the high temperature side cycle includes a compressor (1), a condenser (2) and a liquid receiver (3). , Expansion valve (4), cascade condenser (5),
The low-temperature cycle is configured by sequentially connecting and accumulating pipes (6), and the low-temperature cycle includes a compressor (7), a cascade condenser (5), a liquid receiver (8), an expansion valve (9), an evaporator (10), and an accumulator ( 11) is constructed by connecting piping in sequence. Further, in the above-mentioned configuration circuit, in the present invention, as shown in FIG. 1, between the liquid receiver (3) and the expansion valve (4) of the high temperature side cycle, and between the cascade condenser (5) and the accumulator (6). Economizer for heat exchange in
Is provided, and a bypass is provided in parallel with the circuit that enters the economizer (12) from the receiver (3) and that directly enters the expansion valve (4) from the receiver (3). Sensors (15) for measuring the gas temperature of the high boiling point refrigerant discharged from the compressor (1) of the cycle and flow rate adjusting valves (13), (14) operated by signals of a control device (16) are installed.
なお、図中(17)は低温側サイクルの蒸発器における熱
源水入口、(18)は同冷水出口であり、(19)は高温側
サイクルにおける被加熱水入口、(20)は、同蒸気出口
である。In the figure, (17) is the heat source water inlet in the low temperature side evaporator, (18) is the same cold water outlet, (19) is the heated water inlet in the high temperature side cycle, and (20) is the same steam outlet. Is.
しかして、上記カスケードコンデンサ(5)及びエコノ
マイザ(12)によって熱的に結合されている両サイクル
はその凝縮器(2)では被加熱水が冷媒と対向流で熱交
換をすべく配管され、またエコノマイザ(12)及びカス
ケードコンデンサ(5)における冷媒同志の熱交換も対
向流でなされるように配管されている。Therefore, in both of the cycles that are thermally coupled by the cascade condenser (5) and the economizer (12), in the condenser (2), the heated water is piped so as to exchange heat with the refrigerant in a counterflow, and The heat exchange between the refrigerants in the economizer (12) and the cascade condenser (5) is also arranged so as to be performed in counterflow.
次に上記第1図における2元ヒートポンプサイクルの動
作状況を第2図に示すモリエル線図と共に説明すると、
高温側サイクルでは、圧縮機(1)から高温高圧で吐出
される高沸点冷媒(R−114)は凝縮器(2)において
対向流をなす被加熱水を加熱し、蒸気として出口(20)
より出すとともに自身は冷却されて高温の液冷媒とな
り、受液器(3)へ一時貯溜された後、エコノマイザ
(12)へ入る。この間の状態を第2図のモリエル線図で
は、(f),(g)から(i)へ至る線で示している。
そして前記エコノマイザ(12)では対向して流れるカス
ケードコンデンサ(5)からアキュムレータ(6)に流
れる冷媒と熱交換することで、受液器から出た冷媒は、
過冷却され、第2図における(h)の位置を得る。次い
で、膨張弁(4)へはいり、低圧状態となって、再び第
2図の(e)へ達し、カスケードコンデンサ(5)へ至
り、ここで低圧側サイクルの低沸点冷媒の凝縮熱を吸熱
して低圧状態でガス冷媒になるとともに過熱される。こ
の時点が第2図では(j)で示される。しかる後、エコ
ノマイザ(12)へ至り、対向して流れる受液器(3)か
らエコノマイザ(12)に流れる冷媒より熱を与えられさ
らに過熱された冷媒はアキュムレータ(6)を経て圧縮
機(1)によって吸引されサイクルを完了し、この間、
蒸気取出しがなされる。Next, the operating condition of the dual heat pump cycle in FIG. 1 will be described with reference to the Mollier diagram shown in FIG.
In the high temperature side cycle, the high boiling point refrigerant (R-114) discharged from the compressor (1) at high temperature and high pressure heats the counter-current water to be heated in the condenser (2), and outputs it as steam at the outlet (20).
As it is discharged, it cools itself into a high-temperature liquid refrigerant, which is temporarily stored in the liquid receiver (3) and then enters the economizer (12). In the Mollier diagram of FIG. 2, the state during this time is shown by lines from (f) and (g) to (i).
Then, in the economizer (12), heat exchange with the refrigerant flowing from the cascade condenser (5) flowing in the opposite direction to the accumulator (6) causes the refrigerant discharged from the receiver to
It is supercooled and the position (h) in FIG. 2 is obtained. Then, it goes into the expansion valve (4), becomes a low pressure state, reaches (e) of FIG. 2 again, reaches the cascade condenser (5), and absorbs the condensation heat of the low boiling point refrigerant in the low pressure side cycle. It becomes a gas refrigerant under low pressure and is overheated. This point is indicated by (j) in FIG. After that, the refrigerant that reaches the economizer (12) and is further heated by the refrigerant flowing from the liquid receiver (3) flowing in the opposite direction to the economizer (12) is further heated, and then passes through the accumulator (6) to the compressor (1). Completes the cycle as it is aspirated by
Steam is taken out.
なお、以上のサイクルにおいて高温側サイクルは往々に
して第2図における(e)′,(j),(f)′,
(g)′,(i)′,(h)′,(e)′となることが
あるがこれを上述の如きサイクルにもってゆくことは極
めて望ましいことである。In the above cycle, the high temperature side cycle is often (e) ', (j), (f)', in FIG.
(G) ', (i)', (h) ', (e)' may occur, but it is extremely desirable to carry them through the cycle as described above.
一方、低温側サイクルでは、圧縮機(7)から吐出され
る高温高圧の低沸点冷媒は、第2図のモリエル線図では
(c)で示された後、次のカスケードコンデンサ(5)
に入り、ここで前記した高温側サイクルの高沸点冷媒に
凝縮熱を与えるとともに、自身は高沸点冷媒の蒸発によ
って熱を奪われる。この状態が第2図の(d)である。On the other hand, in the low temperature side cycle, the high temperature and high pressure low boiling point refrigerant discharged from the compressor (7) is shown by (c) in the Mollier diagram of FIG. 2 and then the next cascade condenser (5).
Then, the heat of condensation is given to the high boiling point refrigerant in the high temperature side cycle, and at the same time, the heat is taken away by the evaporation of the high boiling point refrigerant. This state is shown in FIG.
この後、受液器(8)で一旦貯溜されて膨張弁を通過
し、第2図の(a)となる。次いで、蒸発器(10)に入
り、熱源水から熱を奪って冷水とし、冷水出口(18)よ
り取出される。After that, the liquid is temporarily stored in the liquid receiver (8) and passes through the expansion valve, resulting in (a) in FIG. Next, it enters the evaporator (10), takes heat from the heat source water to make cold water, and is taken out from the cold water outlet (18).
一方、自身は吸熱してガス冷媒となる。ここは第2図の
(b)である。そして上記動作状況にあって、高温側サ
イクルの圧縮機から吐出する高沸点冷媒のガス温度を感
知し、これに従って流量調整バルブ(13),(14)を作
動することにより、エコノマイザ(12)への流量を調整
し、高温側サイクルの高圧側のエコノマイザ出口の過冷
却度及び低圧側圧縮機吸い込みガスの過熱度を調整し、
圧縮機吐出ガス温度を一定温度にする。On the other hand, it absorbs heat and becomes a gas refrigerant. This is (b) of FIG. Then, under the above operating conditions, the gas temperature of the high boiling point refrigerant discharged from the compressor in the high temperature side cycle is sensed, and the flow rate adjusting valves (13) and (14) are actuated in accordance with the detected gas temperature to the economizer (12). Of the high temperature side of the high temperature side economizer outlet to adjust the degree of supercooling and the low pressure side compressor suction gas superheat degree,
Keep the compressor discharge gas temperature constant.
これを更に詳述すると上記の如く作動する本発明に係る
ヒートポンプにおいて、例えば、前記流量調整バルブ
(13)を開く、または流量調整バルブ(14)を閉じる
と、前記エコノマイザ(12)での交換熱量は多くなり、
その結果、高圧側エコノマイザ(12)出口冷媒の過冷却
は大きくなるとともに、低圧側サイクルにおけるエコノ
マイザ(12)出口側では冷媒の加熱が大きくなる。この
状態で第2図のモリエル線図において、前者は(h)″
で示され、後者は(f)″で示される。More specifically, in the heat pump according to the present invention which operates as described above, for example, when the flow rate adjusting valve (13) is opened or the flow rate adjusting valve (14) is closed, the heat exchange amount in the economizer (12) is changed. Will increase,
As a result, the supercooling of the high-pressure side economizer (12) outlet refrigerant increases, and the refrigerant heating increases on the low-pressure side economizer (12) outlet side. In this state, the former is (h) ″ in the Mollier diagram of FIG.
, And the latter is indicated by (f) ″.
圧縮機(1)吐出ガス温度が高くなる。ここはモリエル
線図の(g)″である。The compressor (1) discharge gas temperature becomes high. This is (g) ″ in the Mollier diagram.
次に反対に、前記流量調整バルブ(13)を閉じるまたは
流量調整バルブ(14)を開くと上記とは逆の作用によ
り、圧縮機(1)吐出ガス温度は低くなる。Next, conversely, when the flow rate adjusting valve (13) is closed or the flow rate adjusting valve (14) is opened, the discharge gas temperature of the compressor (1) becomes low due to the effect opposite to the above.
従って、温度センサー(15)の感知によりその温度セン
サー(15)から出力信号を出し、これに応答する制御装
置(16)によって前記流量調整バルブ(14),(15)を
コントロールすることで、圧縮機(1)吐出ガス温度を
自動的に一定に維持することができる。Therefore, when the temperature sensor (15) senses an output signal from the temperature sensor (15) and the control device (16) responding to the output signal controls the flow rate adjusting valves (14) and (15), the compression is achieved. The discharge gas temperature of the machine (1) can be automatically maintained constant.
かくして、高温側サイクル(e),(j),(f),
(g),(i),(h),(e)と低温側サイクル
(a),(b),(c),(d),(a)は(e),
(j)及び(d),(c)がカスケードコンデンサによ
って、熱的に結合されまた高温側サイクル(i),
(h)(A部分)及び(j),(f)(B部分)がエコ
ノマイザによって熱的に結合され、従前の2元ヒートポ
ンプのモリエル線図である高温側サイクル(e),
(j),(g),(i),(e)と低温側サイクル
(a),(b),(c),(d),(a)に比しより熱
効率を高めることとなる。Thus, the high temperature side cycles (e), (j), (f),
(G), (i), (h), (e) and low temperature side cycles (a), (b), (c), (d), (a) are (e),
(J) and (d), (c) are thermally coupled by a cascade capacitor and the high temperature side cycle (i),
(H) (A part) and (j), (f) (B part) are thermally coupled by an economizer, and a high temperature side cycle (e), which is a Mollier diagram of a conventional binary heat pump,
(J), (g), (i) and (e) and the low temperature side cycles (a), (b), (c), (d) and (a) will result in higher thermal efficiency.
なお、以上は冷水、蒸気の同時取り出しの場合について
述べた来たが、冷水、蒸気の何れか一方のみの使用でも
よいことは前述の通りである。Although the case of simultaneously taking out cold water and steam has been described above, it is as described above that only one of cold water and steam may be used.
また、冷水、蒸気に限らず他の流体に対しても同様に適
用し得る範囲で使用可能であり、冷水、蒸気は広く流体
を意味するものと理解されよう。Further, it can be understood that the present invention can be used not only for cold water and steam but also for other fluids in a range that can be similarly applied, and cold water and steam broadly mean fluids.
(発明の効果) 以上のように本発明に係る2元ヒートポンプは、高温側
サイクルにおいて、流量調整バルブを介装した受液器か
らエコノマイザに入る回路と並列に、流量調整バルブを
介装したバイパスを設け、流量調整バルブの開閉によっ
て、エコノマイザへ流れる高温側冷媒の流量を調整する
ものであるから冷水及び蒸気を同時に取り出す際、高温
側サイクルの圧縮機から吐出する高沸点冷媒の温度が所
定の温度を越えても、前記流量調整バルブを操作するこ
とで直ちに所定の温度へ戻すことが可能となり、同温度
を一定温度に保持し、これによって異常な圧力や温度を
抑え、冷媒や冷凍機油の劣化を防止し、結果として成績
係数の低下を防ぎ、安定して常時、蒸気を取り出すこと
が可能となる顕著な効果を有している。(Effects of the Invention) As described above, in the two-way heat pump according to the present invention, in the high temperature cycle, the bypass including the flow rate adjusting valve is provided in parallel with the circuit that enters the economizer from the liquid receiver including the flow rate adjusting valve. Is provided to adjust the flow rate of the high temperature side refrigerant flowing to the economizer by opening and closing the flow rate adjusting valve. Even if the temperature is exceeded, it is possible to immediately return to a predetermined temperature by operating the flow rate control valve, and maintain the same temperature at a constant temperature, thereby suppressing abnormal pressure and temperature, and refrigerating oil or refrigerating machine oil. It has a remarkable effect of preventing deterioration and, as a result, preventing a decrease in the coefficient of performance, and making it possible to take out steam constantly and stably.
しかも前記流量調整バルブと温度センサー及び制御装置
とを組み合わせることで、高沸点冷媒の圧縮機吐出温度
を自動的に保つこともでき、冷水及び蒸気取出の自動化
を図ることができる。Moreover, by combining the flow rate adjusting valve with the temperature sensor and the control device, the compressor discharge temperature of the high boiling point refrigerant can be automatically maintained, and the cold water and steam can be taken out automatically.
第1図は本発明に係る2元ヒートポンプの一例を示すサ
イクル系統図、第2図は上記サイクルにもとづくモリエ
ル線図、第3図は従来の2元ヒートポンプのサイクル系
統図である。 (1),(7)…圧縮機、(2)…凝縮器、(3),
(8)…受液器、(4),(9)…膨張弁、(5)…カ
スケードコンデンサ、(6),(11)…アキュムレー
タ、(10)…蒸発器、(12)…エコノマイザ、(13),
(14)…流量調整バルブ、(15)…センサー、(16)…
制御装置。FIG. 1 is a cycle system diagram showing an example of a binary heat pump according to the present invention, FIG. 2 is a Mollier diagram based on the above cycle, and FIG. 3 is a cycle system diagram of a conventional binary heat pump. (1), (7) ... Compressor, (2) ... Condenser, (3),
(8) ... Liquid receiver, (4), (9) ... Expansion valve, (5) ... Cascade condenser, (6), (11) ... Accumulator, (10) ... Evaporator, (12) ... Economizer, ( 13),
(14) ... Flow control valve, (15) ... Sensor, (16) ...
Control device.
フロントページの続き (72)発明者 藤島 征雄 大阪府堺市新桧尾台4丁16番6―406 (72)発明者 波多野 泰弘 大阪府堺市三原台3丁33番2号 (72)発明者 緒方 正実 大阪府枚方市田口山2丁目26番9号 (72)発明者 浦田 幸敏 大阪府高槻市深沢町2丁目29番14号 (72)発明者 石川 保 京都府綴喜郡田辺町字天王小字下垣内29 (72)発明者 川端 政行 大阪府枚方市池之宮2丁目11番6号Front Page Continuation (72) Inventor Masao Fujishima 4-16- Shinhinodai, Sakai City, Osaka Prefecture 6-406 (72) Inventor Yasuhiro Hatano 3-33-2 Miharadai, Sakai City, Osaka Prefecture (72) Inventor Masami Ogata Osaka 2-26-9 Taguchiyama, Hirakata-shi (72) Inventor Yukitoshi Urata 2-29-14 Fukasawa-cho, Takatsuki-shi, Osaka (72) Inventor Tamotsu Ishikawa 29, Tenobe-cho, Tsunabe-cho, Kyoto Prefecture Shimogakiuchi (29 72) Inventor Masayuki Kawabata 2-11-6 Ikenomiya, Hirakata City, Osaka Prefecture
Claims (1)
サイクルと、凝縮器を蒸気取り出し用とする高沸点冷媒
を低沸点側サイクルの凝縮器と高沸点側サイクルの蒸発
器とが熱交換するカスケードコンデンサーによって連結
すると共に、高沸点側サイクルの受液器と膨張弁の間
と、蒸発器とアキュムレータの間とで熱交換を行うエコ
ノマイザを設置してなる2元ヒートポンプにおいて、前
記熱交換器を完全に対向流となすと共に、前記受液器か
らエコノマイザに入る回路と並列に受液器から膨張弁へ
直接入り込むバイパスを設け、バイパス回路及び受液器
からエコノマイザに入る回路に高沸点側サイクルの圧縮
機から吐出する高沸点冷媒のガス温度測定センサーと制
御装置の信号で作動する流量調整バルブを設けたことを
特徴とする冷水及び蒸気同時取り出し可能な2元ヒート
ポンプ。1. A low-boiling-point refrigerant cycle in which an evaporator is for taking out cold water, and a high-boiling-point refrigerant in which a condenser is for taking out steam is heat-exchanged between a condenser in a low-boiling-side cycle and an evaporator in a high-boiling-side cycle. In the two-way heat pump, the economizer is installed to connect between the receiver and the expansion valve of the high-boiling-side cycle and between the evaporator and the accumulator while being connected by a cascade condenser that And a bypass that directly enters the expansion valve from the receiver in parallel with the circuit that enters the economizer from the receiver, and a high-boiling-side cycle in the bypass circuit and the circuit that enters the economizer from the receiver. Chilled water characterized by having a gas temperature measuring sensor for high boiling point refrigerant discharged from the compressor and a flow rate control valve operated by a signal from the control device, Care simultaneous removable 2-way heat pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1297289A JPH0765827B2 (en) | 1989-01-21 | 1989-01-21 | Dual heat pump that can take out cold water and steam simultaneously |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1297289A JPH0765827B2 (en) | 1989-01-21 | 1989-01-21 | Dual heat pump that can take out cold water and steam simultaneously |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02195162A JPH02195162A (en) | 1990-08-01 |
| JPH0765827B2 true JPH0765827B2 (en) | 1995-07-19 |
Family
ID=11820145
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1297289A Expired - Lifetime JPH0765827B2 (en) | 1989-01-21 | 1989-01-21 | Dual heat pump that can take out cold water and steam simultaneously |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0765827B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101218808B1 (en) * | 2011-11-10 | 2013-01-09 | 선문대학교 산학협력단 | Demand with duality cycle of heat pump system |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2552555B2 (en) * | 1989-11-02 | 1996-11-13 | 大阪府 | How to operate the heat pump |
| JPH0618107A (en) * | 1991-10-16 | 1994-01-25 | Kyushu Electric Power Co Inc | Ice / hot water double heat storage system |
| KR100690090B1 (en) * | 2006-04-05 | 2007-03-09 | 한국에너지기술연구원 | Seawater Cascade Heat Pump System |
| EP2306122B1 (en) * | 2008-06-24 | 2017-07-26 | Mitsubishi Electric Corporation | Refrigerating cycle apparatus, and air conditioning apparatus |
| JP4915680B2 (en) * | 2009-06-30 | 2012-04-11 | 株式会社東洋製作所 | Multi-source heat pump steam / hot water generator |
| KR101190492B1 (en) * | 2010-05-20 | 2012-10-12 | 엘지전자 주식회사 | Hot water supply device associated with heat pump |
| KR101227181B1 (en) * | 2010-12-31 | 2013-01-28 | 임선식 | Heat pump system for water supply using two stage heat pump |
-
1989
- 1989-01-21 JP JP1297289A patent/JPH0765827B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101218808B1 (en) * | 2011-11-10 | 2013-01-09 | 선문대학교 산학협력단 | Demand with duality cycle of heat pump system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02195162A (en) | 1990-08-01 |
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