JPS6157985B2 - - Google Patents
Info
- Publication number
- JPS6157985B2 JPS6157985B2 JP342281A JP342281A JPS6157985B2 JP S6157985 B2 JPS6157985 B2 JP S6157985B2 JP 342281 A JP342281 A JP 342281A JP 342281 A JP342281 A JP 342281A JP S6157985 B2 JPS6157985 B2 JP S6157985B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- coil
- refrigeration
- air conditioning
- heat recovery
- 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
Links
- 238000005057 refrigeration Methods 0.000 claims description 41
- 238000004378 air conditioning Methods 0.000 claims description 39
- 239000007788 liquid Substances 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 25
- 238000011084 recovery Methods 0.000 claims description 24
- 230000005494 condensation Effects 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 6
- 239000003507 refrigerant Substances 0.000 description 31
- 238000007710 freezing Methods 0.000 description 17
- 230000008014 freezing Effects 0.000 description 17
- 239000007789 gas Substances 0.000 description 17
- 230000008020 evaporation Effects 0.000 description 11
- 238000001704 evaporation Methods 0.000 description 11
- 238000004781 supercooling Methods 0.000 description 11
- 239000002918 waste heat Substances 0.000 description 10
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000013611 frozen food Nutrition 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Central Heating Systems (AREA)
Description
【発明の詳細な説明】
この発明は冷凍冷蔵排熱を利用した暖房装置に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating device that utilizes waste heat from freezing and refrigeration.
例えばスーパーマーケツトと称される大規模小
売店舗では、多量の生鮮食料品や冷凍食料品を取
扱つているので、冷凍冷蔵設備を備え、併せて店
舗内の空調を行なうために空調設備を備えている
のが通常である。ところで従来、このような店舗
においては、冷凍冷蔵設備と空調設備とをそれぞ
れ独立に設け、冷凍冷蔵排熱を大気に放熱する一
方、ヒートポンプにより暖房を行なう場合には蒸
発熱を大気から吸収するように構成していた。し
かしながら、このような各設備の構成では、暖房
を行なう場合、ヒートポンプの一部を構成する蒸
発器(蒸発コイル)における冷媒の蒸発温度を、
大気との温度差をある一定以上にするために例え
ば−5〜−10℃程度の低い温度に設定しなければ
ならないので、凝縮温度と蒸発温度との温度差が
大きくなる関係上空調用圧縮機の圧縮比が高く、
それに伴つて電力消費量が相当多くなるなどの問
題があつた。 For example, large-scale retail stores called supermarkets handle large quantities of fresh and frozen foods, so they are equipped with freezing and refrigeration equipment, and are also equipped with air conditioning equipment to air-condition the store. is normal. Conventionally, in such stores, freezing and refrigeration equipment and air conditioning equipment were installed independently, and waste heat from freezing and refrigeration was radiated to the atmosphere, while when heating was performed using a heat pump, evaporation heat was absorbed from the atmosphere. It was composed of However, in such equipment configurations, when performing heating, the evaporation temperature of the refrigerant in the evaporator (evaporation coil) that constitutes a part of the heat pump is
In order to keep the temperature difference with the atmosphere above a certain level, the temperature must be set to a low temperature of, for example, -5 to -10 degrees Celsius, so the temperature difference between the condensing temperature and the evaporation temperature becomes large. has a high compression ratio,
This has led to problems such as a considerable increase in power consumption.
そこで従来、冷凍または冷蔵用圧縮機の吐出口
とその吐出口に接続したコンデンサーとの間に放
熱コイルを介装し、かつその放熱コイルを例えば
空調用ダクト内に配置し、冷凍または冷蔵排熱に
より店舗内の暖房をすることが行なわれている。
しかしながら、冷凍もしくは冷蔵排熱により店舗
内を十分暖房するためには、冷媒の凝縮温度を相
当高く(例えば40〜50℃)しなければならないの
で、たとえ昼間のみ暖房を行なうにしても所要動
力を大きくし、それに伴つて消費電力が多くなる
問題があり、また、凝縮温度を高めるために圧縮
比を高くしなければならないから、圧縮機の耐用
寿命が短かくなるなどの問題があり、そのため従
来では冷凍冷蔵設備をあまり大容量とせずに暖房
に要する全熱量のうち一部を冷凍排熱とし、不足
する熱量を他の暖房用熱源で補つているのが実情
である。 Conventionally, therefore, a heat dissipation coil is interposed between the discharge port of a refrigeration or refrigeration compressor and a condenser connected to the discharge port, and the heat dissipation coil is placed, for example, in an air conditioning duct. The interior of the store is heated by heating.
However, in order to sufficiently heat the inside of a store using waste heat from freezing or refrigeration, the condensing temperature of the refrigerant must be raised considerably (e.g. 40 to 50 degrees Celsius), so even if heating is performed only during the daytime, the required power will be reduced. There are problems such as increasing the size of the compressor, resulting in increased power consumption, and the need to increase the compression ratio to increase the condensing temperature, which shortens the service life of the compressor. The current situation is that the capacity of refrigeration equipment is not very large, and part of the total heat required for heating is used as waste heat from refrigeration, and the insufficient amount of heat is supplemented by other heat sources for heating.
この発明は上記の事情に鑑みてなされたもの
で、冷凍冷蔵排熱を有効に利用し、消費電力の低
減化を図ることのできる暖房装置を提供すること
を目的とするものである。 The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a heating device that can effectively utilize waste heat from freezing and refrigeration and reduce power consumption.
以下この発明の一実施例を添付の図面を参照し
て説明する。第1図はこの発明の一実施例を原理
的に示すものであつて、まず空調すなわち暖房を
行なうための系路について説明すると、空調用圧
縮機1を吐出口側に四方切換弁2を介して空調用
コイル3が接続され、その空調用コイル3には逆
止弁4および凝縮弁5を介して受液器6が接続さ
れており、その凝縮弁5により冷媒(例えばフロ
ンR−22(商品名))の凝縮温度Tcを暖房に必要
な所定温度に設定するとともに、空調用コイル3
にて顕熱および潜熱を放熱して凝縮液化した冷媒
を受液器6に流入させるようになつている。その
受液器6には、アキユムレーター7内に設けた熱
交換用コイル8が逆止弁9を介して接続され、ま
た熱交換用コイル8は膨張弁10を介して熱回収
コイル11に接続され、さらにその熱回収コイル
11は逆止弁12および前記四方切換弁2を経て
吸入圧力弁13に接続されている。前記熱回収コ
イル11は所定のダクト14内に配置されてお
り、後述するようにそのダクト14内に同様に配
置された冷凍および冷蔵側の放熱コイルとの間で
空気を介して熱授受するようになつており、また
前記吸入圧力弁13により冷媒の蒸発温度Teを
所定の上限温度に設定するようになつている。そ
して、前記吸入圧力弁13は前記アキユムレータ
ー7に接続されるとともにそのアキユムレーター
7は空調用圧縮機1の吸込口側に接続されてお
り、したがつてアキユムレーター7において、前
記膨張弁10および熱回収コイル11を経て蒸発
気化した冷媒により熱交換用コイル8内の液状冷
媒を冷却し、同時に空調用圧縮機1の吸入ガスを
昇温するように構成されている。なお、前記熱交
換用コイル8の流出側管路は途中で分岐し、膨張
弁15を介して液過冷却用熱交換器16に接続さ
れ、ここで冷凍冷蔵側の冷媒を過冷却するように
なつており、そしてその液過冷却用熱変換器16
は前記吸入圧力弁13に接続されている。 An embodiment of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows the principle of an embodiment of the present invention. First, the system for air conditioning or heating will be explained. An air conditioning compressor 1 is connected to the discharge port side via a four-way switching valve 2. An air conditioning coil 3 is connected to the air conditioning coil 3, and a liquid receiver 6 is connected to the air conditioning coil 3 via a check valve 4 and a condensing valve 5. The condensing temperature Tc of the product name)) is set to a predetermined temperature required for heating, and the air conditioning coil 3
The condensed and liquefied refrigerant is made to flow into the receiver 6 by dissipating sensible heat and latent heat. A heat exchange coil 8 provided in an accumulator 7 is connected to the liquid receiver 6 via a check valve 9, and the heat exchange coil 8 is connected to a heat recovery coil 11 via an expansion valve 10. Further, the heat recovery coil 11 is connected to a suction pressure valve 13 via a check valve 12 and the four-way switching valve 2. The heat recovery coil 11 is arranged in a predetermined duct 14, and as described later, it exchanges heat with the refrigeration and refrigeration side heat radiation coils similarly arranged in the duct 14 through the air. The evaporation temperature Te of the refrigerant is set to a predetermined upper limit temperature by the suction pressure valve 13. The suction pressure valve 13 is connected to the accumulator 7 and the accumulator 7 is connected to the suction port side of the air conditioning compressor 1. Therefore, in the accumulator 7, the expansion valve 10 and the heat recovery coil The liquid refrigerant in the heat exchange coil 8 is cooled by the refrigerant evaporated through the refrigerant 11, and at the same time, the temperature of the intake gas of the air conditioning compressor 1 is raised. In addition, the outflow side pipe line of the heat exchange coil 8 branches in the middle and is connected to a liquid supercooling heat exchanger 16 via an expansion valve 15, so that the refrigerant on the freezing and refrigerating side is supercooled here. and its liquid supercooling heat converter 16
is connected to the suction pressure valve 13.
つぎに、冷凍用の系路および冷蔵用の系路につ
いて説明すると、冷凍圧縮機17の吐出口側に排
熱コイル18、凝縮圧力弁19およびコンデンサ
ー20が順次接続されている。その排熱コイル1
8は前記ダクト14内の前記熱回収コイル11の
近傍に配置されており、凝縮圧力弁19にてホツ
トガスの温度を所定の温度tcに設定するととも
に、ホツトガスの有する熱をダクト14内を流れ
る空気を介して前記熱回収コイル11内の冷媒ガ
スに蒸発熱として与えるようになつている。前記
コンデンサー20は受液器21に接続されるとと
もに、その受液器21には、前記液過冷却用熱交
換器16内に配置された液過冷却用コイル22が
接続され、またその液過冷却用コイル22は膨張
弁23および冷却コイル24を順次経て前記冷凍
用圧縮機17の吸込口側に接続されている。 Next, the refrigeration system and the refrigeration system will be explained. A heat exhaust coil 18, a condensing pressure valve 19, and a condenser 20 are sequentially connected to the discharge port side of the refrigeration compressor 17. The heat exhaust coil 1
8 is placed near the heat recovery coil 11 in the duct 14, and sets the temperature of the hot gas to a predetermined temperature tc with the condensing pressure valve 19, and transfers the heat of the hot gas to the air flowing in the duct 14. The heat of evaporation is given to the refrigerant gas in the heat recovery coil 11 through the heat recovery coil 11. The condenser 20 is connected to a liquid receiver 21, and a liquid supercooling coil 22 disposed in the liquid supercooling heat exchanger 16 is connected to the liquid receiver 21. The cooling coil 22 is connected to the suction port side of the refrigeration compressor 17 via an expansion valve 23 and a cooling coil 24 in this order.
一方、冷蔵用の系路は上述した冷凍用の系路と
同様に構成されており、冷蔵用圧縮機25の吐出
口側には、前記ダクト14内の熱回収コイル11
の近傍に配置された排熱コイル26、およびホツ
トガスの温度を所定の温度tc′に設定するための
凝縮圧力弁27が順次接続され、またその凝縮圧
力弁27はコンデンサー28を介して受液器29
に接続され、さらにその受液器29には、前記液
過冷却用熱交換器16内に配置された液過冷却用
コイル30が接続されるとともに、その液過冷却
用コイル30は膨張弁31および冷却コイル32
を順次経て前記冷蔵用圧縮機25の吸込口側に接
続されている。 On the other hand, the refrigeration system is configured similarly to the above-mentioned refrigeration system, and a heat recovery coil 11 in the duct 14 is disposed on the discharge port side of the refrigeration compressor 25.
A heat exhaust coil 26 disposed near the hot gas and a condensing pressure valve 27 for setting the temperature of the hot gas to a predetermined temperature tc' are connected in sequence, and the condensing pressure valve 27 is connected to the liquid receiver via a condenser 28. 29
Further, a liquid supercooling coil 30 disposed in the liquid supercooling heat exchanger 16 is connected to the liquid receiver 29, and the liquid supercooling coil 30 is connected to an expansion valve 31. and cooling coil 32
It is connected to the suction port side of the refrigeration compressor 25 through sequentially.
第2図は上記装置のうち空調用コイル3、熱回
収コイル11、ダクト14、各排熱コイル18、
26および各コンデンサー20,28等の配設位
置の一例を示す略解図であつて、空調用コイル3
は被暖房室である売場33内に設置したパツケー
ジ34内に収容されており、そのパツケージ34
には空調用ダクト35が接続して設けられ、売場
33内の空気をその空調用ダクト35を介してフ
アン36により循環させることにより売場33内
を暖房するようになつている。また、前記熱回収
コイル11および各排熱コイル18,26を収容
したダクト14は機械室37内に配設され、その
ダクト14内に設けたフアン38により機械室3
7内の空気を排熱コイル18,26側から熱回収
コイル11側に向けてダクト14内を流動させる
ようになつている。さらに、機械室37と前記空
調用ダクト35とは連通ダクト39にて接続さ
れ、機械室37内の温暖空気を連通ダクト39内
に設けた1方向ダンパー40およびフアン41を
介して空調用ダクト35すなわち売場33内に送
り込むように構成され、またさらに売場33と機
械室37とは帰還ダクト42にて接続され、売場
33内の空気をその帰還ダクト42内に設けたフ
アン43および1方向ダンパー44を介して機械
室37内に戻すように構成されている。したがつ
て熱回収コイル11および各排熱コイル18,2
6を配置した機械室37と売場33との間には循
環給気経路が形成されている。なお、前記各コン
デンサー20,28は屋外に設置され、大気から
凝縮熱を吸収するようになつている。また、機械
室37には換気フアン45が取付けられ、暖房時
において外気温度が機械室37内よりも高くなつ
た場合にその換気フアン45を起動して外気を機
械室37内に取り入れるように構成されている。 Figure 2 shows the air conditioning coil 3, heat recovery coil 11, duct 14, heat exhaust coils 18,
26 and each condenser 20, 28, etc., and is a schematic diagram showing an example of the arrangement position of the air conditioning coil 3.
is housed in a package cage 34 installed in the sales floor 33, which is a heated room.
An air conditioning duct 35 is connected to the air conditioning duct 35, and the air inside the sales floor 33 is circulated through the air conditioning duct 35 by a fan 36 to heat the interior of the sales floor 33. Further, the duct 14 accommodating the heat recovery coil 11 and each of the heat exhaust coils 18 and 26 is disposed in a machine room 37, and a fan 38 provided in the duct 14 is used to cool the machine room 37.
7 is made to flow through the duct 14 from the heat exhaust coils 18 and 26 side toward the heat recovery coil 11 side. Further, the machine room 37 and the air conditioning duct 35 are connected by a communication duct 39, and the warm air in the machine room 37 is transferred to the air conditioning duct 35 through a one-way damper 40 and a fan 41 provided in the communication duct 39. In other words, the sales floor 33 and the machine room 37 are connected by a return duct 42, and the air in the sales floor 33 is fed into the return duct 42 by a fan 43 and a one-way damper 44. It is configured to be returned into the machine room 37 via. Therefore, the heat recovery coil 11 and each heat exhaust coil 18, 2
A circulating air supply path is formed between the machine room 37 in which the air conditioner 6 is arranged and the sales floor 33. Note that each of the condensers 20 and 28 is installed outdoors to absorb condensation heat from the atmosphere. Further, a ventilation fan 45 is attached to the machine room 37, and is configured to activate the ventilation fan 45 to take outside air into the machine room 37 when the outside air temperature becomes higher than the inside of the machine room 37 during heating. has been done.
つぎに上記装置の作用について説明すると、ま
ず冷凍側および冷蔵側の各凝縮圧力弁19,27
を、ホツトガスの温度tc,tc′が冬期における外
気温度よりもある程度以上高くかつ冷凍および冷
蔵用圧縮機17,25の圧縮比が左程高くならな
い程度(例えば15〜20℃)となるように設定し、
他方空調側の凝縮圧力弁5を、空調用コイル3に
おけるホツトガスの温度が暖房に必要な温度(例
えば40〜45℃)となるように設定する。この場
合、空調側における冷媒の蒸発熱を従来装置のよ
うに大気から吸収するとすれば、冬期における外
気温度を0℃程度に想定する必要があるから冷媒
の蒸発温度を−5〜−10℃程度の低い温度に設定
する必要があるが、上記装置では前記熱回収コイ
ル11の周囲を流れる空気が前記排熱コイル1
8,26にて例えば20℃程度に暖められているの
で、空調側の前記吸入圧力弁13を吸入ガス温度
が10℃程度になるように設定することができる。 Next, to explain the operation of the above device, first, each condensing pressure valve 19, 27 on the freezing side and the refrigeration side
are set so that the hot gas temperatures tc and tc' are higher than the outside air temperature in winter by a certain degree, and the compression ratios of the refrigeration and refrigeration compressors 17 and 25 are not too high (for example, 15 to 20 degrees Celsius). death,
On the other hand, the condensing pressure valve 5 on the air conditioning side is set so that the temperature of the hot gas in the air conditioning coil 3 is the temperature required for heating (for example, 40 to 45 DEG C.). In this case, if the heat of evaporation of the refrigerant on the air conditioning side is absorbed from the atmosphere like in conventional equipment, it is necessary to assume that the outside air temperature in winter is around 0°C, so the evaporation temperature of the refrigerant should be around -5 to -10°C. However, in the above device, the air flowing around the heat recovery coil 11 is set to a low temperature of the heat exhaust coil 1.
8 and 26, the suction pressure valve 13 on the air conditioning side can be set so that the suction gas temperature is about 10°C.
前記各弁5,13,19,27を上述のように
設定した後、各圧縮機1,17,25を起動する
と、まず空調用圧縮機1により圧縮された冷媒ガ
スが四方切換弁2の流路D−Eを経て空調用コイ
ル3に到り、この場合冷媒ガスは凝縮圧力弁5に
て設定された温度Tcまで昇温されるとともに、
空調用コイル3においてその周囲を流れる空気に
対して顕熱および潜熱を放熱して凝縮液化し、そ
の結果売場33内が暖房される。液化した冷媒の
一部はアキユムレーター7内の熱交換用コイル8
を介して膨張弁10に到り、ここで減圧膨張し、
その際冷凍および冷蔵側の排熱コイル18,26
内の冷媒ガスが凝縮圧力弁19,27にて設定さ
れた温度tc,tc′まで昇温されているので、冷凍
および冷蔵側の排熱を熱回収コイル11にて蒸発
熱として吸収し、吸入圧力弁13にて設定した温
度Teで蒸発気化する。そして、気化した冷媒ガ
スは四方切換弁2の流路C−Sを経て吸入圧力弁
13に到り、しかる後アキユムレーター7にて熱
交換用コイル8内の液状冷媒を過冷却すると同時
に若干昇温され、そして空調用圧縮機1に吸入さ
れる。他方、熱交換用コイル8にて過冷却された
液状冷媒の他の一部は他方の膨張弁15を経て液
過冷却用熱交換器16内で蒸発気化し、その液過
冷却用熱交換器16内を冷却し、そして気化した
冷媒は吸入圧力弁13およびアキユムレーター7
を介して空調用圧縮機1に吸入される。 After setting each of the valves 5, 13, 19, and 27 as described above, when each compressor 1, 17, and 25 is started, first, the refrigerant gas compressed by the air conditioning compressor 1 flows through the four-way switching valve 2. The refrigerant gas reaches the air conditioning coil 3 via path D-E, and in this case, the refrigerant gas is heated to the temperature Tc set by the condensing pressure valve 5, and
The air-conditioning coil 3 radiates sensible heat and latent heat to the air flowing around it, condenses and liquefies the air, and as a result, the inside of the sales floor 33 is heated. A part of the liquefied refrigerant is transferred to the heat exchange coil 8 in the accumulator 7.
to the expansion valve 10, where it is decompressed and expanded,
At that time, the heat exhaust coils 18, 26 on the freezing and refrigeration side
Since the temperature of the refrigerant gas inside has been raised to the temperature tc, tc' set by the condensing pressure valves 19, 27, the waste heat from the freezing and refrigeration side is absorbed as heat of evaporation by the heat recovery coil 11 and is then inhaled. It evaporates at a temperature Te set by the pressure valve 13. Then, the vaporized refrigerant gas reaches the suction pressure valve 13 via the flow path C-S of the four-way switching valve 2, and then supercools the liquid refrigerant in the heat exchange coil 8 in the accumulator 7, and at the same time slightly raises the temperature. The air is then sucked into the air conditioning compressor 1. On the other hand, the other part of the liquid refrigerant supercooled in the heat exchange coil 8 passes through the other expansion valve 15 and evaporates in the liquid supercooling heat exchanger 16. 16, and the vaporized refrigerant flows through the suction pressure valve 13 and the accumulator 7.
The air is sucked into the air conditioning compressor 1 through the air conditioning compressor 1.
また、冷凍圧縮機17により圧縮されて凝縮圧
力弁19にて設定した温度tcまで昇温された冷媒
ガスは、排熱コイル18にて凝縮放熱した後液化
し、コンデンサー20において外気により過冷却
され受液器21に到る。そして、液化した冷媒は
前記液過冷却用熱交換器16内に設けた液過冷却
用コイル22により過冷却され、しかる後膨張弁
23および冷却コイル24を経て蒸発気化した後
冷凍用圧縮機17に吸入される。 Further, the refrigerant gas compressed by the refrigeration compressor 17 and heated to the temperature tc set by the condensing pressure valve 19 is liquefied after condensing and dissipating heat in the heat exhaust coil 18, and is supercooled by outside air in the condenser 20. It reaches the liquid receiver 21. Then, the liquefied refrigerant is supercooled by the liquid supercooling coil 22 provided in the liquid supercooling heat exchanger 16, and then evaporated through the expansion valve 23 and the cooling coil 24, and then evaporated into the refrigeration compressor 17. is inhaled.
さらに、冷蔵用圧縮機25にて凝縮圧力弁27
で設定した温度tc′まで圧縮された冷媒ガスは、
排熱コイル26にて凝縮放熱した後液化し、コン
デンサー28にて外気により過冷却され、そして
液過冷却用コイル30により過冷却された液状冷
媒は膨張弁31および冷却コイル32を経て蒸発
気化した後、冷蔵用圧縮機25に吸入される。 Furthermore, the condensing pressure valve 27 in the refrigeration compressor 25
The refrigerant gas compressed to the temperature tc′ set in
After condensing and dissipating heat in the heat exhaust coil 26, the liquid refrigerant is liquefied, supercooled by outside air in the condenser 28, and supercooled by the liquid supercooling coil 30. The liquid refrigerant passes through the expansion valve 31 and the cooling coil 32 and is evaporated. Thereafter, it is sucked into the refrigeration compressor 25.
しかして、上記の装置によれば、冷凍冷蔵排熱
を各排熱コイル18,26および熱回収コイル1
1を介し空調側の冷媒に与えるようにしたので、
空調側の冷媒の蒸発温度Teを外気から吸熱する
従来装置と比べて相当高く(例えば10℃程度)設
定することができ、したがつて圧縮比が低下する
ので暖房に要する動力、消費電力を従来装置に比
べて著しく低減することができる。また、冷凍冷
蔵側の冷媒の凝縮温度tc,tc′を20〜25℃程度の
比較的低い温度に設定することができるので、
1kW当りの冷凍冷蔵能力が向上し、消費電力の
低減化を図ることができるうえに、圧縮比が低く
なるので圧縮機の耐用寿命が延び、保守も容易に
なる。さらに、排熱コイル18,26の周囲を通
過する空気を第2図に示すように売場33等建屋
内で循環するようにしてあるので、夜間に暖房装
置を止めた場合、冷凍冷蔵排熱を建屋内に蓄熱し
ておくことができるので、暖房再開時に建屋内の
温度を所期の温度まで速やかに上げることがで
き、したがつて立上りが良くかつエネルギーロス
の少ない暖房装置とすることができる。またさら
に、冷凍冷蔵側の凝縮圧力弁19,27により凝
縮圧力を高めれば、ホツトガスの温度が上昇し、
それに伴つて排熱量換言すれれば空調側の回収熱
量が増大するので、暖房装置の能力を短時間のう
ちに最大限まで上げることができる。 According to the above device, waste heat from freezing and refrigeration is transferred to each of the waste heat coils 18, 26 and the heat recovery coil 1.
1 to the refrigerant on the air conditioning side,
The evaporation temperature Te of the refrigerant on the air conditioning side can be set much higher (for example, about 10 degrees Celsius) compared to conventional equipment that absorbs heat from outside air, and as a result, the compression ratio decreases, so the power and power consumption required for heating can be reduced compared to conventional equipment. This can be significantly reduced compared to other devices. In addition, since the condensation temperatures tc and tc' of the refrigerant on the freezing and refrigeration side can be set to a relatively low temperature of about 20 to 25 degrees Celsius,
The refrigeration capacity per kW is improved, reducing power consumption, and the lower compression ratio extends the compressor's service life and makes maintenance easier. Furthermore, since the air passing around the heat exhaust coils 18 and 26 is circulated within the sales floor 33 building as shown in Figure 2, when the heating system is turned off at night, the waste heat from freezing and refrigeration can be removed. Since heat can be stored inside the building, the temperature inside the building can be quickly raised to the desired temperature when heating is restarted, and the heating system can therefore start up quickly and reduce energy loss. . Furthermore, if the condensation pressure is increased by the condensation pressure valves 19 and 27 on the freezing and refrigeration side, the temperature of the hot gas will rise,
Accordingly, the amount of exhaust heat, in other words, the amount of heat recovered on the air conditioning side increases, so that the capacity of the heating device can be increased to the maximum in a short time.
なお、前記空調用圧縮機1にて圧縮し、さらに
凝縮液化させた冷媒を空調用コイル3に対して膨
張弁を介して送り込むように構成すれば、上記装
置を冷房用に転用することができることは勿論で
ある。 Note that if the refrigerant compressed by the air conditioning compressor 1 and further condensed and liquefied is sent to the air conditioning coil 3 via an expansion valve, the above device can be used for cooling purposes. Of course.
以上の説明で明らかなようにこの発明の暖房装
置によれば、冷凍冷蔵排熱を空調側の冷媒に与え
るように構成したので、その冷媒の蒸発温度を相
当高めることができ、したがつて負荷が小さく、
成積係数が大きい状態で運転できるため、電力消
費量を従来と比べて著しく低減することができ
る。また、冷凍冷蔵側の冷媒の凝縮温度を20℃程
度の比較的低い温度に設定することができるの
で、冷凍冷蔵能力が向上し、併せて電力消費量を
低減することができ、同時に圧縮比を小さくし得
るので圧縮機の長寿命化を図り、保守を容易なも
のとすることができる。さらにこの発明では、常
時運転される冷凍冷蔵系の排熱を、開店時など人
間の活動時のみに使用される被暖房室は循環給気
経路を介して送るように構成してあるから、暖房
の特に必要のない夜間などの場合にも排熱を暖房
用の熱として蓄えるおくことができるため、熱回
収をより効率良く行なうことができるとともに、
暖房の立上がりを良くすることができる。したが
つて、この発明の暖房装置によれば、小さい容量
で広い空間を暖房することができ、かつ熱の有効
利用を図ることができるため電力消費量を低減す
ることができる等の効果がある。 As is clear from the above explanation, according to the heating device of the present invention, the waste heat from freezing and refrigeration is applied to the refrigerant on the air conditioning side, so the evaporation temperature of the refrigerant can be considerably increased, and therefore the load is small,
Since it can be operated with a large product coefficient, power consumption can be significantly reduced compared to conventional methods. In addition, the condensation temperature of the refrigerant on the freezing and refrigeration side can be set to a relatively low temperature of about 20°C, which improves the freezing and refrigeration capacity and reduces power consumption.At the same time, the compression ratio can be increased. Since it can be made smaller, the life of the compressor can be extended and maintenance can be made easier. Furthermore, in this invention, the exhaust heat from the constantly operating refrigeration system is sent to heated rooms that are used only during human activities such as when opening a store, through the circulating air supply path. Since exhaust heat can be stored as heat for heating even when it is not particularly needed, such as at night, heat can be recovered more efficiently, and
This can improve the heating start-up. Therefore, according to the heating device of the present invention, it is possible to heat a wide space with a small capacity, and since it is possible to use heat effectively, it is possible to reduce power consumption, etc. .
第1図はこの発明の一実施例を原理的に示す系
路図、第2図は空調用コイル、熱回収コイル、排
熱コイルおよびコンデンサーの設置位置を示す略
解図である。
1……空調用圧縮機、3……空調用コイル、5
……凝縮圧力弁、6……受液器、10……膨張
弁、11……熱回収コイル、17……冷凍圧縮
機、18,26……排熱コイル、19,27……
凝縮圧力弁、20,28……コンデンサー、25
……冷蔵用圧縮機。
FIG. 1 is a system diagram showing the principle of an embodiment of the present invention, and FIG. 2 is a schematic diagram showing the installation positions of an air conditioning coil, a heat recovery coil, a heat exhaust coil, and a condenser. 1... Air conditioning compressor, 3... Air conditioning coil, 5
... Condensing pressure valve, 6 ... Liquid receiver, 10 ... Expansion valve, 11 ... Heat recovery coil, 17 ... Refrigeration compressor, 18, 26 ... Exhaust heat coil, 19, 27 ...
Condensing pressure valve, 20, 28...Condenser, 25
...Refrigerating compressor.
Claims (1)
給気経路中に配置した暖房コイルを接続するとと
もにその暖房コイルに凝縮圧力弁を介して受液器
を接続し、その受液器に膨張弁を介して熱回収コ
イルを接続し、またその熱回収コイルを前記空調
用圧縮機の吸込口側に接続し、さらに前記熱回収
コイルの近傍に、冷凍もしくは冷蔵用圧縮機の吐
出口とコンデンサーとの間に介装された排熱コイ
ルを、前記熱回収コイルとの間で空気を介して熱
授受し得るよう配設し、さらにその排熱コイルと
前記コンデンサーとの間に凝縮圧力弁を介装し、
かつ前記熱回収コイルおよび排熱コイルを前記被
暖房室への循環給気経路中に配置してなることを
特徴とする暖房装置。1 Connect a heating coil placed in the air supply path into the room to be heated to the discharge port side of the air conditioning compressor, connect a liquid receiver to the heating coil via a condensing pressure valve, and connect the liquid receiver to the heating coil via a condensing pressure valve. A heat recovery coil is connected to the air conditioner via an expansion valve, and the heat recovery coil is connected to the suction port side of the air conditioning compressor, and a discharge port of the refrigeration or refrigeration compressor is connected near the heat recovery coil. A heat exhaust coil is interposed between the heat recovery coil and the condenser, and is arranged so that heat can be exchanged between the heat recovery coil and the condenser, and a condensation pressure is maintained between the heat recovery coil and the condenser. Interpose a valve,
A heating device characterized in that the heat recovery coil and the exhaust heat coil are disposed in a circulating air supply path to the heated room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP342281A JPS57117757A (en) | 1981-01-13 | 1981-01-13 | Heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP342281A JPS57117757A (en) | 1981-01-13 | 1981-01-13 | Heater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57117757A JPS57117757A (en) | 1982-07-22 |
| JPS6157985B2 true JPS6157985B2 (en) | 1986-12-09 |
Family
ID=11556935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP342281A Granted JPS57117757A (en) | 1981-01-13 | 1981-01-13 | Heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57117757A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0634686U (en) * | 1991-03-01 | 1994-05-10 | 群馬県娯楽機事業協同組合 | Amusement machine structure |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04306461A (en) * | 1991-04-02 | 1992-10-29 | Hitachi Air Conditioning & Refrig Co Ltd | refrigerator |
| JP4258363B2 (en) * | 2003-02-20 | 2009-04-30 | 三菱電機株式会社 | Refrigeration air conditioner, operation method of refrigeration air conditioner |
| JP6548369B2 (en) * | 2014-08-18 | 2019-07-24 | 株式会社クボタ | Heat pump type air conditioner |
| JP7472744B2 (en) * | 2020-09-30 | 2024-04-23 | 株式会社デンソー | Refrigeration Cycle Equipment |
-
1981
- 1981-01-13 JP JP342281A patent/JPS57117757A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0634686U (en) * | 1991-03-01 | 1994-05-10 | 群馬県娯楽機事業協同組合 | Amusement machine structure |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57117757A (en) | 1982-07-22 |
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