JPH02157544A - Cooling and heating system - Google Patents
Cooling and heating systemInfo
- Publication number
- JPH02157544A JPH02157544A JP31462888A JP31462888A JPH02157544A JP H02157544 A JPH02157544 A JP H02157544A JP 31462888 A JP31462888 A JP 31462888A JP 31462888 A JP31462888 A JP 31462888A JP H02157544 A JPH02157544 A JP H02157544A
- Authority
- JP
- Japan
- Prior art keywords
- heating
- cooling
- main
- heat exchanger
- auxiliary
- 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.)
- Granted
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 134
- 238000010438 heat treatment Methods 0.000 title claims abstract description 128
- 239000007788 liquid Substances 0.000 claims abstract description 97
- 239000003507 refrigerant Substances 0.000 claims abstract description 59
- 238000004891 communication Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 65
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000004378 air conditioning Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000005338 heat storage Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000110 cooling liquid Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分腎〉
本発明は、ビルなどにおいて、各階の各部屋に設置され
た個別空気調和機の熱交換器に冷却冷媒または加熱冷媒
を流して冷房および暖房のいずれをも行うことができる
ように構成した冷暖房システムに関する。[Detailed Description of the Invention] <Industrial Applications> The present invention provides cooling and cooling in buildings etc. by flowing a cooling refrigerant or a heating refrigerant through the heat exchanger of an individual air conditioner installed in each room on each floor. The present invention relates to a heating and cooling system configured to perform both heating and heating.
〈従来の技術〉
従来のこの種の空気調和システムとしては、各階の各部
屋に設置された個別空気調和機に冷房用熱交換器と暖房
用熱交換器とを備え、冷房用熱交換器に対し、冷房用凝
縮器と圧縮機とを備えた冷房ユニットを冷房用冷媒配管
を介して連通接続し、一方、暖房用熱交換器に対し、暖
房用蒸発器と圧縮機とを備えた冷房ユニットを暖房用冷
媒配管を介して連通接続し、冷房用凝縮器と冷房用熱交
換器とにわたって冷却冷媒を強制的に循環流動すること
により冷房運転を行い、また、暖房用蒸発器と暖房用熱
交換器とにわたって加熱冷媒を強制的に循環流動するこ
とにより暖房運転を行うように構成していた。<Conventional technology> In conventional air conditioning systems of this type, individual air conditioners installed in each room on each floor are equipped with a cooling heat exchanger and a heating heat exchanger; On the other hand, a cooling unit equipped with a cooling condenser and a compressor is connected via a cooling refrigerant pipe, and a cooling unit equipped with a heating evaporator and a compressor is connected to the heating heat exchanger. are connected via heating refrigerant piping, and cooling operation is performed by forcibly circulating the cooling refrigerant across the cooling condenser and cooling heat exchanger. It was configured to perform heating operation by forcibly circulating heating refrigerant across the exchanger.
ところが、負荷の高い冷房運転において、多数の熱交換
器に冷却冷媒を強制的に流動するためには、圧縮機とし
て掻めて能力の大きい圧縮機が必要であり、設備費はも
とより稼働のための動力費が増大して不経済になる欠点
があった。However, in order to force the cooling refrigerant to flow through a large number of heat exchangers during high-load cooling operations, a compressor with a large capacity is required, which increases not only equipment costs but also operational costs. The disadvantage was that the power cost increased, making it uneconomical.
そこで、ビルの屋上などの塔屋に冷房用凝縮器を設置す
るとともに、ビルの地下室などに暖房用蒸発器を設置し
、かつ、冷房用凝縮器と冷房用冷媒配管および冷房用熱
交換器とにわたって冷房用冷媒を、一方、暖房用蒸発器
と暖房用冷媒配管および暖房用熱交換器とにわたって暖
房用冷媒をそれぞれ密閉状態で流動するように構成し、
冷房用冷媒として、冷房用熱交換器での熱交換に伴って
液体から蒸気に相変化する冷媒を使用するとともに、冷
房用mll1!器と冷房用熱交換器との間に、液体に相
変化した冷媒を冷房用熱交換器に移送するに足るヘッド
差を備え、一方、暖房用冷媒として、暖房用熱交換器で
の熱交換に伴って蒸気から液体に相変化する冷媒を使用
するとともに、暖房用蒸発器と暖房用熱交換器との間に
、液体に相変化した冷媒を暖房用蒸発器に移送するに足
るヘッド差を備え、冷房用冷媒および暖房用冷媒のいず
れをも、自然的にWi環流動するように構成したシステ
ムが開発されている。Therefore, a cooling condenser is installed on a tower such as the roof of a building, a heating evaporator is installed in the basement of the building, and the cooling condenser is connected to the cooling refrigerant piping and the cooling heat exchanger. On the other hand, the cooling refrigerant is configured to flow through the heating evaporator, the heating refrigerant piping, and the heating heat exchanger in a sealed state, respectively;
As a cooling refrigerant, a refrigerant whose phase changes from liquid to vapor as a result of heat exchange in a cooling heat exchanger is used, and the cooling mll1! There is a head difference between the refrigerant and the cooling heat exchanger that is sufficient to transfer the phase-changed refrigerant to the cooling heat exchanger. In addition to using a refrigerant that changes phase from vapor to liquid as the temperature increases, a sufficient head difference is created between the heating evaporator and the heating heat exchanger to transfer the refrigerant that has changed phase to liquid to the heating evaporator. A system has been developed in which both the cooling refrigerant and the heating refrigerant are configured to naturally circulate.
〈発明が解決しようとする課題〉
しかしながら、先に説明した従来例、ならびに、開発さ
れた従来例のいずれにおいても、冷房用および暖房用そ
れぞれに専用の熱交換器と冷媒配管が必要で、冷房用の
熱交換器と冷媒配管においては、冷房負荷のピークに合
った能力のものを設け、一方、暖房用の熱交換器と冷媒
配管においては、暖房負荷のピークに合った能力のもの
を設けなければならず、画然交換器それぞれとして大型
になるとともに、両冷媒配管それぞれとして大径のもの
が必要になり、イニシャルコストが高価になる欠点があ
った。<Problems to be Solved by the Invention> However, in both the conventional example described above and the conventional example developed, dedicated heat exchangers and refrigerant piping are required for cooling and heating, and cooling For heat exchangers and refrigerant piping for air conditioning, install one with a capacity that matches the peak of the cooling load.On the other hand, for the heat exchanger and refrigerant piping for heating, install one that has a capacity that matches the peak of the heating load. As a result, each exchanger becomes large, and both refrigerant pipes each require large diameter pipes, resulting in high initial cost.
本発明は、このような事情に鑑みてなされたものであっ
て、冷房および暖房のいずれをも自然循環によって動力
費少なく行うことができながら、熱交換器および冷媒配
管の小型化を図り、イニシャルコストを低減できるよう
にすることを目的とする。The present invention has been made in view of these circumstances, and it is possible to perform both cooling and heating at low power costs through natural circulation, while reducing the size of the heat exchanger and refrigerant piping, and reducing the initial cost. The purpose is to reduce costs.
〈課題を解決するための手段〉
本発明の冷暖房システムは、上述のような目的を達成す
るために、各階に設けられた個別空気調和機それぞれに
主熱交換器と補助熱交換器とを備え、主液配管と主ガス
配管に、前記主熱交換器それぞれを並列に連通接続し、
前記主液配管に、冷房用主液配管を介して冷房用凝縮器
を、暖房用主液配管を介して暖房用蒸発器をそれぞれ連
通接続するとともに、前記主ガス配管に、冷房用主ガス
配管を介して冷房用凝縮器を、暖房用主ガス配管を介し
て暖房用蒸発器をそれぞれ連通接続し、かつ、補助液配
管と補助ガス配管に、前記補助熱交換器それぞれを並列
に連通接続し、前記補助液配管を前記冷房用主液配管お
よび暖房用主液配管それぞれに連通接続するとともに、
前記補助ガス配管を前記冷房用主ガス配管および暖房用
主ガス配管それぞれに連通接続し、前記主液配管および
主ガス配管に対して、前記冷房用凝縮器のみを連通接続
する冷房運転モードと前記暖房用蒸発器のみを連通接続
する暖房運転モードとに切り換える運転モード切り換え
機構を設けるとともに、前記冷房用凝縮器および暖房用
蒸発器それぞれから前記主熱交換器および補助熱交換器
それぞれに冷媒を密閉状態で循環流動可能に構成し、そ
の冷媒として、前記冷房運転モードにおける前記主熱交
換器での熱交換に伴って液体から蒸気に相変化するとと
もに前記暖房運転モードにおける前記主熱交換器での熱
交換に伴って蒸気から液体に相変化する冷媒を使用し、
前記冷房用凝縮器と前記主熱交換器との間に、液体に相
変化した冷媒を前記熱交換器に移送するに足るヘッド差
を備えるとともに、前記主熱交換器と前記暖房用蒸発器
との間に、液体に相変化した冷媒を前記暖房用蒸発器に
移送するに足るヘッド差を備えて構成する。<Means for Solving the Problems> In order to achieve the above-mentioned purpose, the heating and cooling system of the present invention includes a main heat exchanger and an auxiliary heat exchanger for each individual air conditioner provided on each floor. , each of the main heat exchangers is connected in parallel to the main liquid pipe and the main gas pipe,
A cooling condenser is connected to the main liquid pipe via a main liquid pipe for cooling, and a heating evaporator is connected to the main liquid pipe for heating, and a main gas pipe for cooling is connected to the main gas pipe. The cooling condenser is connected in communication with the heating evaporator through the heating main gas piping, and the auxiliary heat exchangers are connected in parallel with the auxiliary liquid piping and the auxiliary gas piping. , connecting the auxiliary liquid pipe to each of the main liquid pipe for cooling and the main liquid pipe for heating;
A cooling operation mode in which the auxiliary gas piping is connected to each of the main gas piping for cooling and the main gas piping for heating, and only the cooling condenser is connected in communication to the main liquid piping and the main gas piping; An operation mode switching mechanism is provided for switching to a heating operation mode in which only the heating evaporator is connected in communication, and a refrigerant is hermetically sealed from each of the cooling condenser and heating evaporator to the main heat exchanger and the auxiliary heat exchanger. The refrigerant is configured to be able to circulate and flow in the heating operation mode, and as the refrigerant, the phase changes from liquid to vapor as a result of heat exchange in the main heat exchanger in the cooling operation mode, and also in the heating operation mode in the main heat exchanger. Using a refrigerant that changes phase from vapor to liquid as heat is exchanged,
A head difference is provided between the cooling condenser and the main heat exchanger that is sufficient to transfer the refrigerant whose phase has changed to a liquid to the heat exchanger, and a head difference between the main heat exchanger and the heating evaporator is provided. In between, there is a sufficient head difference to transfer the refrigerant whose phase has changed to liquid to the heating evaporator.
く作用〉
上記構成によれば、運転モード切り換え機構の切換えに
より、冷房を主体とした冷房運転モードおよび暖房を主
体とした暖房運転モードそれぞれを得、各季節に合った
冷暖房運転を次のようにして行うことができる。According to the above configuration, by switching the operation mode switching mechanism, a cooling operation mode mainly for cooling and a heating operation mode mainly for heating are obtained, and the heating and cooling operation suitable for each season can be performed as follows. It can be done by
■冷房主体の冷房運転モード
冷媒を、
冷房用凝縮器→冷房用主液配管→主液配管→個別空気調
和機それぞれの主熱交換器→主ガス配管→冷房用主ガス
配管→冷房用凝縮器
と循環流動させて冷房を行うことができる。■Cooling operation mode mainly for cooling Refrigerant: Cooling condenser → Cooling main liquid piping → Main liquid piping → Main heat exchanger of each individual air conditioner → Main gas piping → Cooling main gas piping → Cooling condenser Cooling can be achieved by circulating the fluid.
中間期において、冷房を必要とする部屋と暖房を必要と
する部屋の両方があるような場合にあっては、冷媒の一
部を、
暖房用蒸発器→暖房用主ガス配管→補助ガス配管→個別
空気調和機それぞれの補助熱交換器→補助液配管→暖房
用主液配管→暖房用蒸発器と循環流動させて暖房をも行
うことができる。During the interim period, if there are rooms that require both cooling and heating, a portion of the refrigerant is transferred from the heating evaporator to the heating main gas piping to the auxiliary gas piping. Heating can also be performed by circulating the fluid through the auxiliary heat exchanger of each individual air conditioner → auxiliary liquid piping → main heating liquid piping → heating evaporator.
■暖房主体の暖房運転モード
冷媒を、
暖房用蒸発器→暖房用主ガス配管→主ガス配管→個別空
気調和機それぞれの主熱交換器→主液配管→暖房用主液
配管→暖房用蒸発器
と循1!Jfi動させて暖房を行うことができる。■Heating operation mode mainly for heating Refrigerant heating evaporator → main gas piping for heating → main gas piping → main heat exchanger of each individual air conditioner → main liquid piping → main liquid piping for heating → evaporator for heating And cycle 1! Heating can be performed by moving the Jfi.
中間期にあって、冷房をも必要とする場合には、冷媒の
一部を、
冷房用凝縮器→冷房用主液配管→補助液配管→個別空気
調和機それぞれの補助熱交換器→補助ガス配管→冷房用
主ガス配管→冷房用凝縮器と循環流動させて冷房をも行
うことができる。During the interim period, if cooling is also required, some of the refrigerant is transferred to the cooling condenser → cooling main liquid piping → auxiliary liquid piping → auxiliary heat exchanger for each individual air conditioner → auxiliary gas Cooling can also be performed by circulating the flow from piping to cooling main gas piping to cooling condenser.
〈実施例〉
以下、本発明の実施例を図面に基づいて詳細に説明する
。<Example> Hereinafter, an example of the present invention will be described in detail based on the drawings.
第1図は、本発明に係る冷暖房システムの実施例を示す
全体システム構成図である。FIG. 1 is an overall system configuration diagram showing an embodiment of a heating and cooling system according to the present invention.
この図において、Aは、ビルBの屋上に設置された熱源
であり、微細な氷を製造する製氷機lとその製水itで
得られた微細な氷を供給して蓄える蓄熱槽2とから構成
されている。In this figure, A is a heat source installed on the roof of building B, which is composed of an ice maker 1 that produces fine ice and a heat storage tank 2 that supplies and stores the fine ice obtained by the water maker IT. It is configured.
ビルBの屋上の塔屋内に冷房用凝縮器3が設置され、そ
の冷房用凝縮器3と蓄熱槽2とが循環ポンプ4を介して
連通接続され、蓄熱槽2に蓄えられている冷水を冷房用
凝縮器3に循環供給するように構成されている。A cooling condenser 3 is installed inside the tower on the roof of building B, and the cooling condenser 3 and the heat storage tank 2 are connected through a circulation pump 4 to cool the cold water stored in the heat storage tank 2. It is configured to circulate and supply the water to the condenser 3 for use.
一方、ビルBの各階F・・・の各部屋それぞれなどに、
送風ファン5、主熱交換器6および補助熱交換器7を備
えた個別空気調和機8が設けられている。On the other hand, in each room of each floor F of building B, etc.
A separate air conditioner 8 with a blower fan 5, a main heat exchanger 6 and an auxiliary heat exchanger 7 is provided.
前記主熱交換器6・・・それぞれは、ヘッダー9および
電磁弁10を介して主液配管11に並列に連通接続され
るとともに、ヘッダー12を介して主ガス配管13に並
列に連通接続されている。Each of the main heat exchangers 6 is connected in parallel to the main liquid pipe 11 via a header 9 and a solenoid valve 10, and is also connected in parallel to the main gas pipe 13 via a header 12. There is.
前記主液配管11には、冷房用主液配管14および冷房
用受液器15を介して冷房用凝縮器3が連通接続されて
いる。A cooling condenser 3 is connected to the main liquid pipe 11 via a cooling main liquid pipe 14 and a cooling liquid receiver 15 .
一方、主ガス配管13には、冷房用主ガス配管16を介
して冷房用凝縮器3が連通接続されている。On the other hand, a cooling condenser 3 is connected to the main gas pipe 13 via a main gas pipe 16 for cooling.
ビルBの地下室などに暖房用蒸発器17が設置され、そ
の暖房用蒸発器17と主液配管11とが、暖房用主液配
管18および暖房用受液器19を介して連通接続されて
いる。また、暖房用蒸発器17と主ガス配管13とが、
暖房用主ガス配管20を介して連通接続されている。A heating evaporator 17 is installed in a basement or the like of building B, and the heating evaporator 17 and main liquid pipe 11 are connected to each other via a heating main liquid pipe 18 and a heating liquid receiver 19. . In addition, the heating evaporator 17 and the main gas pipe 13 are
They are connected via a heating main gas pipe 20.
前記補助熱交換器7・・・それぞれは、ヘッダー21お
よび電磁弁22を介して補助液配管23に並列に連通接
続されるとともに、ヘンダー24を介して補助ガス配管
25に並列に連通接続されてい ゛る。Each of the auxiliary heat exchangers 7 is connected in parallel to an auxiliary liquid pipe 23 via a header 21 and a solenoid valve 22, and is also connected in parallel to an auxiliary gas pipe 25 via a header 24. It's true.
前記補助液配管23が冷房用主液配管14および暖房用
主液配管18それぞれに連通接続されるとともに、前記
補助ガス配管25が冷房用主ガス配管16および暖房用
主ガス配管20それぞれに連通接続されている。The auxiliary liquid pipe 23 is connected in communication with the main liquid pipe 14 for cooling and the main liquid pipe 18 for heating, and the auxiliary gas pipe 25 is connected in communication with the main gas pipe 16 for cooling and the main gas pipe 20 for heating, respectively. has been done.
冷房用主液配管14と補助液配管23との接続箇所にお
いて、冷房用主液配管14側に第1の電磁弁26aが、
そして、補助液配管23側に第2の電磁弁26bがそれ
ぞれ介装されている。At the connection point between the cooling main liquid pipe 14 and the auxiliary liquid pipe 23, a first electromagnetic valve 26a is provided on the cooling main liquid pipe 14 side.
A second electromagnetic valve 26b is provided on the side of the auxiliary liquid pipe 23, respectively.
暖房用主液配管18と補助液配管23との接続箇所にお
いて、暖房用主液配管18側に第3の電磁弁26cが、
そして、補助液配管23側に第4の電磁弁26dがそれ
ぞれ介装されている。At the connection point between the heating main liquid pipe 18 and the auxiliary liquid pipe 23, a third solenoid valve 26c is provided on the heating main liquid pipe 18 side.
A fourth electromagnetic valve 26d is interposed on the auxiliary liquid pipe 23 side.
冷房用主ガス配管16と補助ガス配管25との接続箇所
において、冷房用主ガス配管16側に第5の電磁弁26
eが、そして、補助ガス配管25側に第6の電磁弁26
fがそれぞれ介装されてぃ暖房用主ガス配管20と補助
ガス配管25との接続箇所において、暖房用主ガス配管
20側に第7の電磁弁26gが、そして、補助ガス配管
25側に第8の電磁弁26hがそれぞれ介装されている
。A fifth electromagnetic valve 26 is installed on the cooling main gas pipe 16 side at the connection point between the cooling main gas pipe 16 and the auxiliary gas pipe 25.
e, and a sixth solenoid valve 26 on the auxiliary gas pipe 25 side.
At the connection point between the heating main gas piping 20 and the auxiliary gas piping 25, a seventh solenoid valve 26g is installed on the heating main gas piping 20 side, and a seventh solenoid valve 26g is installed on the auxiliary gas piping 25 side. Eight solenoid valves 26h are interposed, respectively.
上記第1ないし第8の電磁弁26a、26b26c、2
6d、26e、26f、26g、26hにより、主液配
管11および主ガス配管13に対して、冷房用凝縮器3
のみを連通接続する冷房運転モードと暖房用蒸発器17
のみを連通接続する暖房運転モードとに切り換え、かつ
、前記冷房運転モードにおいて、暖房用主液配管18を
補助液配管23に連通接続するとともに暖房用主ガス配
管20を補助ガス配管25に連通接続するか、暖房運転
モードにおいて、冷房用主液配管14を補助液配管23
に連通接続するとともに冷房用主ガス配管1Gを補助ガ
ス配管25に連通接続する中間期の運転モードに切換え
るように運転モード切り換え機構が構成されている。The first to eighth solenoid valves 26a, 26b26c, 2
6d, 26e, 26f, 26g, and 26h connect the cooling condenser 3 to the main liquid pipe 11 and the main gas pipe 13.
Cooling operation mode and heating evaporator 17 that connect only
switching to a heating operation mode in which only the main gas pipe for heating is connected in communication with the auxiliary gas pipe 25, and in the cooling operation mode, the main liquid pipe for heating 18 is connected in communication with the auxiliary liquid pipe 23, and the main gas pipe for heating 20 is connected in communication with the auxiliary gas pipe 25. Or, in the heating operation mode, the cooling main liquid pipe 14 is connected to the auxiliary liquid pipe 23.
An operation mode switching mechanism is configured to switch to an intermediate operation mode in which the cooling main gas pipe 1G is connected to the auxiliary gas pipe 25 in communication with the cooling main gas pipe 25.
前述の各液配管11,14.1B、23、各ガス配管1
3,16,20,25、冷房用凝縮器3および暖房用蒸
発器17にわたって、冷房運転モードにおける主熱交換
器6での熱交換に伴って液体から蒸気に相変化するとと
もに暖房運転モードにおける主熱交換器6での熱交換に
伴って蒸気から液体に相変化する冷媒が密閉状態で封入
されている。Each of the aforementioned liquid piping 11, 14.1B, 23, each gas piping 1
3, 16, 20, 25, the cooling condenser 3 and the heating evaporator 17 undergo a phase change from liquid to vapor as a result of heat exchange in the main heat exchanger 6 in the cooling operation mode, and also in the heating operation mode. A refrigerant whose phase changes from vapor to liquid as heat is exchanged in the heat exchanger 6 is sealed in a sealed state.
前記冷房用受液器15および冷房用凝縮器3は、主熱交
換器6・・・および補助熱交換器7・・・それぞれより
も高い位置に設置され、冷房用凝縮器3での凝縮により
蒸気から液体に相変化された冷媒が主熱交換器6・・・
および補助熱交換器7・・・それぞれに流下供給される
とともに、主熱交換器6・・・および補助熱交換器7・
・・それぞれでの熱交換に伴って液体から蒸気に相変化
された冷媒が上昇して冷房用凝縮器3に戻されるに足る
ヘッド差が備えられ、冷房運転モードや中間期の運転モ
ードにおいて、蒸気と液体との相変化により、冷媒が冷
房用凝縮器3と主熱交換器6・・・および補助熱交換器
7・・・それぞれとの間で自然的にva1流動するよう
に構成されている。The cooling liquid receiver 15 and the cooling condenser 3 are installed at a higher position than the main heat exchanger 6 and the auxiliary heat exchanger 7, respectively. The refrigerant whose phase has changed from vapor to liquid is transferred to the main heat exchanger 6...
and the auxiliary heat exchanger 7... are supplied downstream, and the main heat exchanger 6... and the auxiliary heat exchanger 7...
... A sufficient head difference is provided for the refrigerant whose phase has changed from liquid to vapor due to heat exchange in each to rise and return to the cooling condenser 3, and in the cooling operation mode and the intermediate operation mode, Due to the phase change between vapor and liquid, the refrigerant is configured to naturally flow between the cooling condenser 3 and the main heat exchanger 6 and the auxiliary heat exchanger 7. There is.
前記暖房用受液器19および暖房用蒸発器17は、主熱
交換器6・・・および補助熱交換器7・・・それぞれよ
りも低い位置に設置され、暖房用蒸発器17での蒸発に
より液体から蒸気に相変化された冷媒が上昇して主熱交
換器6・・・および補助熱交換器7・・・それぞれに供
給されるとともに、主熱交換器6・・・および補助熱交
換器7・・・それぞれでの熱交換に伴って蒸気から液体
に相変化された冷媒が流下して暖房用蒸発器17に戻さ
れるに足るヘッド差が備えられ、暖房運転モードや中間
期の運転モードにおいて、蒸気と液体との相変化により
、冷媒が暖房用蒸発器17と主熱交換器6・・・および
補助熱交換器7・・・それぞれとの間で自然的に循環流
動するように構成されている。The heating liquid receiver 19 and the heating evaporator 17 are installed at a lower position than the main heat exchanger 6 and the auxiliary heat exchanger 7, respectively, and the evaporation in the heating evaporator 17 causes The refrigerant whose phase has changed from liquid to vapor rises and is supplied to the main heat exchanger 6... and the auxiliary heat exchanger 7, respectively, and the main heat exchanger 6... and the auxiliary heat exchanger 7... A sufficient head difference is provided for the refrigerant whose phase has changed from vapor to liquid due to heat exchange in each to flow down and return to the heating evaporator 17, and the heating operation mode and the intermediate period operation mode are provided. , the refrigerant is configured to naturally circulate and flow between the heating evaporator 17 and the main heat exchanger 6 and the auxiliary heat exchanger 7 due to a phase change between vapor and liquid. has been done.
前記冷媒としてはフロンガスR−22が用いられる。こ
れは、水素、塩素を含んでいて対fL団で分解するため
に、オゾン層を破壊する虞の無い利点を有している。Freon gas R-22 is used as the refrigerant. This has the advantage that it contains hydrogen and chlorine and is decomposed by anti-fL groups, so there is no risk of destroying the ozone layer.
前記電磁弁10・・・、22・・・それぞれは、全開状
態から全閉状態にわたって流量制御可能に構成されてい
て、主熱交換器6・・・および補助熱交換器7・・・そ
れぞれへの冷媒液流入量を調節できるようになっている
。Each of the electromagnetic valves 10..., 22... is configured to be able to control the flow rate from a fully open state to a fully closed state, and is configured to be able to control the flow rate from a fully open state to a fully closed state. The amount of refrigerant liquid inflow can be adjusted.
以上の構成により、次のような各種の運転モードで冷暖
房を行うことができる。なお、第2図において、黒く塗
りつぶした電磁弁は開き状態であることを示している。With the above configuration, heating and cooling can be performed in the following various operation modes. In addition, in FIG. 2, the black solenoid valves are shown to be in the open state.
■冷房主体の冷房運転モード
第2図の(a)に示すように、第1の電磁弁26aと第
5の電磁弁26eだけを開き状態にし、冷媒を、
冷房用凝縮器3→冷房用主液配管14→主液配管11→
個別空気調和機8それぞれの主熱交換器6→主ガス配管
13→冷房用主ガス配管16→冷房用凝縮器3
と循環流動させて冷房を行もことができる。■ Cooling operation mode mainly based on cooling As shown in FIG. Liquid piping 14 → Main liquid piping 11 →
Cooling can also be performed by circulating the air in the following order: main heat exchanger 6 of each individual air conditioner 8 → main gas pipe 13 → cooling main gas pipe 16 → cooling condenser 3.
中間期において、冷房を必要とする部屋と暖房を必要と
する部屋の両方があるような場合にあっては、第2図の
(b)に示すように、更に、第4の電磁弁26dと第8
の電磁弁26hとを開き状態にして中間期の運転モード
に切換え、冷媒の一部を、
暖房用蒸発器17→讐房用主ガス配管20→補助ガス配
管25→個別空気調和機8それぞれの補助熱交IQ器7
→補助液配管23→暖房用主液配管18→暖房用蒸発器
17
とWifff流動させて暖房をも行うことができる。In the intermediate period, if there are both rooms that require cooling and rooms that require heating, as shown in FIG. 2(b), the fourth solenoid valve 26d and 8th
The solenoid valve 26h is opened to switch to the intermediate operation mode, and a portion of the refrigerant is supplied to each of the heating evaporator 17 → main gas piping 20 → auxiliary gas piping 25 → individual air conditioner 8. Auxiliary heat exchanger IQ device 7
→ Auxiliary liquid piping 23 → Main liquid piping 18 for heating → Evaporator for heating 17 By causing the Wiff to flow, heating can also be performed.
また、冷房運転時において、上記中間期の運転モードに
切換えた状態で、補助熱交換器7への冷媒液出口箇所に
設けた重石#22の開度を小にしておき、主熱交換器6
で得られた冷風を補助熱交IQ器7によりわずか加熱し
、除湿を行うようにしても良い。In addition, during the cooling operation, with the operation mode switched to the intermediate operation mode, the opening degree of the weight #22 provided at the refrigerant liquid outlet to the auxiliary heat exchanger 7 is made small, and the main heat exchanger 6
The cold air obtained in step 1 may be slightly heated by the auxiliary heat exchanger IQ device 7 to dehumidify it.
■暖房主体の暖房運転モード
第2図の(c)に示すように、第3の電磁弁26cと第
7の電磁弁26gだけを開き状態にし、冷媒を、
暖房用蒸発2117→暖房用主ガス配管20→主ガス配
管13→個別空気調和機8それぞれの主熱交換器6→主
液配管11→暖房用主液配管18→暖房用蒸発器17
と循環流動させて暖房を行うことができる。■ Heating operation mode mainly for heating As shown in Figure 2 (c), only the third solenoid valve 26c and the seventh solenoid valve 26g are opened, and the refrigerant is transferred from the heating evaporator 2117 to the heating main gas. Heating can be performed by circulating the gas in the following order: piping 20 → main gas piping 13 → main heat exchanger 6 of each individual air conditioner 8 → main liquid piping 11 → heating main liquid piping 18 → heating evaporator 17.
中間期において、暖房運転モードの状態で冷房を必要と
する部屋と暖房を必要とする部屋の両方があるような場
合にあっては、図示しないが、更に、第2の電磁弁26
bと第6の電6n弁26fとを開き状態にして中間期の
運転モードに切換え、冷媒の一部を、
冷房用凝縮器3→冷房用主液配管14→補助液配管23
→個別空気調和機8それぞれの補助熱交換器7→補助ガ
ス配管25→冷房用主ガス配管16→冷房用IjllI
I器3
と循環流動させて冷房をも行うことができる。In the intermediate period, if there are both rooms that require cooling and rooms that require heating in the heating operation mode, the second solenoid valve 26 (not shown) is added.
b and the sixth electric 6n valve 26f are opened to switch to the intermediate operation mode, and a part of the refrigerant is transferred from the cooling condenser 3 to the cooling main liquid pipe 14 to the auxiliary liquid pipe 23.
→ Auxiliary heat exchanger 7 of each individual air conditioner 8 → Auxiliary gas piping 25 → Main gas piping 16 for cooling → IjllI for cooling
Cooling can also be performed by circulating the fluid with the I container 3.
上記実施例における熱IAとしては、吸収式冷凍機を用
い、その吸収式冷凍機からの冷水や低温冷媒などを冷房
用凝縮器3に供給するように構成するとか、あるいは、
地域冷暖房システムによって得られる冷水を冷房用凝縮
器3に供給するように構成するなど、各種のものが採用
できる。As the heat IA in the above embodiment, an absorption refrigerating machine is used, and cold water, low-temperature refrigerant, etc. from the absorption refrigerating machine are supplied to the cooling condenser 3, or,
Various configurations can be adopted, such as a configuration in which cold water obtained by a district heating and cooling system is supplied to the cooling condenser 3.
〈発明の効果〉
本発明の冷暖房システムによれば、運転モード切り換え
機構の切換えにより、冷房および暖房のいずれであって
も、その主体となる側の運転を、主液配管、個別空気調
和機それぞれの主熱交換器および主ガス配管に冷媒を流
V」することによって行い、一方、中間期のさほど熱負
荷を必要としない暖房または冷房運転を、補助ガス配管
、個別空気調和機それぞれの補助熱交換器および補助液
配管に冷媒を流動することによって行うから、冷房用主
液配管、冷房用主ガス配管、暖房用主液配管、暖房用主
ガス配管、主液配管、主熱交換器および主ガス配管それ
ぞれの大きさを、冷房負荷と暖房負荷のうちの高い方の
ピークに合ったものに構成するものの、補助ガス配管、
補助熱交換器および補助液配管それぞれとして、中間期
の小さい負荷に合わせて構成すれば良く、多数の個別空
気調和機それぞれにおいて、補助熱交換器として能力の
小さいものを備えるだけで済むとともに、個別空気調和
機を備えた最上階から最下階にわたる長い補助ガス配管
および補助液配管それぞれを小径の配管で構成でき、冷
房および暖房のいずれをも自然循環によって動力費少な
く行うことができながら、更に、個別空気調和機に備え
る熱交換器、ならびに、それに連通接続する冷媒配管を
小型かつ安価に構成でき、イニシャルコストを大幅に低
減できるようになった。<Effects of the Invention> According to the air conditioning system of the present invention, by switching the operation mode switching mechanism, the main operation of either cooling or heating can be switched between the main liquid piping and the individual air conditioner. This is done by flowing refrigerant through the main heat exchanger and main gas piping of the auxiliary gas piping and individual air conditioners, while heating or cooling operations that do not require much heat load in the intermediate period are carried out through the auxiliary heat exchanger of the auxiliary gas piping and the individual air conditioners. This is done by flowing the refrigerant through the exchanger and auxiliary liquid piping, so the main liquid piping for cooling, the main gas piping for cooling, the main liquid piping for heating, the main gas piping for heating, the main liquid piping, the main heat exchanger, and the main Although the size of each gas pipe is configured to match the peak of the higher of the cooling load and heating load, the auxiliary gas pipe,
The auxiliary heat exchanger and the auxiliary liquid piping can each be configured to suit the small load during the intermediate period, and each of a large number of individual air conditioners only needs to be equipped with an auxiliary heat exchanger with a small capacity. The long auxiliary gas piping and auxiliary liquid piping that run from the top floor to the bottom floor where the air conditioner is installed can be constructed with small diameter piping, allowing both cooling and heating to be performed with natural circulation, reducing power costs. , the heat exchanger provided in the individual air conditioner and the refrigerant piping connected thereto can be constructed compactly and inexpensively, making it possible to significantly reduce the initial cost.
殊に、高層ビルのように、個別空気調和機の個数が多い
うえに、その設置階が多階層にわたる場所の冷暖房シス
テムを構築する場合に、その工費を大幅に低減でき、極
めて有用である。In particular, when constructing a heating and cooling system for a place such as a high-rise building where there are many individual air conditioners and where the air conditioners are installed on multiple floors, the construction cost can be significantly reduced, making it extremely useful.
図面は、本発明に係る冷暖房システムの実施例を示し、
第1図は全体システム構成図、第2図は、各運転モード
を説明する概略システム構成図である。
3・・・冷房用凝縮器
6・・・主熱交換器
7・・・補助熱交換器
8・・・個別空気調和機
1・・・主液配管
3・・・主ガス配管
4・・・冷房用主液配管
6・・・冷房用主ガス配管
7・・・暖房用蒸発器
8・・・暖房用主液配管
0・・・暖房用主ガス配管
3・・・補助液配管
5・・・補助ガス配管
F・・・各階The drawings show an embodiment of the heating and cooling system according to the present invention,
FIG. 1 is an overall system configuration diagram, and FIG. 2 is a schematic system configuration diagram explaining each operation mode. 3... Cooling condenser 6... Main heat exchanger 7... Auxiliary heat exchanger 8... Individual air conditioner 1... Main liquid piping 3... Main gas piping 4... Main liquid piping for cooling 6... Main gas piping for cooling 7... Evaporator for heating 8... Main liquid piping for heating 0... Main gas piping for heating 3... Auxiliary liquid piping 5...・Auxiliary gas piping F...each floor
Claims (1)
交換器と補助熱交換器とを備え、主液配管と主ガス配管
に、前記主熱交換器それぞれを並列に連通接続し、前記
主液配管に、冷房用主液配管を介して冷房用凝縮器を、
暖房用主液配管を介して暖房用蒸発器をそれぞれ連通接
続するとともに、前記主ガス配管に、冷房用主ガス配管
を介して冷房用凝縮器を、暖房用主ガス配管を介して暖
房用蒸発器をそれぞれ連通接続し、かつ、補助液配管と
補助ガス配管に、前記補助熱交換器それぞれを並列に連
通接続し、前記補助液配管を前記冷房用主液配管および
暖房用主液配管それぞれに連通接続するとともに、前記
補助ガス配管を前記冷房用主ガス配管および暖房用主ガ
ス配管それぞれに連通接続し、前記主液配管および主ガ
ス配管に対して、前記冷房用凝縮器のみを連通接続する
冷房運転モードと前記暖房用蒸発器のみを連通接続する
暖房運転モードとに切り換える運転モード切り換え機構
を設けるとともに、前記冷房用凝縮器および暖房用蒸発
器それぞれから前記主熱交換器および補助熱交換器それ
ぞれに冷媒を密閉状態で循環流動可能に構成し、その冷
媒として、前記冷房運転モードにおける前記主熱交換器
での熱交換に伴って液体から蒸気に相変化するとともに
前記暖房運転モードにおける前記主熱交換器での熱交換
に伴って蒸気から液体に相変化する冷媒を使用し、前記
冷房用凝縮器と前記主熱交換器との間に、液体に相変化
した冷媒を前記熱交換器に移送するに足るヘッド差を備
えるとともに、前記主熱交換器と前記暖房用蒸発器との
間に、液体に相変化した冷媒を前記暖房用蒸発器に移送
するに足るヘッド差を備えたことを特徴とする冷暖房シ
ステム。(1) Each individual air conditioner installed on each floor is equipped with a main heat exchanger and an auxiliary heat exchanger, each of the main heat exchangers is connected in parallel to the main liquid piping and the main gas piping, and the A cooling condenser is connected to the main liquid piping via the cooling main liquid piping.
The heating evaporators are connected through the heating main liquid piping, and the cooling condenser is connected to the main gas piping via the cooling main gas piping, and the heating evaporator is connected to the heating main gas piping through the heating main gas piping. the auxiliary heat exchangers are connected in parallel to the auxiliary liquid piping and the auxiliary gas piping, and the auxiliary liquid piping is connected to the cooling main liquid piping and the heating main liquid piping, respectively. At the same time, the auxiliary gas pipe is connected in communication with each of the main gas pipe for cooling and the main gas pipe for heating, and only the cooling condenser is connected in communication with the main liquid pipe and the main gas pipe. An operation mode switching mechanism is provided for switching between a cooling operation mode and a heating operation mode in which only the heating evaporator is connected, and the cooling condenser and heating evaporator are connected to the main heat exchanger and the auxiliary heat exchanger, respectively. Each refrigerant is configured to be able to circulate and flow in a sealed state, and as the refrigerant, the phase changes from liquid to vapor in accordance with heat exchange in the main heat exchanger in the cooling operation mode, and the main heat exchanger in the heating operation mode. A refrigerant whose phase changes from vapor to liquid as a result of heat exchange in a heat exchanger is used, and between the cooling condenser and the main heat exchanger, the refrigerant whose phase changes to liquid is transferred to the heat exchanger. A head difference sufficient to transfer the refrigerant, and a head difference sufficient to transfer the refrigerant whose phase has changed to a liquid to the heating evaporator is provided between the main heat exchanger and the heating evaporator. Features a heating and cooling system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63314628A JP2530490B2 (en) | 1988-12-12 | 1988-12-12 | Air conditioning system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63314628A JP2530490B2 (en) | 1988-12-12 | 1988-12-12 | Air conditioning system |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02157544A true JPH02157544A (en) | 1990-06-18 |
JP2530490B2 JP2530490B2 (en) | 1996-09-04 |
Family
ID=18055600
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63314628A Expired - Lifetime JP2530490B2 (en) | 1988-12-12 | 1988-12-12 | Air conditioning system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2530490B2 (en) |
-
1988
- 1988-12-12 JP JP63314628A patent/JP2530490B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2530490B2 (en) | 1996-09-04 |
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