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JPH0686958B2 - Solar water heater - Google Patents
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JPH0686958B2 - Solar water heater - Google Patents

Solar water heater

Info

Publication number
JPH0686958B2
JPH0686958B2 JP61248616A JP24861686A JPH0686958B2 JP H0686958 B2 JPH0686958 B2 JP H0686958B2 JP 61248616 A JP61248616 A JP 61248616A JP 24861686 A JP24861686 A JP 24861686A JP H0686958 B2 JPH0686958 B2 JP H0686958B2
Authority
JP
Japan
Prior art keywords
refrigerant
water
heat
defrosting operation
compressor
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
JP61248616A
Other languages
Japanese (ja)
Other versions
JPS63101661A (en
Inventor
和彦 宮本
正久 田島
佳嗣 藤本
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP61248616A priority Critical patent/JPH0686958B2/en
Publication of JPS63101661A publication Critical patent/JPS63101661A/en
Publication of JPH0686958B2 publication Critical patent/JPH0686958B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers

Landscapes

  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、太陽熱利用給湯装置に関するものである。Description: FIELD OF THE INVENTION The present invention relates to a water heater utilizing solar heat.

従来の技術 従来のこの種の太陽熱利用給湯装置は、第2図に示すよ
うに、圧縮機1,四方弁8,冷媒対水熱交換器2,高圧冷媒配
管3,逆止弁5を並列に装着した膨張弁4,集熱器6,低圧冷
媒配管7,四方弁8,圧縮機1を、順次環状に連結してなる
主冷媒回路と、蓄熱槽9、水循環ポンプ10,冷媒対水熱
交換器2を、順次環状に連結してなる水循環回路を備え
ている。
2. Description of the Related Art As shown in FIG. 2, a conventional solar hot water supply system of this type includes a compressor 1, a four-way valve 8, a refrigerant-to-water heat exchanger 2, a high-pressure refrigerant pipe 3, and a check valve 5 in parallel. The expansion valve 4, the heat collector 6, the low-pressure refrigerant pipe 7, the four-way valve 8, and the compressor 1 which are mounted in this order are annularly connected to the main refrigerant circuit, the heat storage tank 9, the water circulation pump 10, the refrigerant-to-water heat exchange. The water circulation circuit is formed by sequentially connecting the vessels 2 in an annular shape.

上記構成により、集熱運転時には、圧縮機1及び水循環
ポンプ10を駆動させることにより、圧縮機1で圧縮され
た高温・高圧な状態の冷媒が、四方弁8を介して、冷媒
対水熱交換器2に流入し、ここで伝熱関係にある水循環
回路の給湯水を加熱し、凝縮液化する。又加熱された給
湯水は水循環ポンプ10によって送水され、蓄熱槽9上部
に流入する。凝縮された冷媒は高圧冷媒配管3を通り、
逆止弁5を並列に装着した膨張弁4に至る、ここで冷媒
は逆止弁5を流れることができず、膨張弁4を減圧され
ながら通過し、低温,低圧な状態で集熱器6に流入す
る。集熱器6に流入した冷媒は、太陽熱及び大気熱より
吸熱し、蒸発気化する。気化した冷媒は、低圧冷媒配管
7を通り、四方弁8を介して、圧縮機1に再び吸入され
る構成になっており、この冷媒のサイクルが蓄熱槽9の
給湯水を加熱するようになっている。
With the above configuration, during heat collection operation, by driving the compressor 1 and the water circulation pump 10, the high-temperature, high-pressure refrigerant compressed by the compressor 1 exchanges heat with the refrigerant via the four-way valve 8. The hot water supplied to the water circulation circuit, which flows into the vessel 2 and has a heat transfer relationship, is heated and condensed and liquefied. The heated hot water is sent by the water circulation pump 10 and flows into the upper part of the heat storage tank 9. The condensed refrigerant passes through the high pressure refrigerant pipe 3,
The refrigerant reaches the expansion valve 4 in which the check valve 5 is installed in parallel, where the refrigerant cannot flow through the check valve 5, passes through the expansion valve 4 while being decompressed, and the heat collector 6 is kept in a low temperature and low pressure state. Flow into. The refrigerant flowing into the heat collector 6 absorbs heat from solar heat and atmospheric heat and evaporates. The vaporized refrigerant is configured to be sucked into the compressor 1 again through the low-pressure refrigerant pipe 7 and the four-way valve 8, and the refrigerant cycle heats the hot water in the heat storage tank 9. ing.

しかし、集熱器6が着霜状態になると著しく集熱能力が
低下する。そこで、この霜を除霜し、さらに集熱を続け
るのである。
However, when the heat collector 6 is in a frosted state, the heat collecting ability is significantly reduced. Therefore, this frost is defrosted and heat collection is continued.

除霜運転時には集熱器6の着霜状態を、集熱器6入口の
冷媒温度から温度センサー18が検知し、制御器19へ信号
を伝送する。制御器19は四方弁8に通電し切り替えるこ
とにより、冷媒を可逆的に循環せしめ、集熱器6を除霜
する。すなわち、圧縮機1で圧縮された高温・高圧な状
態の冷媒は、四方弁8が切り替わっているので、冷媒対
水熱交換器2に流入せず、集熱運転時の低圧冷媒配管7
(以降、すべて低圧冷媒配管と称す)を通り、集熱器6
へ送られる。集熱器6は、着霜状態にあるので、冷媒は
霜に放熱し、融解しながら凝縮液化する。凝縮された冷
媒は、膨張弁4を容易に通過しないが、並列に装着され
ている逆止弁5を通り、集熱運転時の高圧冷媒配管3
(以降、すべて高圧冷媒と称す)を流れ、冷媒対水熱交
換器2に流入する(ただし、除霜運転時は冷媒と給湯水
は同一方向に流れている)。集熱器6で放熱した冷媒
は、冷媒対水熱交換器2に水循環ポンプ10によって送水
される給湯水より低温になっているので、伝熱関係にあ
る給湯水よりわずかに加熱される(この時、当然、給湯
水は放熱しているので、温度が下がった状態で、蓄熱槽
9の上部に送水されている。)。冷媒対水熱交換器2を
出た冷媒は、四方弁8を介して、圧縮機1に再び吸入さ
れる構成になっており、この冷媒のサイクルが集熱器6
を除雪するようになっており、従来の太陽熱利用給湯装
置は、前記集熱運転と除霜運転とを繰り返すことで、蓄
熱槽9内の給湯水全体を徐々に昇温するのである。
During the defrosting operation, the frosting state of the heat collector 6 is detected by the temperature sensor 18 from the refrigerant temperature at the inlet of the heat collector 6, and a signal is transmitted to the controller 19. The controller 19 energizes and switches the four-way valve 8 to reversibly circulate the refrigerant and defrost the heat collector 6. That is, the high-temperature / high-pressure refrigerant compressed by the compressor 1 does not flow into the refrigerant-to-water heat exchanger 2 because the four-way valve 8 is switched, and the low-pressure refrigerant pipe 7 during the heat collecting operation is used.
(Hereinafter referred to as low-pressure refrigerant pipes) and passes through the heat collector 6
Sent to. Since the heat collector 6 is in a frosted state, the refrigerant radiates heat to the frost and condenses and liquefies while melting. The condensed refrigerant does not easily pass through the expansion valve 4, but passes through the check valve 5 mounted in parallel, and the high-pressure refrigerant pipe 3 during the heat collecting operation
(Hereinafter, referred to as high-pressure refrigerant) and flows into the refrigerant-to-water heat exchanger 2 (however, during defrosting operation, the refrigerant and the hot water supply flow in the same direction). The heat radiated by the heat collector 6 has a temperature lower than that of the hot water supplied to the refrigerant-to-water heat exchanger 2 by the water circulation pump 10, and therefore is slightly heated by the hot water having a heat transfer relationship (this At this time, of course, the hot water is radiating heat, so that it is being sent to the upper part of the heat storage tank 9 in a state where the temperature has dropped.). The refrigerant discharged from the refrigerant-to-water heat exchanger 2 is configured to be sucked again into the compressor 1 via the four-way valve 8, and the cycle of this refrigerant is the collector 6
The conventional solar-powered hot water supply device gradually increases the temperature of the entire hot water in the heat storage tank 9 by repeating the heat collecting operation and the defrosting operation.

発明が解決しようとする問題点 しかしながら、前記のような構成では、除霜運転時に蓄
熱槽9上部に、温度が低い給湯水が流入するので、蓄熱
槽9に一定温度の給湯水を蓄えることができず、蓄熱槽
9より安定して湯温の給湯水が、特に低外気環境下にお
いて、供給し得ないのである。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in the above-described configuration, since hot water having a low temperature flows into the upper part of the heat storage tank 9 during the defrosting operation, it is possible to store hot water having a constant temperature in the heat storage tank 9. This cannot be done, and the hot-water supply water having a stable hot water temperature cannot be supplied from the heat storage tank 9, especially in a low outside air environment.

つまり、除霜運転時は、前述のごとく、集熱器6を除霜
するために、冷媒の温度は、霜の融解熱や、低外気環境
への放熱などで、氷点下に下がる場合がある。この低温
な冷媒は、冷媒対水熱交換器2に流入した時、それまで
加熱されていた蓄熱槽9の下部より水循環ポンプ10によ
って送水される給湯水よりも、低い温度である。このた
め、冷媒対水熱交換器2内では、わずかであるが、給湯
水より冷媒へ伝熱する。したがって、給湯水の温度は、
蓄熱槽9下部の状態よりも低下し、蓄熱槽9上部へ送り
出されるのである。
That is, during the defrosting operation, as described above, the temperature of the refrigerant may drop below the freezing point due to the heat of frost melting or heat dissipation to a low outside air environment in order to defrost the heat collector 6. When this low-temperature refrigerant flows into the refrigerant-to-water heat exchanger 2, it has a lower temperature than the hot water supplied by the water circulation pump 10 from the lower part of the heat storage tank 9 which has been heated until then. For this reason, in the refrigerant-to-water heat exchanger 2, heat is slightly transferred from the hot water to the refrigerant. Therefore, the temperature of the hot water is
It is lower than the state of the lower part of the heat storage tank 9, and is sent out to the upper part of the heat storage tank 9.

一方、除霜運転が終了し、再び、集熱運転を開始した
時、蓄熱槽9上部へは、蓄熱槽9下部より送水され冷媒
対水熱交換器2にて加熱された給湯水が、送り出される
ため、蓄熱槽9内では積層な状態に給湯水が蓄えられて
しまう。
On the other hand, when the defrosting operation is finished and the heat collecting operation is started again, the hot water supplied from the lower part of the heat storage tank 9 and heated by the refrigerant-to-water heat exchanger 2 is sent to the upper part of the heat storage tank 9. Therefore, in the heat storage tank 9, the hot water is stored in a stacked state.

ところが、本太陽熱利用給湯装置は蓄熱槽9に蓄えられ
た給湯水を供給する場合、蓄熱槽9の底部に設けられた
給水口12より給水し、蓄熱槽9の最上部に設けられた給
湯口11より給湯する構成なので、温度の分布が積層な状
態で蓄熱槽9に蓄えられた時、一定の温度での給湯が、
困難という問題点を有していた。
However, in the case of supplying the hot water stored in the heat storage tank 9, the solar water heating system of the present invention supplies water from the water supply port 12 provided at the bottom of the heat storage tank 9, and the hot water supply port provided at the top of the heat storage tank 9. Since it is configured to supply hot water from 11, the hot water is supplied at a constant temperature when stored in the heat storage tank 9 in a laminated state of temperature distribution.
It had the problem of difficulty.

本従来例は、除霜運転時に、水循環ポンプ10を運転する
としたけれども、水循環ポンプ10を除霜運転時に停止し
ても、冷媒対水熱交換器2に流入する冷媒の温度は、氷
点下以下になる得るので、冷媒対水熱交換器2内に残留
した給湯水は凍結し、集熱運転を再開した場合に、正常
な運転が出来ないばかりか、冷媒対水熱交換器2自身、
及び他の機器を破壊する恐れがあり、従来例に示す構成
においては、つねに水循環ポンプ10を運転する必要があ
るので、前記問題点を解決し得ない、したがって、ここ
では特に述べていない。
In this conventional example, the water circulation pump 10 is operated during the defrosting operation, but even if the water circulation pump 10 is stopped during the defrosting operation, the temperature of the refrigerant flowing into the refrigerant-to-water heat exchanger 2 remains below the freezing point. Therefore, the hot water supply remaining in the refrigerant-to-water heat exchanger 2 freezes, and when the heat collecting operation is restarted, not only normal operation cannot be performed, but also the refrigerant-to-water heat exchanger 2 itself,
In addition, in the configuration shown in the conventional example, it is necessary to always operate the water circulation pump 10, and therefore the above problems cannot be solved. Therefore, it is not particularly described here.

本発明は、かかる従来の問題点を解消するもので、太陽
熱利用給湯装置において、外気環境の変動にかかわら
ず、蓄熱槽内の給湯水の温度分布が積層な状態に蓄わえ
られるのを防止することを目的とする。
The present invention solves such a conventional problem, and prevents the temperature distribution of the hot water in the heat storage tank from being accumulated in a stacked state in the solar heat utilizing hot water supply apparatus, regardless of changes in the outside air environment. The purpose is to do.

問題点を解決するための手段 上記問題点を解決するために、本発明の太陽熱利用給湯
装置は、圧縮機の吐出配管と、逆止弁と冷媒対水熱交換
器とを接続する配管の間に、減圧機構を介してホットガ
スバイパス回路と、冷媒対水熱交管器と高圧冷媒配管と
を接続する配管と、圧縮機の吸入配管の間に、電磁弁を
介した除霜運転時吸入回路を設け、除霜運転を行うため
には従来のものと同様に四方弁を切り替え冷媒を可逆的
に循環せしめる必要がある。本発明は、この四方弁だけ
でなく水循環境ポンプと電磁弁と下記のごとく温度セン
サーの検知信号で制御するものである。すなわち制御方
法として (1)四方弁を切り替え冷媒を可逆的に循環させる。
Means for Solving the Problems In order to solve the above problems, the solar heat utilizing hot water supply device of the present invention has a discharge pipe of a compressor and a pipe connecting a check valve and a refrigerant-to-water heat exchanger. In addition, a hot gas bypass circuit via a pressure reducing mechanism, a pipe connecting the refrigerant-to-water heat exchanger and the high-pressure refrigerant pipe, and a suction pipe during the defrosting operation via a solenoid valve between the suction pipe of the compressor. In order to perform the defrosting operation, it is necessary to switch the four-way valve to reversibly circulate the refrigerant as in the conventional one. The present invention controls not only the four-way valve but also a water circulation boundary pump, a solenoid valve, and a detection signal from a temperature sensor as described below. That is, as the control method, (1) the four-way valve is switched to circulate the refrigerant reversibly.

(2)同時に水循環ポンプを停止させる。(2) At the same time, stop the water circulation pump.

(3)同時に除霜運転時回路の電磁弁を開く。(3) At the same time, open the solenoid valve of the circuit during defrosting operation.

という構成を備えたものである。It is equipped with the configuration.

作用 本発明は上記した構成によって、除霜運転時にも冷媒対
水熱交換器内に、氷点下以上の冷媒力が流入するので、
水循環ポンプを停止していても、冷媒対水熱交換器内の
給湯水が凍結することがなく、したがって、除霜運転が
終了し、集熱運転が開始されたのち、冷媒対水熱交換器
内の給湯水を、十分に加熱してから蓄熱槽の上部に送り
出すことが出来るので、蓄熱槽内の給湯水の温度分布が
積層な状態に蓄えられることを、確実に防止できるので
ある。
Action The present invention, due to the above-described configuration, in the refrigerant-to-water heat exchanger even during the defrosting operation, since the refrigerant force below the freezing point flows in,
Even when the water circulation pump is stopped, the hot water supply water in the refrigerant-to-water heat exchanger does not freeze, so the defrosting operation ends and the heat collection operation starts, then the refrigerant-to-water heat exchanger. Since the hot water in the inside can be sent out to the upper part of the heat storage tank after being sufficiently heated, it is possible to reliably prevent the temperature distribution of the hot water in the heat storage tank from being accumulated in a laminated state.

実施例 以下、本発明の実施例を添付図面にもとづいて説明す
る。
Embodiments Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図において、本発明のポイントとなる、太陽熱利用
給湯装置の構成について詳細に説明する。なお、第2図
に示す従来例と同一部品については、同一番号を付し、
その説明は省略する。
In FIG. 1, the structure of the solar heat utilizing hot water supply device, which is the point of the present invention, will be described in detail. The same parts as those of the conventional example shown in FIG.
The description is omitted.

本実施例の冷媒が循環する経路には圧縮機1の吐出配管
と、逆止弁11と冷媒対水熱交換器2とを接続する配管の
間に、キャピラリーチューブ等の減圧機構を介したホッ
トガスバイパス回路16が、四方弁8と逆止弁11をバイパ
スするように設けられている。また、冷媒対水熱交換器
2と高圧冷媒配管3とを接続する配管と、圧縮機1の吸
入配管の間には、除霜運転時のみ開放する電磁弁15を介
した、除霜運転時吸入回路17が設けられており、これら
によって、本実施例における冷媒の循環する経路は、集
熱運転時は実線で、除霜運転時は破線の矢印に示される
ものである。
In the route in which the refrigerant of the present embodiment circulates, between the discharge pipe of the compressor 1 and the pipe connecting the check valve 11 and the refrigerant-to-water heat exchanger 2, a hot air is introduced via a pressure reducing mechanism such as a capillary tube. A gas bypass circuit 16 is provided so as to bypass the four-way valve 8 and the check valve 11. In addition, between the pipe connecting the refrigerant-to-water heat exchanger 2 and the high-pressure refrigerant pipe 3 and the suction pipe of the compressor 1 via a solenoid valve 15 which is opened only during the defrosting operation, during the defrosting operation. The suction circuit 17 is provided, and the path through which the refrigerant circulates in this embodiment is shown by the solid line during the heat collecting operation and by the broken arrow during the defrosting operation.

すなわち、集熱運転時は、圧縮機1を吐出した冷媒は、
ホットガスバイパス回路16に設けられた減圧機構によっ
て、そのほとんどが、四方弁8と逆止弁11を介する主冷
媒循環回路を流れる。又、除霜運転時吸入回路17の電磁
弁15は閉じているので、従来例と同様の循環経路を流れ
る。このため従来例の持つ、蓄熱槽9に蓄える給湯水の
加熱能力と同等以上の能力は維持している。
That is, during the heat collecting operation, the refrigerant discharged from the compressor 1 is
Due to the pressure reducing mechanism provided in the hot gas bypass circuit 16, most of it flows through the main refrigerant circulation circuit via the four-way valve 8 and the check valve 11. In addition, since the solenoid valve 15 of the suction circuit 17 is closed during the defrosting operation, it flows through the same circulation path as the conventional example. Therefore, the heating capacity of the conventional example, which is equal to or higher than the heating capacity of the hot water supply stored in the heat storage tank 9, is maintained.

一方、除霜運転時は温度センサー18の検知信号により通
電された四方弁8は切り替わり、冷媒の循環経路も集熱
運転時と逆転するのであるが、同時に、水循環ポンプ10
は停止され、除霜運転時吸入回路17に備えられた電磁弁
15が開らくのである。本実施例では、圧縮機1を吐出し
た冷媒の一部は、四方弁8に流入せず、ホットガスバイ
パス回路16に分流される。四方弁8に流入した冷媒は、
この後、従来例と同様に、集熱器6に流入し除霜を行な
う。又、ホットガスバイパス回路16に分流された高温・
高圧な状態の冷媒は、冷媒対水熱交換器2に流入する。
冷媒対水熱交換器2を流出した冷媒は、高圧冷媒配管3
の手前すなわち、除霜運転時吸入回路17の入口まで流れ
る。この時、集熱器6を除霜した冷媒は、逆止弁5を通
過し、高圧冷媒配管3を流れて、やはり除霜運転時吸入
回路17の入口に至っている。除霜運転時吸入回路17の電
磁弁15は、除霜運転時には開放になっているので、これ
ら2方向より流れてきた冷媒は、合流し、一気に圧縮機
1の吸入配管へ流入するのである。
On the other hand, during the defrosting operation, the four-way valve 8 energized by the detection signal of the temperature sensor 18 is switched, and the circulation path of the refrigerant is also reversed from that during the heat collection operation.
Is stopped and the solenoid valve provided in the suction circuit 17 during defrosting operation
15 opens. In this embodiment, part of the refrigerant discharged from the compressor 1 does not flow into the four-way valve 8 but is split into the hot gas bypass circuit 16. The refrigerant flowing into the four-way valve 8 is
After that, as in the conventional example, it flows into the heat collector 6 to perform defrosting. In addition, the high temperature shunted to the hot gas bypass circuit 16
The high-pressure refrigerant flows into the refrigerant-to-water heat exchanger 2.
The refrigerant flowing out of the refrigerant-to-water heat exchanger 2 has a high-pressure refrigerant pipe 3
Before, i.e., to the inlet of the suction circuit 17 during the defrosting operation. At this time, the refrigerant that has defrosted the heat collector 6 passes through the check valve 5, flows through the high pressure refrigerant pipe 3, and reaches the inlet of the suction circuit 17 during defrosting operation as well. Since the solenoid valve 15 of the suction circuit 17 during the defrosting operation is open during the defrosting operation, the refrigerants flowing from these two directions merge and flow into the suction pipe of the compressor 1 at once.

上記構成において、先に述べたとおり、集熱運転時の加
熱能力の低下がなく、除霜運転時に、冷媒対水熱交換器
2に流入する冷媒の温度を、長時間にわたって、氷点下
以上に維持することが可能である。
In the above configuration, as described above, there is no decrease in heating capacity during the heat collecting operation, and during defrosting operation, the temperature of the refrigerant flowing into the refrigerant-to-water heat exchanger 2 is maintained above the freezing point for a long time. It is possible to

このため、除霜運転が開始された場合に、水循環ポンプ
10を停止し、蓄熱槽9上部に、従来例にみられたよう
な、温度の低い給湯水を送り出すことがなく、さらに、
冷媒対水熱交換器2内に残留する給湯水を凍結させ、機
器を破損に至らしめることが、確実に防止できる。この
結果、除霜運転が、頻繁に行なわれても、温度分布が積
層な状態な給湯水が、蓄熱槽9に、蓄えられることがな
いという効果がある。
Therefore, when the defrosting operation is started, the water circulation pump
10 is stopped, the hot water having a low temperature as in the conventional example is not sent to the upper part of the heat storage tank 9, and further,
It is possible to reliably prevent the hot water supply remaining in the refrigerant-to-water heat exchanger 2 from being frozen and causing damage to the equipment. As a result, even if the defrosting operation is frequently performed, there is an effect that hot water having a laminated temperature distribution is not stored in the heat storage tank 9.

ここで、本実施例と従来例とを比較する、なお集熱運転
時の能力は、前者のものが同等もしくは優れているの
で、ここでは特に述べない。
Here, the present example and the conventional example are compared with each other, and the ability during the heat collection operation is equal to or superior to that of the former one, and therefore is not particularly described here.

第3図は、除霜運転時の、圧縮機消費電力特性を示した
ものであり、横軸には除霜量を、縦軸には除霜運転中の
圧縮機1の入力を示す。この特性の測定は、乾球温度1.
5℃,湿球温度0.5℃,相対湿度85%,風速0m/sの外気環
境の条件で行った。又、前者の水循環ポンプ10は停止状
態,圧縮機の容量は12cc、後者の水循環ポンプ10は作動
状態,圧縮機の容量は8ccである。
FIG. 3 shows the compressor power consumption characteristics during the defrosting operation, where the horizontal axis shows the defrosting amount and the vertical axis shows the input of the compressor 1 during the defrosting operation. Dry-bulb temperature 1.
The test was performed under the conditions of an outside air environment of 5 ° C, a wet bulb temperature of 0.5 ° C, a relative humidity of 85%, and a wind speed of 0 m / s. The former water circulation pump 10 is stopped, the capacity of the compressor is 12 cc, the latter water circulation pump 10 is in operation, and the capacity of the compressor is 8 cc.

また、第3図の曲線Aは、本実施例の除霜量と、圧縮機
1入力の特性を示すもので、点Bは、従来例が、0.4kg
除霜するのに要する入力を示す。
A curve A in FIG. 3 shows the defrosting amount of this embodiment and the characteristic of the compressor 1 input, and the point B is 0.4 kg in the conventional example.
Indicates the input required to defrost.

この第3図より、次のような傾向が把握できる、本実施
例の除霜運転では、曲線Aより集熱器6に着霜した霜0.
4kgを除霜するのに、圧縮機1の入力がおよそ31Wで、従
来例のもの(点B)と同等であることが明らかである。
From FIG. 3, the following tendency can be understood, and in the defrosting operation of the present embodiment, the frost on the heat collector 6 from the curve A is 0.
It is clear that the input of the compressor 1 is about 31 W for defrosting 4 kg, which is equivalent to that of the conventional example (point B).

これは、圧縮機1の容量を増大し、ホットガスバイパス
回路16内のキャピラリーチューブ14を任意に設定するこ
とで、除霜運転時に圧縮機1を吐出した冷媒を、ホット
ガスバイパス回路16に分流しながら、集熱器6へ従来例
と同等以上の冷媒を流入させたためである。これによ
り、水循環ポンプ2が停止状態でも冷媒対水熱交換器2
に残留する給湯水を凍結させることなく、従来例と同量
の霜を除霜し、又、除霜に要する圧縮機1への入力の増
加を防止することが可能なのである。いいかえれば、除
霜の効率を低下させることなく、蓄熱槽9に温度分布が
積層な状態で、給湯水を蓄えることを防ぐのである。
By increasing the capacity of the compressor 1 and arbitrarily setting the capillary tube 14 in the hot gas bypass circuit 16, the refrigerant discharged from the compressor 1 during the defrosting operation is distributed to the hot gas bypass circuit 16. This is because a refrigerant equal to or more than that in the conventional example was made to flow into the heat collector 6 while flowing. Thereby, even if the water circulation pump 2 is stopped, the refrigerant-to-water heat exchanger 2
It is possible to defrost the same amount of frost as in the conventional example and to prevent an increase in the input to the compressor 1 required for defrosting, without freezing the hot water supply remaining in the. In other words, it is possible to prevent the hot water from being stored in the heat storage tank 9 in a laminated temperature distribution without lowering the defrosting efficiency.

さらに、除霜運転中は、水循環ポンプ10は停止している
ので、電力を消費しない。したがって、除霜運転時の総
消費電力が、低減するという効果も得られるのである。
Further, during the defrosting operation, the water circulation pump 10 is stopped, so that it does not consume power. Therefore, the effect of reducing the total power consumption during the defrosting operation can be obtained.

発明の効果 以上のように本発明の太陽熱利用給湯装置によれば、次
の効果が得られる。
EFFECTS OF THE INVENTION As described above, according to the solar heat utilizing hot water supply device of the present invention, the following effects can be obtained.

(1)四方弁を切り替え冷媒の循環が逆となる除霜運転
中でも、水循環ポンプを停止し、温度の低い給湯水を、
蓄熱槽上部へ送り出さないとしているので、低外気環境
において、除霜運転が頻繁に繰り返えされても、蓄熱槽
に、給湯水の温度分布が積層な状態で、蓄えることがな
く、つねに一定の温度での給湯が可能という効果があ
る。
(1) Even during the defrosting operation in which the four-way valve is switched and the refrigerant circulation is reversed, the water circulation pump is stopped to supply hot water having a low temperature.
Since it is not sent to the upper part of the heat storage tank, even if the defrosting operation is repeated frequently in a low outside air environment, the temperature distribution of the hot water supply is not accumulated in the heat storage tank in a stacked state, and it is always constant. There is an effect that hot water can be supplied at the temperature.

(2)除霜運転中,水循環ポンプが停止し、冷媒対水熱
交換器内に給湯水が残留するが、圧縮機を吐出した高温
・高圧な状態の冷媒が、ホットガスバイパス回路を一定
量流れ、冷媒対水熱交換器内へ流入するので、冷媒と伝
熱関係にある給湯水は凍結せず、機器の破損を防止する
ことができる。
(2) During the defrosting operation, the water circulation pump stops and hot water remains in the refrigerant-to-water heat exchanger, but the high-temperature, high-pressure refrigerant discharged from the compressor causes a certain amount of hot gas bypass circuit. Since it flows and flows into the refrigerant-to-water heat exchanger, the hot-water supply water that has a heat transfer relationship with the refrigerant does not freeze, and damage to the equipment can be prevented.

(3)除霜運転中、水循環ポンプを停止するので、除霜
の効率を低下させることがなく、除霜運転中の総消費電
力を低減することができる。
(3) Since the water circulation pump is stopped during the defrosting operation, it is possible to reduce the total power consumption during the defrosting operation without lowering the efficiency of the defrosting.

【図面の簡単な説明】 第1図は本発明の一実施例の太陽熱利用給湯装置の構成
図、第2図は従来例を説明するための構成図、第3図は
従来例と、本発明の一実施例の効果を比較したグラフで
ある。 1……圧縮機、2……冷媒対水熱交換器、3……高圧冷
媒配管、4……膨張弁、5……逆止弁、6……集熱器、
7……低圧冷媒配管、8……四方弁、9……蓄熱槽、10
……水循環ポンプ、11……給湯口、12……給水口、13…
…逆止弁、14……キャピラリーチューブ、15……電磁
弁、16……ホットガスバイパス回路、17……除霜運転時
吸入回路、18……温度センサー、19……制御器。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a configuration diagram of a solar water heating system according to an embodiment of the present invention, FIG. 2 is a configuration diagram for explaining a conventional example, and FIG. 3 is a conventional example and the present invention. It is a graph which compared the effect of one Example. 1 ... Compressor, 2 ... Refrigerant-to-water heat exchanger, 3 ... High-pressure refrigerant pipe, 4 ... Expansion valve, 5 ... Check valve, 6 ... Heat collector,
7 ... Low-pressure refrigerant pipe, 8 ... Four-way valve, 9 ... Heat storage tank, 10
…… Water circulation pump, 11 …… Hot water inlet, 12 …… Water inlet, 13…
Check valve, 14 Capillary tube, 15 Solenoid valve, 16 Hot gas bypass circuit, 17 Inhalation circuit during defrosting operation, 18 Temperature sensor, 19 Controller.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】圧縮機、四方弁、逆止弁、冷媒対水熱交換
器、膨張弁、集熱器、四方弁、圧縮機の順に環状連結さ
れた主冷媒循環回路と、この主冷媒循環回路の集熱器の
入り口に温度センサーを備えるとともに、蓄熱槽、水循
環ポンプ、及び冷媒対水熱交換器とを順に、環状連結し
てなる水循環回路を構成し、前記主冷媒循環回路の四方
弁、逆止弁と並列に、減圧機構を具備するホットガスバ
イパス回路を設けるとともに、前記冷媒対水熱交換器の
出口と、前記圧縮機の吸入管を、電磁弁を具備する除霜
運転時吸入回路で連結し、除霜運転を行う時、前記温度
センサーの検知信号により、前記四方弁を切替え、前記
水循環ポンプを停止させ、前記電磁弁を開くように制御
するようにしてなる、太陽熱利用給湯装置。
1. A main refrigerant circulation circuit in which a compressor, a four-way valve, a check valve, a refrigerant-to-water heat exchanger, an expansion valve, a heat collector, a four-way valve and a compressor are annularly connected in this order, and this main refrigerant circulation. A temperature sensor is provided at the inlet of the heat collector of the circuit, and a heat storage tank, a water circulation pump, and a refrigerant-to-water heat exchanger are sequentially connected to form a water circulation circuit, and the four-way valve of the main refrigerant circulation circuit is formed. , A hot gas bypass circuit having a pressure reducing mechanism is provided in parallel with the check valve, and the outlet of the refrigerant-to-water heat exchanger and the suction pipe of the compressor are sucked at the time of defrosting operation by using a solenoid valve. When using a circuit to connect the circuit and perform a defrosting operation, the four-way valve is switched by the detection signal of the temperature sensor, the water circulation pump is stopped, and the solenoid valve is controlled to open. apparatus.
JP61248616A 1986-10-20 1986-10-20 Solar water heater Expired - Lifetime JPH0686958B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61248616A JPH0686958B2 (en) 1986-10-20 1986-10-20 Solar water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61248616A JPH0686958B2 (en) 1986-10-20 1986-10-20 Solar water heater

Publications (2)

Publication Number Publication Date
JPS63101661A JPS63101661A (en) 1988-05-06
JPH0686958B2 true JPH0686958B2 (en) 1994-11-02

Family

ID=17180767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61248616A Expired - Lifetime JPH0686958B2 (en) 1986-10-20 1986-10-20 Solar water heater

Country Status (1)

Country Link
JP (1) JPH0686958B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101154698B1 (en) 2010-01-14 2012-06-08 (주)티엠테크 Solar collecting apparatus
JP5570531B2 (en) * 2010-01-26 2014-08-13 三菱電機株式会社 Heat pump equipment
CN101867325A (en) * 2010-06-08 2010-10-20 孙国锋 Cooling device of solar photovoltaic generation system
CN102865621B (en) * 2012-10-12 2015-01-07 陕西华夏新能源科技有限公司 System and method for solar energy centralized hot water supply for high-rise residence
CN109708380B (en) * 2019-01-05 2023-10-31 天津大学 Cold storage refrigeration system based on solar PV/T technology and working method
CN112050399B (en) * 2020-09-08 2021-09-28 青岛海信日立空调系统有限公司 Air conditioner

Also Published As

Publication number Publication date
JPS63101661A (en) 1988-05-06

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