JP2001108385A - Heat accumulating device - Google Patents
Heat accumulating deviceInfo
- Publication number
- JP2001108385A JP2001108385A JP28229799A JP28229799A JP2001108385A JP 2001108385 A JP2001108385 A JP 2001108385A JP 28229799 A JP28229799 A JP 28229799A JP 28229799 A JP28229799 A JP 28229799A JP 2001108385 A JP2001108385 A JP 2001108385A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- pump
- heat storage
- fluid
- fluid circuit
- 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
- 239000012530 fluid Substances 0.000 claims abstract description 151
- 238000005338 heat storage Methods 0.000 claims description 233
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 104
- 238000001816 cooling Methods 0.000 claims description 64
- 238000010438 heat treatment Methods 0.000 claims description 53
- 230000005855 radiation Effects 0.000 claims description 14
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 19
- 230000007423 decrease Effects 0.000 description 10
- 238000004891 communication Methods 0.000 description 6
- 238000012546 transfer Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007429 general method Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 239000012267 brine Substances 0.000 description 1
- 230000010485 coping Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Other Air-Conditioning Systems (AREA)
- Air Conditioning Control Device (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、余剰の電力を熱に
代えて蓄熱しておき、日中使用電力が大きくなった時に
蓄熱しておいた熱を取り出して利用し、全体として電気
エネルギーの消費量をできるだけ少なくすることができ
る蓄熱装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for storing surplus electric power in place of heat and extracting and utilizing the stored heat when the power used during the day becomes large. The present invention relates to a heat storage device capable of minimizing consumption.
【0002】[0002]
【従来の技術】従来から、余剰電力を熱に代えて蓄熱し
ておくことにより、電力エネルギーを有効活用するシス
テムは実公平3−30744号公報等に有るように公知
であり、またこれとは別に図11、図12に示すような
システムも公知である。ここで、図11に示すシステム
構成を説明すると、図11において、Rは冷熱温熱兼用
冷凍機、P1は第1ポンプ、101は第1切替え弁、1
02は第2切替え弁であり、これらは蓄熱槽103と接
続されている第1流体管路100内に直列に配置されて
いる。また、この第1流体管路100とは別に蓄熱槽1
03と接続されている第2管路管路110が第1流体管
路に対して並列に配置され、第2流体管路110内に蓄
熱槽103に対して並列に複数の放熱器111と、放熱
器111に対して直列に第2ポンプP2、第3切替え弁
113、第4切替え弁114が接続されており、さらに
各放熱器111毎に制御弁112が配置されている。蓄
熱槽103は冷却または加熱される流体が満たされてお
り、各流体管路に配置された各切替え弁101、10
2、113、114は図示のように蓄熱槽に接続されて
いる。このシステムでは、例えば電力に余剰が生じる時
間帯(夜間等の電力料金の安価な時間帯)を利用して第
1ポンプP1および冷熱温熱兼用冷凍機Rを運転し、蓄
熱槽103内の流体を冷却あるいは加熱して蓄熱槽10
3内に蓄熱をしておく。そして冷房あるいは暖房等の負
荷が最大になる昼間等の時間帯に、蓄熱槽103内の流
体を第2ポンプP2によって汲み上げ放熱器111に流
して、冷房あるいは暖房を行うことができるようになっ
ている。しかしながら、このシステムでは、第1、第2
ポンプおよび流体管路は、複数有る放熱器の最大負荷運
転状態に対応して設備しておく必要があり、大型のポン
プおよび断面積の大きな4本の流体管(主管)を使用す
る必要があり、設備費が高価になるなどの問題がある。2. Description of the Related Art Hitherto, a system for effectively utilizing electric power energy by storing surplus electric power instead of heat has been known as disclosed in Japanese Utility Model Publication No. 3-30744, and the like. Separately, systems as shown in FIGS. 11 and 12 are also known. Here, the system configuration shown in FIG. 11 will be described. In FIG. 11, R is a cooling / heating refrigerating machine, P1 is a first pump, 101 is a first switching valve,
Reference numeral 02 denotes a second switching valve, which is arranged in series in the first fluid line 100 connected to the heat storage tank 103. The heat storage tank 1 is separate from the first fluid line 100.
A plurality of radiators 111 arranged in parallel with the first fluid pipeline, and in the second fluid pipeline 110 in parallel with the heat storage tank 103; A second pump P2, a third switching valve 113, and a fourth switching valve 114 are connected in series with the radiator 111, and a control valve 112 is provided for each radiator 111. The heat storage tank 103 is filled with a fluid to be cooled or heated, and each switching valve 101, 10
2, 113 and 114 are connected to a heat storage tank as shown. In this system, the first pump P1 and the cold / hot / heat refrigerating machine R are operated, for example, using a time zone in which surplus power is generated (a time zone in which the power rate is low, such as at night), and the fluid in the heat storage tank 103 is discharged. Cool or heat and heat storage tank 10
Heat is stored in 3. Then, during a time period such as daytime when the load such as cooling or heating is maximized, the fluid in the heat storage tank 103 is pumped up by the second pump P2 and flows to the radiator 111 so that cooling or heating can be performed. I have. However, in this system, the first and second
It is necessary to provide pumps and fluid pipes in accordance with the maximum load operation state of a plurality of radiators, and it is necessary to use a large pump and four fluid pipes (main pipes) having a large cross-sectional area. However, there is a problem that the equipment cost becomes expensive.
【0003】また図12に示すシステムは、放熱器20
1および冷熱温熱兼用冷凍機Rを有する回路を密閉型流
体回路とし、この密閉型流体回路内に熱交換器203を
配置し、さらに此の密閉型流体回路とは別に前記熱交換
器203と接続する大気開放型流体回路205を設け、
熱交換器203を介して蓄熱槽204内に蓄熱したり、
蓄熱槽204内の熱を熱交換器201に流したりするこ
とができる構成を採用している。このシステムでは冷熱
温熱兼用冷凍機から複数の放熱器に流体を供給する管を
共通にするとともに第1ポンプP1への流入管路と放熱
器201からの吐出管路とを別々の管で構成し、これに
よってコストの低減を図ろうとしたものである。しかし
ながら、このシステムにおいても、冷熱温熱兼用冷凍機
から複数の放熱器に流体を供給する管路は最大負荷に併
せた大きな断面積のものを使用する必要があり、システ
ムのコスト低減には十分寄与していない。[0003] The system shown in FIG.
1 and a circuit having the cold / hot / heat refrigerating machine R as a closed fluid circuit, a heat exchanger 203 is arranged in the closed fluid circuit, and further connected to the heat exchanger 203 separately from the closed fluid circuit. An open-air fluid circuit 205 is provided,
Heat is stored in the heat storage tank 204 via the heat exchanger 203,
A configuration in which the heat in the heat storage tank 204 can flow to the heat exchanger 201 is adopted. In this system, a pipe for supplying a fluid from the cooling / heating / refrigerating machine to a plurality of radiators is made common, and an inflow pipe to the first pump P1 and a discharge pipe from the radiator 201 are constituted by separate pipes. Thus, the cost is reduced. However, even in this system, it is necessary to use a pipe with a large cross-sectional area that matches the maximum load for the fluid supply line from the cooling / heating refrigerator to the multiple radiators, which sufficiently contributes to the cost reduction of the system. I haven't.
【0004】そこで、本発明は、蓄熱時と放熱時いずれ
の状態においても2本の管路で対応できるようにすると
ともに、その管路の太さを従来のそれと比較して細くで
きる蓄熱装置を提供し、上記問題を解決するとともに、
ポンプが消費する搬送動力の低減を図ることを目的とす
る。本発明は、密閉型流体回路と大気開放型流体回路と
を熱交換器で接続し、この熱交換器を介して、夜間等の
余剰の電力を熱に代えて蓄熱槽内に蓄熱しておき、日中
使用電力が大きくなった時に蓄熱槽内に蓄熱しておいた
熱を熱交換器を介して取り出して利用し、日中の消費電
力を夜間にシフトするとともに流体搬送用電気エネルギ
ーの消費量をできるだけ少なくすることができる蓄熱装
置として構成されており、蓄熱槽内に蓄熱する蓄熱量は
日中の最大負荷の全量でない蓄熱量(多くの計画は、5
0%近くの蓄熱量)とし、放熱時には各放熱器に供給す
る熱は蓄熱槽と熱源機とが分担するように構成されてい
る。 このため、日中の負荷量が蓄熱量より大きい日の
運転状況では、蓄熱時と放熱時に共用される配管内にお
いて両端より互いに冷(温)水を対向流として流し、そ
れぞれに近い(流れの上流の)位置の各放熱器に対し必
要とされる量が各分岐管を通じ供給されて行き、最後の
放熱器には両者がそれぞれ受け持つ量が双方向より供給
されることになる。そして各放熱器において必要とされ
た冷(温)水は、各放熱器において熱交換された後、蓄
熱時と放熱時に共用される配管において相反する方向流
を形成し、冷凍機、熱交換器に戻り循環を繰り返す。ま
た、日中の負荷量が蓄熱量以下の日の運転状況ではすべ
ての負荷量を蓄熱槽に貯えた熱をもって対応することに
なる。この時の循環冷(温)水の全量は熱交換器を介
し、蓄熱槽から熱を受けることになる。[0004] Therefore, the present invention provides a heat storage device capable of coping with two pipes in both the state of heat storage and the state of heat radiation and capable of making the diameter of the pipe thinner than that of the conventional one. To resolve the above issues,
It is an object of the present invention to reduce the transfer power consumed by the pump. According to the present invention, a closed type fluid circuit and an open-to-atmosphere type fluid circuit are connected by a heat exchanger, and through this heat exchanger, surplus electric power at night or the like is stored in a heat storage tank instead of heat. When the power used during the day increases, the heat stored in the heat storage tank is taken out through the heat exchanger and used to shift the daytime power consumption at night and consume the electric energy for fluid transport. It is configured as a heat storage device that can reduce the amount of heat as much as possible. The amount of heat stored in the heat storage tank is not the full amount of daytime maximum load (most plans are 5
(The amount of heat storage near 0%), and the heat supplied to each radiator at the time of heat radiation is configured to be shared between the heat storage tank and the heat source device. For this reason, in an operation condition in which the daytime load is larger than the heat storage amount, cold (warm) water flows in opposite directions from both ends in the pipe shared during heat storage and heat release, and is close to each other. The required quantity for each radiator in the (upstream) position will be supplied through each branch pipe, and the last radiator will be supplied in both directions with the respective quantities. Then, the cold (warm) water required in each radiator is subjected to heat exchange in each radiator, and then forms opposite flow directions in pipes shared during heat storage and heat release. Return to and repeat the circulation. In addition, in an operation state in which the daytime load amount is equal to or less than the heat storage amount, all the load amounts are handled by the heat stored in the heat storage tank. At this time, the entire amount of the circulating cold (warm) water receives heat from the heat storage tank via the heat exchanger.
【0005】[0005]
【課題を解決するための手段】このため、本発明が採用
した技術解決手段は、流体を循環させることができる密
閉型流体回路内に、熱源機とこの熱源機に流体を供給す
る第1ポンプと熱交換器とをこの順で直列に配置し、さ
らに前記熱源機と第1ポンプおよび熱交換器に対して並
列に複数の管路を設け、これら夫々の管路に放熱器を配
置し、さらに前記熱交換器に対して前記とは別の並列管
路を設けこの管路内に第2ポンプを配置し、また前記熱
交換器には密閉型流体回路とは別に蓄熱槽からの流体を
循環させることができる蓄熱流体回路を接続してなり、
前記密閉型流体回路内の熱源機と第一ポンプとを運転し
て前記熱源機により密閉型流体回路内の流体を冷却また
は加熱し、この冷却または加熱した流体を前記熱交換器
に流して前記蓄熱流体回路内の流体を冷熱または加熱し
て蓄熱槽内に蓄熱する第一過程と、前記密閉型流体回路
内の熱源機と第一ポンプとを必要に応じて運転して前記
熱源機によって密閉型流体回路内の流体を冷却または加
熱し、冷却または加熱された流体を前記放熱器の一部に
循環させるとともに、前記第二ポンプを運転して前記密
閉型流体回路内の流体を前記熱交換器に供給して前記蓄
熱流体回路の流体によって冷却または加熱し、この流体
を前記残りの放熱器に前記第1ポンプからの流れと対向
する方向に流して冷房または暖房する第二過程とを選択
できるようにしたことを特徴とする蓄熱装置であり、複
数階からなるビルの上階に熱源機とこの熱源機に直列に
接続され前記熱源機に流体を供給する第1ポンプとを配
置し、地上側の階に熱交換器を配置し、これらを密閉型
流体回路で直列に接続し、さらに、この密閉型流体回路
内の前記熱源機、第1ポンプと熱交換器の間の各階毎に
前記熱源機と第1ポンプに対して並列の管路を形成して
各管路内に放熱器を配置し、また、前記熱交換器に対し
て地上側に並列に管路を形成し、該管路内に第2ポンプ
を配置し、また前記熱交換器には密閉型流体回路とは別
に蓄熱槽からの流体を循環させることができる大気開放
型の蓄熱流体回路を接続して流体回路を構成し、前記密
閉型流体回路内の熱源機と第一ポンプとを運転して前記
熱源機により密閉型流体回路内の流体を冷却または加熱
し、この冷却または加熱した流体を前記熱交換器に流し
て前記蓄熱回路内の流体を冷熱または加熱して蓄熱槽内
に蓄熱する第一過程と、前記密閉型流体回路内の熱源機
と第一ポンプとを必要に応じて運転して前記熱源機によ
って密閉型流体回路内の流体を冷却または加熱し、冷却
または加熱された流体を前記上階から下階の放熱器に向
けて循環させるとともに、前記第二ポンプを運転して前
記密閉型流体回路内の流体を前記熱交換器に供給して前
記蓄熱流体回路の流体によって冷却または加熱し、この
流体を下階から上階の放熱器に向けて前記第1ポンプか
らの流れに対向する方向に流して冷房または暖房する第
二過程とを選択できるようにしたことを特徴とする蓄熱
装置である。For this reason, the technical solution adopted by the present invention is to provide a heat source device and a first pump for supplying a fluid to the heat source device in a sealed fluid circuit capable of circulating a fluid. And the heat exchanger are arranged in series in this order, furthermore, a plurality of pipelines are provided in parallel with the heat source unit, the first pump and the heat exchanger, and a radiator is arranged in each of these pipelines. Further, a separate parallel pipe is provided for the heat exchanger, and a second pump is disposed in this parallel pipe.Fluid from a heat storage tank is provided in the heat exchanger separately from a closed fluid circuit. A heat storage fluid circuit that can be circulated is connected,
The heat source device in the closed type fluid circuit and the first pump are operated to cool or heat the fluid in the closed type fluid circuit by the heat source device, and the cooled or heated fluid is caused to flow through the heat exchanger, A first step of cooling or heating the fluid in the heat storage fluid circuit to store heat in the heat storage tank, and operating the heat source device and the first pump in the closed type fluid circuit as necessary to seal the heat source device. Cooling or heating the fluid in the fluid circuit, circulating the cooled or heated fluid through a part of the radiator, and operating the second pump to exchange the fluid in the closed fluid circuit with the heat. Cooling or heating by the fluid in the heat storage fluid circuit and supplying the fluid to the remaining radiator in a direction opposite to the flow from the first pump to select cooling or heating. Made it possible A heat source device and a first pump connected in series with the heat source device and supplying a fluid to the heat source device are arranged on an upper floor of a multi-storey building, and a floor on the ground side is provided. Are arranged in series with a sealed fluid circuit, and further, the heat source device in the sealed fluid circuit, the heat source device for each floor between the first pump and the heat exchanger. A pipe is formed in parallel with the first pump, a radiator is arranged in each pipe, and a pipe is formed in parallel with the heat exchanger on the ground side. A second pump is disposed, and the heat exchanger is connected to a heat storage fluid circuit of an open-to-atmosphere type that can circulate fluid from a heat storage tank separately from a closed fluid circuit, to form a fluid circuit, By operating the heat source unit and the first pump in the closed fluid circuit, the heat source unit allows the flow in the closed fluid circuit to flow. Cooling or heating, the first step of flowing the cooled or heated fluid to the heat exchanger to cool or heat the fluid in the heat storage circuit and store heat in the heat storage tank, and in the closed fluid circuit The heat source unit and the first pump are operated as necessary to cool or heat the fluid in the closed fluid circuit by the heat source unit, and direct the cooled or heated fluid from the upper floor to the lower floor radiator. While circulating, the second pump is operated to supply the fluid in the closed fluid circuit to the heat exchanger to be cooled or heated by the fluid in the heat storage fluid circuit, and the fluid is cooled from the lower floor to the upper floor. A second step of cooling or heating by flowing in a direction opposite to the flow from the first pump toward the radiator of (1).
【0006】[0006]
【実施の形態】以下、図面に基づいて本発明の実施の形
態を説明すると、図1は建築物内(たとえば高層ビル
等)に本蓄熱装置を装備した第1実施形態に関わる蓄熱
装置の構成図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows the structure of a heat storage device according to a first embodiment in which the present heat storage device is installed in a building (for example, a high-rise building). FIG.
【0007】図において、1は夜間の蓄熱と日中の不足
熱量を補うための熱源機としての冷熱温熱兼用冷凍機で
あり、切り替えによって冷熱と温熱とを供給出来る機能
を有している。2は前記冷熱温熱兼用冷凍機1に流体を
供給する第1ポンプであり、これら冷熱温熱兼用冷凍機
1と第1ポンプ2とは流体回路内の最上部(例えばビル
の最上階)に配置されている。3は建物内の各階を冷房
又は暖房するための放熱器3であり、この放熱器3は各
階毎に配置されている。4は流体回路内の最下部(例え
ばビルの地下等)に配置され安価な電力を熱に代え蓄熱
槽(後述する)11内に蓄熱するための熱交換器、5は
前記熱交換器の近くに配置され前記放熱器3に流体を流
すための第2ポンプ、6は冷熱温熱兼用冷凍機1の吐出
側に接続された一方向流れを形成する逆止弁、7は放熱
器3の流入側管路に接続された制御弁、8は管路を切り
替える第1切替え弁、9は管路を切り替える第2切替え
弁、10は制御装置である。In FIG. 1, reference numeral 1 denotes a cold / heat / heat refrigerating machine as a heat source device for supplementing nighttime heat storage and daytime insufficient heat, and has a function of supplying cold and warm by switching. Reference numeral 2 denotes a first pump for supplying a fluid to the cooling / heating / cooling machine 1. The cooling / heating / cooling machine 1 and the first pump 2 are arranged at the uppermost part (for example, the top floor of a building) in a fluid circuit. ing. Reference numeral 3 denotes a radiator 3 for cooling or heating each floor in the building. The radiator 3 is arranged for each floor. Reference numeral 4 denotes a heat exchanger which is disposed at the lowermost portion of the fluid circuit (for example, underground of a building) and stores heat in a heat storage tank (described later) 11 in place of inexpensive electric power, and 5 near the heat exchanger. A second pump for flowing a fluid to the radiator 3, a check valve 6 for forming a one-way flow connected to a discharge side of the refrigerator 1, and a flow-in side 7 of the radiator 3. A control valve connected to the pipeline, 8 is a first switching valve for switching the pipeline, 9 is a second switching valve for switching the pipeline, and 10 is a control device.
【0008】前記冷熱温熱兼用冷凍機1、第1ポンプ
2、熱交換器4は図中の符号(カ)、(キ)で示す管路
で直列に接続されており、また前記放熱器3は、冷熱温
熱兼用冷凍機1、第1ポンプ2と前記熱交換器4との間
で、冷熱温熱兼用冷凍機1と第1ポンプ2および熱交換
器4のそれぞれに対して並列に複数配置された管路
(ク)内に設けられており、また前記第2ポンプ5も前
記熱交換器4に対して並列の管路(コ)内に配置されて
いる。さらに第1切替え弁8は管路(カ)内に、また、
第2切替え弁9は管路(キ)内に配置され、さらに第1
切替え弁8は、第1ポンプ2と第2切替え弁9との間の
管路(キ)に管路(ケ)により接続されている。そし
て、前記冷熱温熱兼用冷凍機1、第1ポンプ2、熱交換
器4、放熱器3等が接続される管路は全体として図のよ
うに密閉型流体回路を構成している。また、第1ポンプ
2および第2ポンプ5は運転状態によって吐出流量を変
えることができる機能を有しており、さらに前記第1、
第2切替え弁8、9、制御弁7も共に、制御装置10か
らの指令によって管路の切替えや流量が制御される構成
となっている。The cooling / heating / cooling machine 1, the first pump 2, and the heat exchanger 4 are connected in series by pipes indicated by reference numerals (f) and (g) in the figure. A plurality of the chiller / heater / refrigerator 1, the first pump 2 and the heat exchanger 4, and a plurality of chiller / heater / refrigerator 1, the first pump 2 and the heat exchanger 4 are arranged in parallel with each other. The second pump 5 is provided in a pipeline (h) parallel to the heat exchanger 4. Further, the first switching valve 8 is provided in the pipeline (f),
The second switching valve 9 is disposed in the pipeline (g),
The switching valve 8 is connected to a pipe (g) between the first pump 2 and the second switching valve 9 by a pipe (k). The pipelines to which the cooling / heating / refrigerating unit 1, the first pump 2, the heat exchanger 4, the radiator 3 and the like are connected as a whole constitute a closed fluid circuit as shown in the figure. Further, the first pump 2 and the second pump 5 have a function of changing the discharge flow rate according to the operation state.
Both the second switching valves 8 and 9 and the control valve 7 are configured so that the switching of the pipeline and the flow rate are controlled by a command from the control device 10.
【0009】前記熱交換器4には大気開放型流体回路
(ア)が接続され、この流体回路は蓄熱槽11に接続さ
れ、大気開放型流体回路は循環ポンプ12と二つの分岐
切替え弁13、14を備えている。蓄熱槽11は複数の
隔壁15によって区画された槽を有し、各槽は連通管1
6で連通され、さらにそのうち図中左側の槽17は低温
側として右側の槽18は高温側として機能を果たし、各
槽は水等の流体によって満たされている。そして、蓄熱
槽11の低温側の槽17および高温側の槽18には前記
二つの分岐切替え弁13、14に接続する管路(ウ)、
(オ)、(イ)、(エ)が図のように配置されており、
この大気開放型流体回路と蓄熱槽11とによって、余剰
電力を熱に代えて蓄熱する蓄熱手段を構成している。な
おこの蓄熱手段は従来から公知のものであり、また種々
の蓄熱手段を使用することができ、本発明の特徴部では
ないので詳細な説明は省略する。An air release type fluid circuit (A) is connected to the heat exchanger 4, and this fluid circuit is connected to a heat storage tank 11. The air release type fluid circuit has a circulation pump 12 and two branch switching valves 13, 14 is provided. The heat storage tank 11 has tanks partitioned by a plurality of partition walls 15, and each tank has a communication pipe 1.
6, the tank 17 on the left side in the figure functions as a low temperature side and the tank 18 on the right side functions as a high temperature side, and each tank is filled with a fluid such as water. The low temperature side tank 17 and the high temperature side tank 18 of the heat storage tank 11 have pipes (c) connected to the two branch switching valves 13 and 14, respectively.
(E), (A), and (E) are arranged as shown in the figure.
The open-to-atmosphere type fluid circuit and the heat storage tank 11 constitute a heat storage means for storing surplus electric power instead of heat. The heat storage means is conventionally known, and various heat storage means can be used. Since the heat storage means is not a feature of the present invention, a detailed description is omitted.
【0010】つづいて、上記蓄熱装置の運転状態を説明
する。 冷房蓄熱時(図2) 図2は安価な電力を使用して蓄熱槽11内に冷熱蓄熱す
る状態のシステム図であり、図中太線が運転されている
状態の管路である。 基本動作 密閉型流体回路は、熱源である冷熱温熱兼用冷凍機1、
第1ポンプ2は運転状態にあり、第1切替え弁8、第2
切替え弁9は、密閉型流体回路(カ)、(キ)を連通す
るように切替えられ、さらに各放熱器3用の制御弁7は
強制的に遮断され、第2ポンプ5は停止状態とする。ま
た、大気開放型回路(ア)側は、循環ポンプ12は運転
され、分岐切替え弁13、14は図のように直流を形成
するように切換られる。この状態において、大気開放型
回路側では、蓄熱槽11の高温槽18側の上部より、配
管(ウ)を介し循環ポンプ12により汲み上げられた高
冷水(前夜に利用され温度が上昇した蓄熱槽水)は熱交
換器4によって冷熱温熱兼用冷凍機1によって冷却され
た冷水によって冷却される。この冷却された蓄熱槽水
は、蓄熱槽11の低温槽17側に配管(ア)、(イ)を
介し移送され、蓄熱される。この状況が継続すると蓄熱
槽11内の低温槽17は冷却された冷水で満たされ更に
継続すると連通管16で連結された隣の槽に移送され、
順次冷却処理された冷水により蓄熱槽11内は蓄熱され
ていく。一方、密閉型流体回路では、冷熱温熱兼用冷凍
機1によって冷却された冷水により熱交換器4によって
大気開放型回路内の蓄熱槽水を冷却し、温度上昇した密
閉型流体回路内の高冷水は第1ポンプ2により冷熱温熱
兼用冷凍機1に供給して冷却され再度熱交換器4に供給
され、上記事項を繰り返す。Next, the operation state of the heat storage device will be described. Cooling Heat Storage (FIG. 2) FIG. 2 is a system diagram showing a state where cold heat is stored in the heat storage tank 11 using inexpensive electric power. Basic operation The closed-type fluid circuit is composed of a cooling / heating / cooling machine 1, which is a heat source,
The first pump 2 is in the operating state, and the first switching valve 8 and the second
The switching valve 9 is switched so as to communicate the closed fluid circuits (f) and (g), the control valve 7 for each radiator 3 is forcibly shut off, and the second pump 5 is stopped. . On the side of the open-to-atmosphere circuit (a), the circulation pump 12 is operated, and the branch switching valves 13 and 14 are switched so as to form a direct current as shown in the figure. In this state, on the open-to-atmosphere circuit side, the high-temperature water pumped up by the circulating pump 12 through the pipe (c) from the upper part of the heat storage tank 11 on the high-temperature tank 18 side (the heat storage tank water used in the previous night and having an increased temperature). ) Is cooled by the cold water cooled by the cold / hot / heat refrigerating machine 1 by the heat exchanger 4. This cooled heat storage tank water is transferred to the low temperature tank 17 side of the heat storage tank 11 via the pipes (A) and (A) and stored. If this situation continues, the low-temperature tank 17 in the heat storage tank 11 will be filled with cooled cold water, and if it continues further, it will be transferred to the next tank connected by the communication pipe 16,
Heat is stored in the heat storage tank 11 by the cold water that has been sequentially cooled. On the other hand, in the closed type fluid circuit, the heat storage tank water in the open-to-atmosphere type circuit is cooled by the heat exchanger 4 with the cold water cooled by the cold / hot / heat refrigerating machine 1. The first pump 2 supplies the heat to the cooling / heating / cooling machine 1 to be cooled and supplied to the heat exchanger 4 again, and the above items are repeated.
【0011】冷房放熱時(図3) 図3は蓄熱槽11内に蓄熱された冷熱を利用するととも
に、冷熱温熱兼用冷凍機1を利用してして冷房を行う状
態の図であり、図中太線が運転されている状態の管路で
あり、各放熱器3に対する流体の流れは太点線で示され
ている。 基本動作 密閉型流体回路は、熱源である冷熱温熱兼用冷凍機1、
第1ポンプ2は運転状態にあり、第2切替え弁9は熱交
換器4と第2ポンプ5の吸入口を接続するように、また
第1切替え弁8は熱交換器4と第1ポンプ2の吸入口を
接続するように切替えられる。さらに、各放熱器3用の
制御弁7は各放熱器3が必要とする流量に応じた開閉状
況となるように制御装置10からの指令により作動さ
れ、第2ポンプ5は運転状態にする。一方、開放回路側
は、循環ポンプ12は運転、分岐切替え弁13、14は
図のように直流を形成するように切替えられる。 基本運転状況 大気開放型回路では、蓄熱槽11の低温槽17側の下部
より、配管(オ)を介し循環ポンプ12により汲み上げ
られた低冷水(前夜に冷却された蓄熱槽水)は熱交換器
4を介し、密閉型流体回路内の放熱器3によって温度上
昇された高冷水を冷却する。この温度上昇された蓄熱槽
水は、蓄熱槽11の高温槽18側に配管(エ)を介し移
送される。この状況が継続すると蓄熱槽11内の高温槽
18は温度上昇された高冷水で満たされ更に継続すると
連通管で連結された隣の槽に移送され、順次温度上昇さ
れた高冷水により蓄熱槽11内は満たされていく。一
方、密閉型流体回路では、熱交換器4を介し蓄熱槽11
の冷水により冷却された冷水は第2切替え弁9、配管
(コ)を介して第2ポンプ5により汲み上げられ共用配
管(カ)内を蓄熱時とは逆方向に流れ、近傍の放熱器3
にそれぞれが必要とする冷水量をその制御弁7の開度に
応じて供給し熱交換する。ここで温度上昇した高冷水は
再度第2ポンプ5によって共用配管(キ)を蓄熱時と反
対方向に流れ、さらに第1切替え弁8を介して熱交換器
4に供給される。また、第1ポンプ2の運転により冷熱
温熱兼用冷凍機1に供給され冷却された冷水は逆止弁
6、共用配管(カ)を介し、蓄熱時と同方向の流れを
し、近傍の放熱器3にそれぞれが必要とする冷水量をそ
の制御弁7の開度に応じて供給し、熱交換する。ここで
温度上昇した高冷水は共用配管(キ)を蓄熱時と同方向
流れをして再度第1ポンプ2によって冷熱温熱兼用冷凍
機1に供給され冷却されて、上記事項を繰り返す。FIG. 3 is a diagram showing a state in which cooling is performed by utilizing the cold stored in the heat storage tank 11 and utilizing the cooling / heating / heat refrigerating machine 1 in FIG. 3. The bold line indicates the operating pipeline, and the flow of fluid to each radiator 3 is indicated by a bold dotted line. Basic operation The closed-type fluid circuit is composed of a cooling / heating / cooling machine 1, which is a heat source,
The first pump 2 is in operation, the second switching valve 9 connects the heat exchanger 4 to the suction port of the second pump 5, and the first switching valve 8 connects the heat exchanger 4 and the first pump 2 to each other. Is switched to connect the suction port of. Further, the control valve 7 for each radiator 3 is operated by a command from the control device 10 so as to be in an open / close state corresponding to the flow rate required by each radiator 3, and the second pump 5 is put into an operating state. On the other hand, on the open circuit side, the circulation pump 12 is operated, and the branch switching valves 13 and 14 are switched so as to form a direct current as shown in the figure. Basic operation status In the open-to-atmosphere circuit, low-temperature water (heat-storage-tank water cooled the previous night) pumped from the lower part of the heat-storage tank 11 on the low-temperature tank 17 side by the circulation pump 12 through the pipe (e) is used as a heat exchanger. The chilled water whose temperature has been raised by the radiator 3 in the closed type fluid circuit is cooled via 4. The heat storage tank water whose temperature has been raised is transferred to the high temperature tank 18 side of the heat storage tank 11 via the pipe (d). If this situation continues, the high-temperature tank 18 in the heat storage tank 11 is filled with the high-temperature water whose temperature has been raised, and if further continued, it is transferred to the next tank connected by the communication pipe, and the heat storage tank 11 is sequentially heated with the high-temperature water. The inside is filled. On the other hand, in the closed type fluid circuit, the heat storage tank 11 is connected via the heat exchanger 4.
The cold water cooled by the cold water is pumped up by the second pump 5 through the second switching valve 9 and the pipe (U), flows in the common pipe (f) in the direction opposite to the heat storage state, and the nearby radiator 3
Then, the required amount of cold water is supplied according to the degree of opening of the control valve 7 to exchange heat. Here, the high-cooled water whose temperature has risen flows through the common pipe (g) again in the direction opposite to that at the time of heat storage by the second pump 5, and is further supplied to the heat exchanger 4 via the first switching valve 8. The cold water supplied to and cooled by the cold / heat / heat refrigerating machine 1 by the operation of the first pump 2 flows in the same direction as that of the heat storage through the check valve 6 and the common pipe (f). 3 is supplied with the required amount of cold water in accordance with the opening of the control valve 7 to exchange heat. Here, the high-cooled water whose temperature has risen flows in the common pipe (g) in the same direction as when the heat is stored, and is again supplied to the cooling / heating / cooling machine 1 by the first pump 2 to be cooled, and the above items are repeated.
【0012】日中負荷が最大負荷量より減少し、且つ蓄
熱槽内の蓄熱量以上の場合の運転状況 密閉型流体回路の運転は、各放熱器3の負荷の状況によ
り第1ポンプ2の循環量を制御する。全体負荷は冷熱温
熱兼用冷凍機1と蓄熱槽11からの蓄熱とがそれぞれ受
け持ち、第2ポンプ5により供給される冷水量を優先的
に各放熱器3に流し、温度上昇した水は熱交換器4で各
放熱器3に供給すべき温度にまで冷却する。全体の最大
負荷量より負荷量が減少し、且つ蓄熱槽11が保有する
蓄熱量以上の場合、第2ポンプ5は初期の状況(最大負
荷時の分担量)で運転する。この時第1ポンプ2は全体
負荷量が減少した事による全体必要循環量の減少分を初
期の状況(最大負荷時の分担量)から減少するよう制御
装置10が第1ポンプ2を制御し運転する。この結果、
冷熱温熱兼用冷凍機1の運転負荷は第1ポンプ2からの
供給冷水の供給量と、温度によるから、その供給負荷量
によって冷凍機能力が制御される。一方、大気開放型回
路では、蓄熱槽11と熱交換器4の関係は図3の基本運
転状況と同様の作動を行う。即ち、熱交換器4によって
対応出来る範囲の密閉回路の負荷を処理すべく、循環ポ
ンプ12は蓄熱槽11から冷水を汲み上げ熱交換器4に
供給する。 例えば、10階建ての建物において、最大
負荷時に、冷熱温熱兼用冷凍機1と、蓄熱槽11用の熱
交換器4とがそれぞれ半分熱処理を受け持つ様に計画さ
れた施設において全体の負荷量が、80%に減少した
時、冷熱温熱兼用冷凍機1と第1ポンプ2は上側の約4
階分の負荷(放熱器3)に対応し、蓄熱槽11と第2ポ
ンプ5からの蓄熱は下側約6階分の負荷(放熱器3)に
対応する。第1ポンプ2、第2ポンプ5からの放熱器3
への冷水の供給は各ポンプ直近の放熱器3から順次その
先へと共用配管(カ)を通じ行われ、最後の放熱器3に
は両方のポンプより合わせてその必要とする量が供給さ
れる。[0012] Operation when the daytime load is less than the maximum load and is equal to or greater than the amount of heat stored in the heat storage tank. The operation of the sealed fluid circuit depends on the load of each radiator 3 and the circulation of the first pump 2. Control the amount. The overall load is assigned to the cooling / heating / cooling machine 1 and the heat storage from the heat storage tank 11, respectively, and the amount of cold water supplied by the second pump 5 is preferentially flown to each radiator 3, and the water whose temperature has risen is changed by the heat exchanger. In 4, the radiator 3 is cooled to a temperature to be supplied. When the load amount is smaller than the total maximum load amount and is equal to or more than the heat storage amount held by the heat storage tank 11, the second pump 5 operates in the initial state (the shared amount at the time of the maximum load). At this time, the controller 10 controls the first pump 2 so that the first pump 2 controls the first pump 2 so that the decrease in the total required circulation amount due to the decrease in the total load amount is reduced from the initial state (the amount of load at the maximum load). I do. As a result,
The operating load of the cooling / heating / cooling machine 1 depends on the supply amount of cold water supplied from the first pump 2 and the temperature, and the refrigeration function is controlled by the supply load amount. On the other hand, in the open-to-atmosphere circuit, the relationship between the heat storage tank 11 and the heat exchanger 4 performs the same operation as in the basic operation state in FIG. That is, the circulation pump 12 pumps cold water from the heat storage tank 11 and supplies it to the heat exchanger 4 in order to handle the load of the closed circuit within a range that can be handled by the heat exchanger 4. For example, in a 10-story building, at the time of maximum load, the total load in a facility where the cooling / heating / refrigerating machine 1 and the heat exchanger 4 for the heat storage tank 11 are each designed to perform half heat treatment, When the pressure is reduced to 80%, the cooling / heating / cooling machine 1 and the first pump 2 are moved to about 4
The heat storage from the heat storage tank 11 and the second pump 5 corresponds to the load (radiator 3) for the lower approximately six floors. Radiator 3 from first pump 2 and second pump 5
The supply of cold water to the radiator 3 is performed sequentially from the radiator 3 in the immediate vicinity of each pump to the other through a common pipe (f), and the required amount is supplied to the last radiator 3 by both pumps. .
【0013】日中負荷が最大負荷量より減少し蓄熱槽内
の蓄熱量以下の場合の運転状況 密閉型流体回路では、各放熱器3の負荷の状況により第
1ポンプ2の循環量を制御し、その結果として冷熱温熱
兼用冷凍機1を2次的に制御する。全体の最大負荷量よ
り負荷量が減少し蓄熱槽11からの蓄熱による熱交換が
熱交換器4の能力以下となった場合(即ち、蓄熱槽11
からの熱で十分に負荷が賄える状態となった場合)、こ
の時制御装置10により冷熱温熱兼用冷凍機1は全体負
荷量が減少した事により停止すると伴に第1ポンプ2も
同時に停止させる。全体必要循環量を受け持つのは第2
ポンプ5であり、蓄熱槽11内の熱を熱交換器4を介し
て各放熱器3負荷に供給する。第2ポンプ5も受け持つ
全体負荷量に対応する為、負荷量の減少分を初期の状況
(最大負荷時の分担量)から減少させて運転する。この
時の冷水の流れは、共用配管(カ)では蓄熱時とは反対
の流れ方向で循環するとともに、逆止弁6により冷熱蓄
熱兼用冷凍機1および第1ポンプへの流れは止められ
る。大気開放型回路である蓄熱槽11と熱交換器4の関
係は図3に基本運転状況と同じ作動を行う。即ち、熱交
換器4によって対応出来る範囲の密閉型流体回路の負荷
を処理すべく、循環ポンプ12は蓄熱槽11から冷水を
汲み上げ熱交換器4に供給する。密閉型流体回路の負荷
が熱交換器4の最大処理能力以下に減少した時、循環ポ
ンプ12はその負荷量に対応する循環量に変化する。Operating state when the daytime load is less than the maximum load and is equal to or less than the amount of heat stored in the heat storage tank In the closed fluid circuit, the amount of circulation of the first pump 2 is controlled according to the state of load on each radiator 3. As a result, the chiller 1 is secondarily controlled. When the load amount is smaller than the total maximum load amount and the heat exchange by the heat storage from the heat storage tank 11 becomes equal to or less than the capacity of the heat exchanger 4 (that is, the heat storage tank 11
In this case, when the load can be sufficiently covered by the heat from the heat source), the control unit 10 stops the cold / hot / heat refrigerating machine 1 due to the decrease in the overall load, and also stops the first pump 2 at the same time. Second is responsible for the overall required circulation volume
The pump 5 supplies heat in the heat storage tank 11 to each radiator 3 load via the heat exchanger 4. In order to correspond to the total load that the second pump 5 also takes charge of, the operation is performed with the amount of decrease in the load reduced from the initial situation (the amount of load at the maximum load). The flow of the cold water at this time circulates in the common pipe (f) in the flow direction opposite to that during the heat storage, and the check valve 6 stops the flow to the cold / heat storage / refrigerator 1 and the first pump. The relationship between the heat storage tank 11 and the heat exchanger 4, which are open-to-atmosphere circuits, performs the same operation as the basic operation state in FIG. That is, the circulation pump 12 pumps up cold water from the heat storage tank 11 and supplies it to the heat exchanger 4 in order to handle the load of the closed fluid circuit within a range that can be handled by the heat exchanger 4. When the load of the closed fluid circuit decreases below the maximum processing capacity of the heat exchanger 4, the circulation pump 12 changes to a circulation amount corresponding to the load amount.
【0014】例えば、10階建ての建物において、最大
負荷時に、冷熱温熱兼用冷凍機1と、蓄熱槽11からの
蓄熱がそれぞれ半分熱処理を受け持つ様に計画された施
設において全体の負荷量が、40%に減少した時、制御
装置10により冷熱温熱兼用冷凍機1と第1ポンプ2は
停止し、蓄熱槽11からの蓄熱により熱交換器4とその
循環ポンプ12が作動して全ての負荷(放熱器3)に対
応する。第2ポンプ5の循環量は負荷量に応じて制御さ
れる。第2ポンプ5から全ての放熱器3への冷水の供給
はポンプ直近の放熱器3から順次その先へと共用配管
(カ)を通じ行われる。この時、開放回路側の循環ポン
プ12の循環量は第2ポンプ5の循環量と同様に負荷量
に応じて制御される。For example, in a 10-story building, when the maximum load is applied, in a facility where the heat from the cooling / heating / refrigerating machine 1 and the heat storage from the heat storage tank 11 are each to be subjected to half heat treatment, the total load is 40%. %, The control device 10 stops the cold / hot / heat refrigerating machine 1 and the first pump 2, and the heat exchanger 4 and its circulation pump 12 are operated by the heat storage from the heat storage tank 11, and all the loads (radiation) 3). The circulation amount of the second pump 5 is controlled according to the load amount. The supply of the cold water from the second pump 5 to all the radiators 3 is performed sequentially from the radiator 3 immediately near the pump to the other end thereof through a common pipe (f). At this time, the circulation amount of the circulation pump 12 on the open circuit side is controlled in accordance with the load amount similarly to the circulation amount of the second pump 5.
【0015】暖房蓄熱時(図4) 基本動作 密閉型流体回路では、熱源である冷熱温熱兼用冷凍機
1、第1ポンプ2は運転し、第1切替え弁8、第2切替
え弁9は図のように直流を形成するように作動、各放熱
器3用の制御弁7は強制的に閉塞、第2ポンプ5は停止
とする。大気開放型回路は、循環ポンプ12は運転、分
岐切替え弁13、14は図のように直角流を形成するよ
うに作動する。 基本運転状況 大気開放型回路では、蓄熱槽11の低温槽17側の下部
より、配管(オ)を介し循環ポンプ12により汲み上げ
られた低温水(前夜に利用され温度が下降した蓄熱槽
水)は熱交換器4を介し、冷熱温熱兼用冷凍機1によっ
て加温された温水によって加温される。この加温された
蓄熱槽水は、蓄熱槽11の高温槽18側に配管(エ)を
介し移送され、蓄熱される。この状況が継続すると蓄熱
槽11内の高温槽18は加温された温水で満たされ更に
継続すると連通管で連結された隣の槽に移送され、順次
加温処理された温水により蓄熱槽11内は蓄熱されてい
く。一方、密閉型流体回路においては、熱交換器4によ
って蓄熱槽水を加温し、温度下降した低温水は第1ポン
プ2により冷熱温熱兼用冷凍機1に供給加温され再度熱
交換器4に供給され、上記事項を繰り返す。In the closed-circuit type fluid circuit, the cooling / heating / cooling machine 1 and the first pump 2, which are heat sources, are operated, and the first switching valve 8 and the second switching valve 9 are arranged as shown in FIG. The control valve 7 for each radiator 3 is forcibly closed, and the second pump 5 is stopped. In the open-to-atmosphere circuit, the circulation pump 12 operates and the branch switching valves 13 and 14 operate so as to form a right-angle flow as shown in the figure. Basic operation status In the open-to-atmosphere circuit, low-temperature water (heat storage tank water used in the previous night and having a lowered temperature) pumped from the lower part of the heat storage tank 11 on the side of the low-temperature tank 17 by the circulation pump 12 through the pipe (e) is discharged. Through the heat exchanger 4, the water is heated by the warm water heated by the cooling / heating / cooling machine 1. The heated heat storage tank water is transferred to the high temperature tank 18 side of the heat storage tank 11 via the pipe (d) and stored therein. When this situation continues, the high-temperature tank 18 in the heat storage tank 11 is filled with heated warm water, and when the situation continues, the high-temperature tank 18 is transferred to the next tank connected by the communication pipe and sequentially heated by the warm water. Is stored. On the other hand, in the closed type fluid circuit, the heat storage tank water is heated by the heat exchanger 4, and the low-temperature water whose temperature has dropped is supplied to the cold / hot / heat refrigerating machine 1 by the first pump 2 and is heated again by the heat exchanger 4. Supply and repeat the above.
【0016】暖房放熱時(図5) 基本動作 密閉型流体回路は、熱源である冷熱温熱兼用冷凍機1、
第1ポンプ2は運転、第1切替え弁8、第2切替え弁9
は図のように直角流を形成するように作動し、各放熱器
3用の制御弁7は各放熱器3が必要とする流量に応じた
開閉状況となるように制御され、また第2ポンプ5は運
転状態とする。大気開放型回路側は、循環ポンプ12は
運転、分岐切替え弁13、14は図のように直流を形成
するように作動する。 基本運転状況 大気開放型回路側では、蓄熱槽11の高温槽18側の上
部より、配管(ウ)を介し循環ポンプ12により汲み上
げられた高温水(前夜に加温された蓄熱槽水)は熱交換
器4を介し、密閉型流体回路側の放熱器3によって温度
下降された低温水を加熱する。この温度下降された蓄熱
槽水は、蓄熱槽11の低温槽17側に配管(イ)を介し
移送される。この状況が継続すると蓄熱槽11内の低温
槽17は温度下降された低温水で満たされ更に継続する
と連通管16で連結された隣の槽に移送され、順次温度
下降された低温水により蓄熱槽11内は満たされてい
く。一方、密閉回路側においては、第2ポンプ5により
熱交換器4を介し蓄熱槽11の温水により加温された温
水は第2切替え弁9、配管(コ)を介し共用配管(カ)
内を蓄熱時とは逆方向の流れをし、近傍の放熱器3にそ
れぞれが必要とする温水量をその制御弁7の開度に応じ
て放熱器3に供給して熱交換し温度下降した低温水は共
用配管(キ)を蓄熱時と反対方向流れをして再度第2ポ
ンプ5の作用によって熱交換器4に供給される。また、
もう1台の第1ポンプ2の運転により冷熱温熱兼用冷凍
機1に供給され加温された温水は逆止弁6、共用配管
(カ)を介し、蓄熱時と同方向の流れをし、近傍の放熱
器3にそれぞれが必要とする温水量をその制御弁7の開
度に応じて放熱器3に供給され熱交換し温度下降した低
温水は共用配管(キ)を蓄熱時と同方向流れをして再度
第1ポンプ2によって冷熱温熱兼用冷凍機1に供給され
加熱され、上記事項を繰り返す。At the time of heating and radiating heat (FIG. 5) Basic operation The closed type fluid circuit includes a cold / heat / heat refrigerating machine 1, which is a heat source.
The first pump 2 is operated, the first switching valve 8, the second switching valve 9
Operates so as to form a right angle flow as shown in the figure, the control valve 7 for each radiator 3 is controlled so as to open and close according to the flow rate required by each radiator 3, and the second pump 5 is an operation state. On the open-to-atmosphere type circuit side, the circulation pump 12 is operated and the branch switching valves 13 and 14 are operated so as to generate a direct current as shown in the figure. Basic operation status On the open-to-atmosphere circuit side, the high-temperature water (heat storage tank water heated the previous night) pumped by the circulation pump 12 through the pipe (c) from the upper part of the heat storage tank 11 on the high-temperature tank 18 side is heated. Through the exchanger 4, the low-temperature water whose temperature has been lowered by the radiator 3 on the sealed fluid circuit side is heated. The heat storage tank water whose temperature has been lowered is transferred to the low temperature tank 17 side of the heat storage tank 11 via the pipe (a). When this situation continues, the low-temperature tank 17 in the heat storage tank 11 is filled with the low-temperature water whose temperature has been lowered, and when the state continues, the low-temperature tank 17 is transferred to the next tank connected by the communication pipe 16, and the heat storage tank is sequentially cooled by the low-temperature water. The inside of 11 is filled. On the other hand, on the closed circuit side, the warm water heated by the warm water in the heat storage tank 11 via the heat exchanger 4 by the second pump 5 is supplied to the common pipe (f) via the second switching valve 9 and the pipe (f).
The flow in the direction opposite to that of the heat storage is performed, and the amount of hot water required for each of the radiators 3 in the vicinity is supplied to the radiator 3 according to the opening of the control valve 7 to exchange heat and lower the temperature. The low-temperature water flows in the common pipe (g) in the opposite direction to that during heat storage, and is supplied to the heat exchanger 4 again by the action of the second pump 5. Also,
The hot water supplied to the cold / hot / heat refrigerating machine 1 by the operation of the other first pump 2 and warmed flows through the check valve 6 and the common pipe (f) in the same direction as that of the heat storage. The amount of hot water required for each radiator 3 is supplied to the radiator 3 in accordance with the opening of the control valve 7, and the low-temperature water whose temperature has been reduced due to heat exchange flows through the common pipe (g) in the same direction as when storing heat. Then, it is supplied again to the cooling / heating / refrigerating machine 1 by the first pump 2 and heated, and the above items are repeated.
【0017】日中負荷が最大負荷量より減少し、且つ蓄
熱槽内の蓄熱量以上の場合の運転状況 密閉型流体回路の運転は、各放熱器3の負荷の状況によ
り第1ポンプ2の循環量を制御する。全体負荷を冷熱温
熱兼用冷凍機1と蓄熱槽11からの蓄熱とがそれぞれ受
け持ち第2ポンプ5により供給される温水量を優先的に
各放熱器3に与え、放熱器3で降下した水を熱交換器4
で再び熱処理する。全体の最大負荷量より負荷量が減少
し、且つ負荷が蓄熱槽11での蓄熱能力以上の場合、第
2ポンプ5は初期の状況(最大負荷時の分担量)で運転
する。この時第1ポンプ2は全体負荷量が減少した事に
よる全体必要循環量の減少分を初期の状況(最大負荷時
の分担量)から減少させて運転する。この結果、冷熱温
熱兼用冷凍機1の運転負荷は第1ポンプ2からの供給温
水の供給量と、温度によるから、その供給負荷量によっ
て冷熱温熱兼用冷凍機1が制御される。大気開放型回路
である蓄熱槽11と熱交換器4の関係は図5の基本作動
と同様の作動を行う。熱交換器4によって対応出来る範
囲の密閉型流体回路の負荷を処理すべく、循環ポンプ1
2は蓄熱槽11から温水を汲み上げ熱交換器4に供給す
る。The operation state when the daytime load is less than the maximum load amount and is equal to or more than the heat storage amount in the heat storage tank. The operation of the closed type fluid circuit depends on the load condition of each radiator 3 and the circulation of the first pump 2. Control the amount. The entire load is transferred to the cooler / heater refrigerator 1 and the heat storage from the heat storage tank 11, respectively, and the amount of hot water supplied by the second pump 5 is given to each radiator 3 preferentially. Exchanger 4
Heat treatment again. When the load is smaller than the overall maximum load and the load is equal to or greater than the heat storage capacity of the heat storage tank 11, the second pump 5 operates in the initial state (the shared load at the maximum load). At this time, the first pump 2 is operated by reducing the decrease in the total required circulation amount due to the decrease in the total load amount from the initial situation (the amount of load at the maximum load). As a result, the operating load of the cold / hot refrigerating machine 1 depends on the supply amount of the hot water supplied from the first pump 2 and the temperature. Therefore, the cold / hot refrigerating machine 1 is controlled by the supply load amount. The relationship between the heat storage tank 11 and the heat exchanger 4, which is an open-to-atmosphere type circuit, performs the same operation as the basic operation in FIG. In order to handle the load of the closed fluid circuit within a range that can be handled by the heat exchanger 4, the circulation pump 1
2 pumps hot water from the heat storage tank 11 and supplies it to the heat exchanger 4.
【0018】例えば、10階建ての建物において、最大
負荷時に、冷熱温熱兼用冷凍機1と、蓄熱槽11の蓄熱
がそれぞれ半分熱処理を受け持つ様に計画された施設に
おいて全体の負荷量が、80%に減少した時、冷熱温熱
兼用冷凍機1とその第1ポンプ2は上から約4階分の負
荷(放熱器3)に対応し、蓄熱槽11からの蓄熱が下か
ら約6階分の負荷(放熱器3)に対応する。第1ポンプ
2、第2ポンプ5からの放熱器3への温水の供給はポン
プ直近の放熱器3から順次その先へと共用配管(カ)を
通じ行われ、最後の放熱器3には両方のポンプより合わ
せてその必要とする量が供給される。For example, in a 10-story building, when the maximum load is applied, the total load of the cooling / heating / cooling machine 1 and the heat storage in the heat storage tank 11 is set to be half the heat treatment, respectively. , The cooling / heating and refrigerating machine 1 and its first pump 2 correspond to the load (radiator 3) of about four floors from the top, and the heat storage from the heat storage tank 11 becomes the load of about six floors from the bottom. (Radiator 3). The supply of warm water from the first pump 2 and the second pump 5 to the radiator 3 is performed sequentially from the radiator 3 closest to the pump to the destination through a common pipe (f). The required amount is supplied together with the pump.
【0019】日中負荷が最大負荷量より減少し蓄熱槽内
の蓄熱量以下の場合の運転状況 密閉型流体回路の運転は、各放熱器3の負荷の状況によ
り第1ポンプ2の循環量を制御し、その結果として冷熱
温熱兼用冷凍機1を2次的に制御する。全体の最大負荷
量より負荷量が減少し蓄熱槽11での蓄熱量以下となっ
た場合(即ち、蓄熱槽11の蓄熱量で全ての負荷が賄え
る場合)、この時第1ポンプ2は全体負荷量が減少した
事により停止すると伴に冷熱温熱兼用冷凍機1も同時に
停止する。全体必要循環量を受け持つのは第2ポンプ5
であり、蓄熱槽11内の熱を熱交換器4を介して各放熱
器3負荷に供給する。第2ポンプ5も受け持つ全体負荷
量に対応する為、負荷量の減少分を初期の状況(最大負
荷時の分担量)から減少させて運転する。この時の温水
の流れは、共用配管(カ)を蓄熱時とは反対の流れ方向
で循環するとともに、逆止弁6により冷熱蓄熱兼用冷凍
機1および第1ポンプへの流れは止められる。大気開放
型回路である蓄熱槽11と熱交換器4の関係は図5の基
本運転状況と同様の作動を行う。熱交換器4によって対
応出来る範囲の密閉型流体回路の負荷を処理すべく、循
環ポンプ12は蓄熱槽11から温水を汲み上げ熱交換器
4に供給する。密閉型流体回路の負荷が熱交換器4の最
大処理能力以下に減少した時、第2ポンプ5はその負荷
量に対応する循環量に変化する。Operation when the daytime load is less than the maximum load and is equal to or less than the amount of heat stored in the heat storage tank. The operation of the closed type fluid circuit depends on the load of each radiator 3 and the amount of circulation of the first pump 2. Control, and as a result, the cooling / heating / cooling machine 1 is secondarily controlled. In the case where the load amount is smaller than the total maximum load amount and becomes equal to or less than the heat storage amount in the heat storage tank 11 (that is, when all the loads can be covered by the heat storage amount in the heat storage tank 11), the first pump 2 When the refrigerator is stopped due to a decrease in the amount, the refrigerator / cooler 1 also stops at the same time. The second pump 5 is responsible for the overall required circulation volume.
The heat in the heat storage tank 11 is supplied to each radiator 3 load via the heat exchanger 4. In order to correspond to the total load that the second pump 5 also takes charge of, the operation is performed with the amount of decrease in the load reduced from the initial situation (the amount of load at the maximum load). At this time, the flow of the hot water circulates in the common pipe (f) in the flow direction opposite to that during the heat storage, and the flow to the cold / heat storage / refrigerator 1 and the first pump is stopped by the check valve 6. The relationship between the heat storage tank 11 and the heat exchanger 4, which is an open-to-atmosphere type circuit, performs the same operation as in the basic operation state in FIG. The circulation pump 12 pumps hot water from the heat storage tank 11 and supplies it to the heat exchanger 4 in order to handle the load of the closed fluid circuit within a range that can be handled by the heat exchanger 4. When the load of the closed type fluid circuit decreases below the maximum processing capacity of the heat exchanger 4, the second pump 5 changes to a circulation amount corresponding to the load amount.
【0020】例えば、10階建ての建物において、最大
負荷時に、冷熱温熱兼用冷凍機1と、蓄熱槽11の蓄熱
とがそれぞれ半分熱処理を受け持つ様に計画された施設
において全体の負荷量が、40%に減少した時、冷熱温
熱兼用冷凍機1とその第1ポンプ2は停止し、蓄熱槽1
1の蓄熱が全ての負荷(放熱器3)に対応する。第2ポ
ンプ5の循環量は負荷量に応じて制御される。第2ポン
プ5から全ての放熱器3への温水の供給はポンプ直近の
放熱器3から順次その先へと共用配管(カ)を通じ行わ
れる。この時、大気開放型回路側の循環ポンプ12の循
環量は第1ポンプ2の循環量と同様に負荷量に応じて制
御される。For example, in a 10-story building, when the maximum load is applied, in a facility where the cooling / heating / refrigerating refrigerator 1 and the heat storage in the heat storage tank 11 are each designed to perform half heat treatment, the total load is 40%. %, The cooling / heating / cooling machine 1 and its first pump 2 are stopped and the heat storage tank 1 is stopped.
One heat storage corresponds to all loads (radiator 3). The circulation amount of the second pump 5 is controlled according to the load amount. The supply of the hot water from the second pump 5 to all the radiators 3 is performed from the radiator 3 closest to the pump to the destination sequentially through a common pipe (f). At this time, the circulation amount of the circulation pump 12 in the open-to-atmosphere type circuit is controlled according to the load amount similarly to the circulation amount of the first pump 2.
【0021】つづいて第2実施形態に関わる蓄熱装置に
ついて図面を参照して説明すると、図6は高層ビル内に
第2実施形態に係る蓄熱装置を装備した構成図である。
図6に示すように第2実施形態は、第1実施形態のおけ
る放熱器(負荷)3の上流側に配置されている制御弁7
を放熱器3の下流側に配置し、制御弁7Aを3方弁とす
るとともに、制御弁7Aと放熱器3の上流側とを接続し
た点で、第1実施形態と異なる。その他の構成は第1実
施形態と同様であるので説明は省略する。この第2実施
形態の運転状態は基本的には第1実施形態と同様である
が、以下各運転状態を簡単に説明する。 冷房蓄熱時(図7) 図7は安価な電力を使用して蓄熱槽11内に冷熱蓄熱す
る状態のシステム図であり、図中太線が運転されている
状態の管路である。この状態は第1実施形態と同様であ
り、大気開放型回路側では、蓄熱槽11の高温槽18側
の上部より、配管(ウ)を介し循環ポンプ12により汲
み上げられた高冷水(前夜に利用され温度が上昇した蓄
熱槽水)は熱交換器4によって冷熱温熱兼用冷凍機1に
よって冷却された冷水によって冷却され、蓄熱槽11内
に蓄熱が行われる。この状態は第1実施形態と同様であ
る。Next, the heat storage device according to the second embodiment will be described with reference to the drawings. FIG. 6 is a configuration diagram in which a heat storage device according to the second embodiment is provided in a high-rise building.
As shown in FIG. 6, the second embodiment is different from the first embodiment in that a control valve 7 arranged upstream of the radiator (load) 3 is used.
Is arranged on the downstream side of the radiator 3, the control valve 7 </ b> A is a three-way valve, and the control valve 7 </ b> A is connected to the upstream side of the radiator 3. The other configuration is the same as that of the first embodiment, and the description is omitted. Although the operation state of the second embodiment is basically the same as that of the first embodiment, each operation state will be briefly described below. Cooling Heat Storage (FIG. 7) FIG. 7 is a system diagram showing a state in which cold heat is stored in the heat storage tank 11 using inexpensive electric power. This state is the same as that of the first embodiment. On the open-to-atmosphere type circuit side, the high-temperature water pumped from the upper part of the heat storage tank 11 on the high-temperature tank 18 side by the circulation pump 12 via the pipe (c) (used on the previous night) The heat storage tank water whose temperature has risen) is cooled by the cold water cooled by the cooler / heater refrigerator 1 by the heat exchanger 4, and heat is stored in the heat storage tank 11. This state is the same as in the first embodiment.
【0022】冷房放熱時(図8) 図8は蓄熱槽11内に蓄熱された冷熱を利用するととも
に、冷熱温熱兼用冷凍機1を利用してして冷房を行う状
態の図であり、図中太線が運転されている状態の管路で
あり、各放熱器3に対する流体の流れは太点線で示され
ている。この状態の時には密閉型流体回路での運転状況
が第1実施形態と異なっている。即ち、大気開放型回路
では、蓄熱槽11の低温槽17側の下部より、配管
(オ)を介し循環ポンプ12により汲み上げられた低冷
水(前夜に冷却された蓄熱槽水)は熱交換器4を介し、
密閉型流体回路内の放熱器3によって温度上昇された高
冷水を冷却する。一方、密閉型流体回路では、熱交換器
4を介し蓄熱槽11の冷水により冷却された冷水は第2
切替え弁9、配管(コ)を介して第2ポンプ5により汲
み上げられ共用配管(カ)内を蓄熱時とは逆方向に流
れ、近傍の放熱器3にそれぞれが必要とする冷水量をそ
の制御弁7Aの開度に応じて供給し熱交換する。また放
熱器3において余分となる冷水は制御弁7Aを介して、
放熱器3において熱交換し温度上昇した高冷水と混合
し、再度第2ポンプ5によって共用配管(キ)を蓄熱時
と反対方向に流れ、さらに第1切替え弁8を介して熱交
換器4に供給される。また、第1ポンプ2の運転により
冷熱温熱兼用冷凍機1に供給され冷却された冷水は逆止
弁6、共用配管(カ)を介し、蓄熱時と同方向の流れを
し、近傍の放熱器3にそれぞれが必要とする冷水量をそ
の制御弁7Aの開度に応じて供給し、熱交換する。また
放熱器3において余分となる冷水は制御弁7Aを介し
て、放熱器3において熱交換し温度上昇した高冷水と混
合し、再度第1ポンプ2によって冷熱温熱兼用冷凍機1
に供給され冷却されて、上記事項を繰り返す。こうして
放熱器3を通って熱交換される冷水の量は放熱器が必要
とする量に制御することができ、これによって熱交換の
効率を一層向上することができる。FIG. 8 is a diagram showing a state in which cooling is performed by utilizing the cold stored in the heat storage tank 11 and utilizing the cooling / heating / refrigerating unit 1 in FIG. The bold line indicates the operating pipeline, and the flow of fluid to each radiator 3 is indicated by a bold dotted line. In this state, the operation state of the closed fluid circuit is different from that of the first embodiment. That is, in the open-to-atmosphere circuit, the low-temperature water (heat-storage-tank water cooled the previous night) pumped from the lower part of the heat-storage tank 11 on the low-temperature tank 17 side by the circulation pump 12 through the pipe (e) is used as the heat exchanger 4. Through
The chilled water whose temperature has been raised by the radiator 3 in the closed fluid circuit is cooled. On the other hand, in the closed fluid circuit, the cold water cooled by the cold water in the heat storage tank 11 via the heat exchanger 4
It is pumped by the second pump 5 through the switching valve 9 and the pipe (U), flows in the common pipe (F) in the opposite direction to the heat storage, and controls the amount of cold water required for each of the nearby radiators 3. Heat is supplied and heat exchanged according to the opening of the valve 7A. In addition, excess cold water in the radiator 3 is supplied via the control valve 7A.
The heat is exchanged in the radiator 3 and mixed with the high-temperature water whose temperature has risen, and again flows through the common pipe (g) in the opposite direction to the heat storage by the second pump 5, and further flows to the heat exchanger 4 via the first switching valve 8. Supplied. The cold water supplied to and cooled by the cold / heat / heat refrigerating machine 1 by the operation of the first pump 2 flows in the same direction as that of the heat storage through the check valve 6 and the common pipe (f). 3 is supplied with the required amount of cold water in accordance with the opening of the control valve 7A to exchange heat. The excess cold water in the radiator 3 is mixed with the high-cooled water whose temperature has been increased by heat exchange in the radiator 3 through the control valve 7A, and is again cooled and heated by the first pump 2.
Is supplied and cooled, and the above items are repeated. In this manner, the amount of cold water that is heat-exchanged through the radiator 3 can be controlled to the amount required by the radiator, thereby further improving the efficiency of heat exchange.
【0023】暖房蓄熱時(図9) 大気開放型回路では、蓄熱槽11の低温槽17側の下部
より、配管(オ)を介し循環ポンプ12により汲み上げ
られた低温水(前夜に利用され温度が下降した蓄熱槽
水)は熱交換器4を介し、冷熱温熱兼用冷凍機1によっ
て加温された温水によって加温される。一方、密閉型流
体回路においては、熱交換器4によって蓄熱槽水を加温
し、温度下降した低温水は第1ポンプ2により冷熱温熱
兼用冷凍機1に供給加温され再度熱交換器4に供給さ
れ、上記事項を繰り返す。この状態は第1実施形態と同
様である。During heating and heat storage (FIG. 9) In the open-to-atmosphere circuit, low-temperature water pumped from the lower part of the heat storage tank 11 on the low-temperature tank 17 side by the circulation pump 12 via the pipe (e) (the temperature used in the previous night is The lowered heat storage tank water is heated by the hot water heated by the cold / heat / heat refrigerating machine 1 via the heat exchanger 4. On the other hand, in the closed type fluid circuit, the heat storage tank water is heated by the heat exchanger 4, and the low-temperature water whose temperature has dropped is supplied to the cold / hot / heat refrigerating machine 1 by the first pump 2 and is heated again by the heat exchanger 4. Supply and repeat the above. This state is the same as in the first embodiment.
【0024】暖房放熱時(図10) 基本動作 図10は蓄熱槽11内に蓄熱された温熱を利用するとと
もに、冷熱温熱兼用冷凍機1を利用してして暖房を行う
状態の図であり、図中太線が運転されている状態の管路
であり、各放熱器3に対する流体の流れは太点線で示さ
れている。この状態の時には密閉型流体回路での運転状
況が第1実施形態と異なっている。即ち、大気開放型回
路側では、蓄熱槽11の高温槽18側の上部より、配管
(ウ)を介し循環ポンプ12により汲み上げられた高温
水(前夜に加温された蓄熱槽水)は熱交換器4を介し、
密閉型流体回路側の放熱器3によって温度下降された低
温水を加熱する。一方、密閉回路側においては、第2ポ
ンプ5により熱交換器4を介し蓄熱槽11の温水により
加温された温水は第2切替え弁9、配管(コ)を介し共
用配管(カ)内を蓄熱時とは逆方向の流れをし、近傍の
放熱器3にそれぞれが必要とする温水量をその制御弁7
Aの開度に応じて放熱器3に供給して熱交換する。また
放熱器3において余分となる温水は制御弁7Aを介し
て、放熱器3において熱交換し温度下降した低温水と混
合し、再度第2ポンプ5によって共用配管(キ)を蓄熱
時と反対方向に流れ、さらに第1切替え弁8を介して熱
交換器4に供給される。また、もう1台の第1ポンプ2
の運転により冷熱温熱兼用冷凍機1に供給され加温され
た温水は逆止弁6、共用配管(カ)を介し、蓄熱時と同
方向の流れをし、近傍の放熱器3にそれぞれが必要とす
る温水量をその制御弁7Aの開度に応じて供給し、熱交
換する。また放熱器3において余分となる温水は制御弁
7Aを介して、放熱器3において熱交換し温度下降した
低温水と混合し、再度第1ポンプ2によって冷熱温熱兼
用冷凍機1に供給され冷却されて、上記事項を繰り返
す。こうして放熱器3を通って熱交換される温水の量は
放熱器が必要とする量に制御することができ、これによ
って熱交換効率を一層向上することができる。FIG. 10 is a diagram showing a state in which heating is performed by utilizing the heat stored in the heat storage tank 11 and using the cold / heat / heat refrigerating machine 1 while heating and radiating heat (FIG. 10). The heavy line in the drawing is the pipeline in the operating state, and the flow of the fluid to each radiator 3 is indicated by a thick dotted line. In this state, the operation state of the closed fluid circuit is different from that of the first embodiment. That is, on the open-to-atmosphere circuit side, high-temperature water (heat storage tank water heated on the previous night) pumped from the upper part of the heat storage tank 11 on the high-temperature tank 18 side by the circulation pump 12 via the pipe (c) is exchanged with heat. Via vessel 4
The low-temperature water whose temperature has been lowered by the radiator 3 on the closed fluid circuit side is heated. On the other hand, on the closed circuit side, the warm water heated by the warm water in the heat storage tank 11 via the heat exchanger 4 by the second pump 5 passes through the second switching valve 9 and the pipe (U) to the inside of the common pipe (f). The heat flows in the opposite direction to the heat storage, and the amount of hot water required for each of the radiators 3 in the vicinity is controlled by the control valve 7.
The heat is supplied to the radiator 3 in accordance with the opening degree of A to exchange heat. Excessive hot water in the radiator 3 is mixed with low-temperature water whose temperature has been reduced by heat exchange in the radiator 3 via the control valve 7A, and the common pump (g) is again moved by the second pump 5 in the direction opposite to the heat storage. And is supplied to the heat exchanger 4 via the first switching valve 8. Also, another first pump 2
The hot water supplied to the chiller / heater / refrigerator 1 and heated by the operation described above flows through the check valve 6 and the common pipe (f) in the same direction as that of the heat storage, and each of the radiators 3 in the vicinity is required. Is supplied in accordance with the opening of the control valve 7A to exchange heat. The excess hot water in the radiator 3 is mixed with the low-temperature water whose temperature has been reduced due to heat exchange in the radiator 3 via the control valve 7A, and is again supplied to the cool / heat / heat refrigerating machine 1 by the first pump 2 to be cooled. And repeat the above. In this way, the amount of hot water heat exchanged through the radiator 3 can be controlled to the amount required by the radiator, thereby further improving the heat exchange efficiency.
【0025】以上本発明に係る実施形態について説明し
たが、これらの実施形態が従来の蓄熱装置に比較して有
利な点について説明する。 〔本発明と、従来装置との配管設備、冷温水循環量及び
その搬送動力の差異〕各装置は最大負荷時に対応出来る
様決定される。 最大負荷時において ・一般的には、全負荷を蓄熱槽の蓄熱でまかなわず、5
0%を蓄熱量で対応し、残りの50%を冷凍機の追い掛
け運転により処置するよう装置全体の設計を行うケース
が経済性の面で多い。このケースを一般方式とここでは
仮称する。この一般方式において、 ・放熱器全負荷=qL ・冷凍機能力=qR ・蓄熱槽用熱交換器能力=qHEX(qR) ・放熱器出入口温度差をΔT とすると qL=qR+qHEX =2×qR となる。Although the embodiments according to the present invention have been described above, the advantages of these embodiments as compared with the conventional heat storage device will be described. [Differences in Piping Facilities, Cooling / Hot Water Circulating Amounts and Transport Powers Between the Present Invention and Conventional Apparatus] Each apparatus is determined to be able to cope with the maximum load. At maximum load ・ Generally, the entire load cannot be covered by the heat storage in the heat storage tank.
In many cases, the whole device is designed so that 0% is handled by the heat storage amount and the remaining 50% is treated by the chase operation of the refrigerator. This case is temporarily referred to as a general method here. In this general method, the total radiator load = qL, the refrigeration function capacity = qR, the heat exchanger capacity for the heat storage tank = qHEX (qR), and the radiator inlet / outlet temperature difference is ΔT: qL = qR + qHEX = 2 × qR .
【0026】一般方式の一方式である図−11のシステ
ム(従来システム)の場合では、放熱時の最大負荷時の
放熱運転は、各放熱器111の合計負荷に対応するた
め、循環ポンプP2により蓄熱槽から必要循環量QLを
放熱器系に供給すると、蓄熱槽内の利用温度差もΔTと
することが出来、 qL=QL・ΔT であるから QL=qL/ΔT となる。 又、蓄熱時における、冷凍機と蓄熱槽間の循環量QSTは
循環ポンプP1により蓄熱槽から冷凍機1に供給され qR=QST・ΔT であるから QST=qR/ΔT=1/2×qL/ΔT となる。In the case of the system shown in FIG. 11 (conventional system), which is one of the general systems, the heat dissipation operation at the maximum load during heat dissipation corresponds to the total load of each radiator 111. When the required circulation amount QL is supplied from the heat storage tank to the radiator system, the temperature difference in use in the heat storage tank can also be set to ΔT. Since qL = QL · ΔT, QL = qL / ΔT. In addition, the amount of circulation Q ST between the refrigerator and the heat storage tank during heat storage is supplied from the heat storage tank to the refrigerator 1 by the circulation pump P1, so that q R = Q ST · ΔT, so that Q ST = qR / ΔT = 1/2. × qL / ΔT.
【0027】即ち、図11の従来システムでは、蓄熱時
の冷凍機と蓄熱槽間の主管における循環量はQST=1/
2×qL/ΔT が必要であり、放熱時の蓄熱槽と各放
熱器との間の主幹部における循環量は QL=qL/Δ
T を必要とする。次に、一般方式の一方式である図1
2のシステム(従来システム)の場合では、放熱時の最
大負荷時の運転は、各放熱器負荷201の全負荷に対応
するため、放熱器による全負荷を熱源装置である蓄熱槽
用熱交換器203と冷凍機R1との両者が合せて対応す
る。即ち、全放熱器負荷による温度上昇分ΔTをそれぞ
れの熱源装置が各々1/2×ΔTづつ直列に対応する。
このときの装置全体必要循環量QLO、放熱器出入口温度
差をΔTとすると、qL=QLO×ΔT=2×qR=2・
qHEX であるからQLO=(2×qR)/ΔT=(2
×qHEX)/ΔT=qL/ΔTとなる。即ち、冷凍
機、蓄熱槽用熱交換器共に循環量はQLO=qL/ΔTが
必要となる。この時、前述した如く蓄熱槽用熱交換器を
介し負荷の熱処理を行った結果の温度差は1/2×ΔT
となり、蓄熱槽内の利用温度差は蓄熱槽用熱交換器20
3を介し決定されるため、その利用温度差も1/2×Δ
Tとなる。又、蓄熱時における、冷凍機と蓄熱槽用熱交
換器との間の循環水量QSTO はqR=QSTO ×(1/
2)×ΔT であるからQSTO =(2×q
R)/ΔT=qL/ΔTとなる。即ち、図12の従来シ
ステムにおいては、蓄熱時における冷凍機と蓄熱槽用熱
交換器とを直接結ぶ主管と、放熱時における冷凍機、蓄
熱槽用熱交換器及び放熱器とを結ぶ主管とに流れる流量
は共に、QLO=QSTO =qL/ΔTが必要となる。That is, in the conventional system shown in FIG. 11, the amount of circulation in the main pipe between the refrigerator and the heat storage tank during heat storage is Q ST = 1/1.
2 × qL / ΔT is required, and the amount of circulation in the main trunk between the heat storage tank and each radiator during heat release is QL = qL / Δ
Requires T. Next, FIG.
In the case of the system 2 (conventional system), the operation at the maximum load during the heat radiation corresponds to the full load of each radiator load 201, so the full load by the radiator is used as the heat source device heat exchanger for the heat storage tank. Both 203 and the refrigerator R1 correspond. That is, each heat source device corresponds to the temperature increase ΔT due to the total radiator load in series by ×× ΔT.
Assuming that the required total circulation amount Q LO and the temperature difference between the radiator inlet and outlet at this time are ΔT, qL = Q LO × ΔT = 2 × qR = 2 ·
Since qHEX, Q LO = (2 × qR) / ΔT = (2
× qHEX) / ΔT = qL / ΔT. That is, the circulation amount of both the refrigerator and the heat storage tank heat exchanger needs to be Q LO = qL / ΔT. At this time, the temperature difference as a result of performing the heat treatment of the load through the heat exchanger for the heat storage tank as described above is ×× ΔT
And the difference in the use temperature in the heat storage tank depends on the heat exchanger 20 for the heat storage tank.
3 so that the difference in utilization temperature is also 1/2 × Δ
It becomes T. Further, the amount of circulating water Q STO between the refrigerator and the heat exchanger for the heat storage tank during heat storage is qR = Q STO × (1 /
2) × ΔT, so Q STO = (2 × q
R) / ΔT = qL / ΔT. That is, in the conventional system of FIG. 12, the main pipe directly connecting the refrigerator and the heat storage tank heat exchanger during heat storage, and the main pipe connecting the refrigerator, the heat storage tank heat exchanger and the heat radiator during heat radiation. Both flow rates require Q LO = Q STO = qL / ΔT.
【0028】本発明によると全負荷を蓄熱槽が50%対
応するという一般方式のもとでは qL=qR+qHEX qR=qL/2であるから qHEX=qL×1/2 ・放熱器出入口の温度差をΔT という前述の従来方式と同一条件下において放熱時で
は、図3(冷房時の放熱時フロー図)に示した如く、全
放熱器負荷を2分割しながら冷凍機と蓄熱槽用熱交換器
がそれぞれ分担し合う。負荷を2分割し合って対応する
時、冷凍機とこれが対応する放熱器との間の循環量、蓄
熱槽用熱交換器とこれが対応する放熱器との間の循環水
量は同量であり、この循環量QLNは qR=qHEX=QLN×ΔT=qL/2であるから QLN=1/2×qL/ΔT となる。 故に、本発明における放熱時の放熱器と冷凍機、蓄熱槽
用熱交換器との間の必要循環量は図−11のシステムに
おける必要循環量QL =qL/ΔTの1/2同様に図−
12のシステムにおける循環量QLO=qL/ΔTの1/
2となる。また、蓄熱時では、冷凍機と蓄熱槽用熱交換
器との間の循環水量QSTN はqR=ΔT×QSTN =qH
EX=1/2qLであるからQSTN =QLN=1/2×q
L/ΔT となり、本発明における冷凍機
と蓄熱槽用熱交換器との間の必要循環量は、図−11の
システムにおける必要循環量QST =1/2×qL/Δ
Tと同量、図−12のシステムにおける必要循環量Q
STO =qL/ΔTの1/2となる。According to the present invention, qL = qR + qHEX qR = qL / 2 under the general system in which the heat storage tank corresponds to 50% of the entire load. QHEX = qL × 1/2. At the time of heat radiation under the same condition as the above-mentioned conventional method of ΔT, as shown in FIG. 3 (flow diagram at the time of heat radiation at the time of cooling), the refrigerator and the heat exchanger for the heat storage tank are divided while dividing the total radiator load into two. Share each other. When the load is divided into two to correspond, the amount of circulation between the refrigerator and the corresponding radiator, and the amount of circulating water between the heat exchanger for the heat storage tank and the corresponding radiator are the same, Since the circulation amount Q LN is qR = qHEX = Q LN × ΔT = qL / 2, Q LN = 1 / × qL / ΔT. Thus, the radiator and the refrigerator of the heat radiation in the present invention, 1/2 Similarly, FIG necessary circulation amount Q L = qL / ΔT required circulation amount in the system of Figure 11 between the heat storage tank heat exchanger −
The circulation amount Q LO = qL / ΔT in the 12 systems
It becomes 2. In the heat storage, the circulating water amount Q STN between the refrigerator and the heat storage tank heat exchanger is qR = ΔT × Q STN = qH
Since EX = 1 / qL, Q STN = Q LN = 1 / × q
L / ΔT, and the required circulation amount between the refrigerator and the heat storage tank heat exchanger in the present invention is the required circulation amount Q ST = 1/2 × qL / Δ in the system of FIG.
Same amount as T, required circulation amount Q in the system of Fig.-12
STO = 1/2 of qL / ΔT.
【0029】以上のことにより、本発明による冷凍機と
蓄熱槽用熱交換器とを直接結ぶ主管及び放熱器への供給
主管は、従来システムと比較し、その循環量を前述した
如く減することが出来、その結果配管径を細くすること
が出来る。又、循環量が1/2ですむことにより、搬送
動力も減少させることが出来る。さらに蓄熱槽内の熱利
用温度差に関しても、図−7のシステムに比べ、蓄熱槽
用熱交換器における利用温度差はΔT/2からΔTへと
2倍に拡大する事が出来るため、同一熱量を蓄熱すると
き蓄熱槽容積を1/2に減少する事ができる。これらの
ことにより、本発明は経済性において、従来システムと
比較すると配管口径を細くする事が出来ると共に、蓄熱
水槽容積をも1/2にすることにが出来、装置のイニシ
ャルコストの低減が計れる。又、省エネルギー性に関し
ては、循環量を1/2にすることにより搬送動力を大幅
に削減する事が出来、省エネルギー性も発揮する。以上
のように本発明によれば、蓄熱時と放熱時に共に2本の
主管で対応でき、さらにその管の太さを従来のそれと比
較し細くする事ができ、また、最大負荷時の放熱対応に
おいて、従来のシステムと比較すると各ポンプが受け持
つ循環量と放熱器3の受け持ち分担域を約二分の一に減
少させる事が出来き、各ポンプの消費動力のみならず、
それらの合計消費量を低減できる。さらに循環量が従来
方式と比較し半減する事になり配管の太さを細くする事
が出来工事費も低減できる。なお、上記実施形態におい
ては熱源機として冷熱温熱兼用冷凍機を使用した例につ
いて説明したが、熱源機として、単独の暖房機あるいは
冷凍機を使用したり、併用することもできる。また、本
システムに使用する熱媒体としては水、ブライン等、本
システムの機能を達成できる種々の熱媒体を使用するこ
とができる。さらに、上記実施形態ではビルのような上
下に配管した具体例について説明したが、流体を循環さ
せることができる密閉型流体回路と、蓄熱槽からの流体
を循環させることができる蓄熱流体回路とを同一平面上
に配置しても同様な効果を達成できることは当然であ
る。また、本発明はその精神又は主要な特徴から逸脱す
ることなく他の色々な形で実施することができ、また、
前述の実施例はあらゆる点で単なる例示に過ぎず、限定
的に解釈してはならない。As described above, the main pipe for directly connecting the refrigerator and the heat exchanger for the heat storage tank according to the present invention and the main pipe for supplying to the radiator are required to reduce the circulation amount as described above as compared with the conventional system. And, as a result, the pipe diameter can be reduced. Further, since the circulation amount is reduced to half, the transfer power can be reduced. Regarding the difference in heat utilization temperature in the heat storage tank, the difference in utilization temperature in the heat exchanger for the heat storage tank can be doubled from ΔT / 2 to ΔT as compared with the system in Fig. 7; When the heat is stored, the heat storage tank volume can be reduced to half. Due to these facts, the present invention can reduce the pipe diameter in comparison with the conventional system, reduce the heat storage water tank volume to half, and reduce the initial cost of the apparatus in terms of economy. . Concerning energy saving, by reducing the circulation amount to 1 /, the transfer power can be greatly reduced, and energy saving can be exhibited. As described above, according to the present invention, two main pipes can be used for both heat storage and heat release, and the thickness of the pipes can be made smaller than that of the conventional pipes. In comparison with the conventional system, it is possible to reduce the amount of circulation occupied by each pump and the area shared by the radiator 3 to about a half, and not only the power consumption of each pump,
Their total consumption can be reduced. Furthermore, the amount of circulation is reduced by half compared with the conventional method, and the thickness of the piping can be reduced, thereby reducing the construction cost. In the above-described embodiment, an example in which a cooling / heating / refrigerating machine is used as the heat source device has been described. However, a single heating device or a refrigerator can be used as the heat source device, or they can be used in combination. Further, as the heat medium used in the present system, various heat mediums that can achieve the functions of the present system, such as water and brine, can be used. Furthermore, in the above-described embodiment, a specific example in which pipes are vertically arranged such as a building has been described.However, a closed fluid circuit that can circulate fluid and a heat storage fluid circuit that can circulate fluid from a heat storage tank are described. Naturally, the same effect can be achieved even if they are arranged on the same plane. The present invention may be embodied in various other forms without departing from its spirit or main characteristics,
The foregoing embodiments are merely illustrative in every respect and should not be construed as limiting.
【0030】[0030]
【発明の効果】以上詳細に述べた如く本発明によれば、
本蓄熱装置では、蓄熱時と放熱時に共に2本の主管で対
応でき、さらにその管の太さを従来のそれと比較し細く
する事ができる。最大負荷時の放熱対応において、従来
のシステムと比較すると各ポンプが受け持つ循環量と放
熱器3の受け持ち分担域を約二分の一に減少させる事が
出来き、各ポンプの消費動力のみならず、それらの合計
消費量を低減できる。又、循環量が従来方式と比較し半
減する事になり配管の太さを細くする事が出来工事費も
低減できる。本装置の日中放熱時において、日中の負荷
が蓄熱量以上の場合、即ち熱交換器を介し蓄熱槽の熱と
熱源機の熱を同時に利用する場合、各放熱器の利用温度
差に等しい温度差をもって各熱源は対応できる。一方、
従来の冷凍機と熱交換器とが密閉配管で直列配列型のシ
ステムにおいては、各放熱器の利用温度差を冷凍機と、
蓄熱槽用の熱交換器とが合わせて受け持つ事となり各熱
源の処理する温度差は小さい。このように本方式は従来
方式と比較し各熱源の温度処理範囲を高くすることがで
きる。日中、最大負荷量に対し50%蓄熱の場合には熱
交換器(蓄熱槽)からの取り出した熱量を搬送するポン
プと、不足分への対応をするポンプを、主管の相対する
位置に設置しそれぞれのポンプの吐出流が主管内部を対
向して流れるようにする。両端に設置した2台のポンプ
より供給された冷温水は、両端より主管からの分岐管を
介し各放熱器に分割供給され、最終的には主管の半ばで
最後の放熱器に両方のポンプより供給された冷温水がそ
の必要量として分岐管を介し供給される。2台のポンプ
は、各放熱器が必要とするその量と場所とを受け持ち分
担する。最大負荷時においては、両者が2等分して分担
し合うが、その他の場合には、蓄熱槽の熱の利用が過半
数を占めるように制御をする。最大負荷時には、搬送動
力は激減し、省エネ、と電力費の削減ができる。等々の
優れた効果を奏することができる。As described in detail above, according to the present invention,
In this heat storage device, two main pipes can be used for both heat storage and heat release, and the thickness of the pipe can be made smaller than that of the conventional one. When dealing with heat dissipation at the maximum load, compared to the conventional system, the amount of circulation occupied by each pump and the area shared by the radiator 3 can be reduced to about half, and not only the power consumption of each pump, Their total consumption can be reduced. In addition, the amount of circulation is reduced by half compared with the conventional method, and the thickness of the piping can be reduced, so that the construction cost can be reduced. At the time of daytime heat radiation of the present apparatus, when the daytime load is equal to or greater than the heat storage amount, that is, when the heat of the heat storage tank and the heat of the heat source device are simultaneously used via the heat exchanger, the difference between the use temperature of each radiator is equal. Each heat source can respond with a temperature difference. on the other hand,
In a conventional system in which a refrigerator and a heat exchanger are arranged in series with a closed pipe, a difference in the use temperature of each radiator is determined by a refrigerator,
The heat exchanger for the heat storage tank also serves as the heat exchanger, and the difference in the temperature to be processed by each heat source is small. Thus, the present system can increase the temperature processing range of each heat source as compared with the conventional system. In the daytime, when the heat load is 50% of the maximum load, a pump that conveys the amount of heat extracted from the heat exchanger (heat storage tank) and a pump that responds to the shortage are installed at positions opposite to the main pipe. Then, the discharge flows of the respective pumps are made to flow in the main pipe so as to face each other. The cold and hot water supplied from the two pumps installed at both ends is divided and supplied to each radiator through the branch pipe from the main pipe from both ends, and finally the last radiator from both pumps in the middle of the main pipe The supplied cold and hot water is supplied as a required amount through a branch pipe. The two pumps share and share the amount and location required by each radiator. At the time of the maximum load, the two are equally divided and shared, but in other cases, the control is performed so that the use of the heat of the heat storage tank occupies the majority. At the maximum load, the transfer power is drastically reduced, which can save energy and reduce electricity costs. Excellent effects can be achieved.
【図1】本発明の実施形態に係わる蓄熱装置の全体構成
図である。FIG. 1 is an overall configuration diagram of a heat storage device according to an embodiment of the present invention.
【図2】同装置の冷房蓄熱時の運転状況説明図である。FIG. 2 is an explanatory diagram of an operation state of the device during cooling heat storage.
【図3】同装置の冷房放熱時の運転状況説明図である。FIG. 3 is an explanatory diagram of an operation state of the device at the time of cooling and heat radiation.
【図4】同装置の暖房蓄熱時の運転状況説明図である。FIG. 4 is an explanatory diagram of an operation state of the device during heating and heat storage.
【図5】同装置の暖房放熱時の運転状況説明図である。FIG. 5 is an explanatory diagram showing an operation state of the device at the time of heat radiation.
【図6】本発明の第2実施形態に係わる蓄熱装置の全体
構成図である。FIG. 6 is an overall configuration diagram of a heat storage device according to a second embodiment of the present invention.
【図7】同装置の冷房蓄熱時の運転状況説明図である。FIG. 7 is an explanatory diagram of an operation state of the device during cooling heat storage.
【図8】同装置の冷房放熱時の運転状況説明図である。FIG. 8 is an explanatory diagram of an operation state of the device at the time of cooling and heat radiation.
【図9】同装置の暖房蓄熱時の運転状況説明図である。FIG. 9 is an explanatory diagram of an operation state of the device during heating and heat storage.
【図10】同装置の暖房放熱時の運転状況説明図であ
る。FIG. 10 is an explanatory diagram of an operation state of the device at the time of heat radiation.
【図11】従来の蓄熱装置の全体構成図である。FIG. 11 is an overall configuration diagram of a conventional heat storage device.
【図12】他の形態の従来の蓄熱装置の全体構成図であ
る。FIG. 12 is an overall configuration diagram of another conventional heat storage device.
1 冷熱温熱兼用冷凍機 2 第1ポンプ 3 放熱器 4 熱交換器 5 第2ポンプ 6 逆止弁 7、7A 制御弁 8 第1切替え弁 9 第2切替え弁 10 制御装置 11 蓄熱槽 12 循環ポンプ 13、14 分岐切替え弁 15 隔壁 16 連通管 17 低温槽 18 高温槽 REFERENCE SIGNS LIST 1 cold / heat / heat refrigerating machine 2 first pump 3 radiator 4 heat exchanger 5 second pump 6 check valve 7, 7A control valve 8 first switching valve 9 second switching valve 10 control device 11 heat storage tank 12 circulation pump 13 , 14 Branch switching valve 15 Partition wall 16 Communication pipe 17 Low temperature tank 18 High temperature tank
Claims (12)
回路内に、熱源機とこの熱源機に流体を供給する第1ポ
ンプと熱交換器とをこの順で直列に配置し、さらに前記
熱源機と第1ポンプおよび熱交換器に対して並列に複数
の管路を設け、これら夫々の管路に放熱器を配置し、さ
らに前記熱交換器に対して前記とは別の並列管路を設け
この管路内に第2ポンプを配置し、また前記熱交換器に
は密閉型流体回路とは別に蓄熱槽からの流体を循環させ
ることができる蓄熱流体回路を接続してなり、 前記密閉型流体回路内の熱源機と第一ポンプとを運転し
て前記熱源機により密閉型流体回路内の流体を冷却また
は加熱し、この冷却または加熱した流体を前記熱交換器
に流して前記蓄熱流体回路内の流体を冷熱または加熱し
て蓄熱槽内に蓄熱する第一過程と、前記密閉型流体回路
内の熱源機と第一ポンプとを必要に応じて運転して前記
熱源機によって密閉型流体回路内の流体を冷却または加
熱し、冷却または加熱された流体を前記放熱器に循環さ
せるとともに、前記第二ポンプを運転して前記密閉型流
体回路内の流体を前記熱交換器に供給して前記蓄熱流体
回路の流体によって冷却または加熱し、この流体を前記
放熱器に前記第1ポンプからの流れと対向する方向に流
して冷房または暖房する第二過程とを選択できるように
したことを特徴とする蓄熱装置。1. A heat source device, a first pump for supplying a fluid to the heat source device, and a heat exchanger are arranged in series in this order in a sealed fluid circuit capable of circulating a fluid. A plurality of pipelines are provided in parallel with the heat pump, the first pump and the heat exchanger, a radiator is arranged in each of these pipelines, and another parallel pipeline is provided for the heat exchanger. A second pump is disposed in the pipe, and a heat storage fluid circuit capable of circulating fluid from a heat storage tank is connected to the heat exchanger separately from the closed fluid circuit; The heat source device in the fluid circuit and the first pump are operated to cool or heat the fluid in the closed fluid circuit by the heat source device, and the cooled or heated fluid is caused to flow through the heat exchanger so that the heat storage fluid circuit First to cool or heat the fluid in the tank and store heat in the heat storage tank Process, the heat source device and the first pump in the closed type fluid circuit are operated as necessary to cool or heat the fluid in the closed type fluid circuit by the heat source device, and the cooled or heated fluid is cooled. While circulating through the radiator, the second pump is operated to supply the fluid in the closed fluid circuit to the heat exchanger, and is cooled or heated by the fluid in the heat storage fluid circuit. A second step of cooling or heating by flowing in a direction opposite to the flow from the first pump.
熱源機に直列に接続され前記熱源機に流体を供給する第
1ポンプとを配置し、地上側の階に熱交換器を配置し、
これらを密閉型流体回路で直列に接続し、さらに、この
密閉型流体回路内の前記熱源機、第1ポンプと熱交換器
の間の各階毎に前記熱源機と第1ポンプに対して並列の
管路を形成して各管路内に放熱器を配置し、また、前記
熱交換器に対して地上側に並列に管路を形成し、該管路
内に第2ポンプを配置し、また前記熱交換器には密閉型
流体回路とは別に蓄熱槽からの流体を循環させることが
できる大気開放型の蓄熱流体回路を接続して流体回路を
構成し、 前記密閉型流体回路内の第一ポンプを運転して前記熱源
機により密閉型流体回路内の流体を冷却または加熱し、
この冷却または加熱した流体を前記熱交換器に流して前
記蓄熱回路内の流体を冷熱または加熱して蓄熱槽内に蓄
熱する第一過程と、前記密閉型流体回路内の熱源機と第
一ポンプとを必要に応じて運転して前記熱源機によって
密閉型流体回路内の流体を冷却または加熱し、冷却また
は加熱された流体を前記上階から下階の放熱器に向けて
循環させるとともに、前記第二ポンプを運転して前記密
閉型流体回路内の流体を前記熱交換器に供給して前記蓄
熱流体回路の流体によって冷却または加熱し、この流体
を下階から上階の放熱器に向けて前記第1ポンプからの
流れに対向する方向に流して冷房または暖房する第二過
程とを選択できるようにしたことを特徴とする蓄熱装
置。2. A heat source unit and a first pump connected in series to the heat source unit and supplying a fluid to the heat source unit are arranged on an upper floor of a building having a plurality of floors, and a heat exchanger is provided on a floor on the ground side. Place,
These are connected in series by a closed fluid circuit, and furthermore, the heat source device in this closed fluid circuit, and the heat source device and the first pump are connected in parallel to each floor between the first pump and the heat exchanger. Forming a pipe and disposing a radiator in each of the pipes, forming a pipe in parallel on the ground side with respect to the heat exchanger, disposing a second pump in the pipe, The heat exchanger is connected to an open-to-atmosphere type heat storage fluid circuit capable of circulating fluid from a heat storage tank separately from the closed type fluid circuit to form a fluid circuit. By operating a pump to cool or heat the fluid in the closed fluid circuit by the heat source device,
A first step of flowing the cooled or heated fluid through the heat exchanger to cool or heat the fluid in the heat storage circuit and store heat in the heat storage tank; a heat source unit and a first pump in the closed fluid circuit By operating as necessary, the heat source device cools or heats the fluid in the sealed fluid circuit, and circulates the cooled or heated fluid from the upper floor to the lower floor radiator, By operating the second pump, the fluid in the closed type fluid circuit is supplied to the heat exchanger and cooled or heated by the fluid of the heat storage fluid circuit, and the fluid is directed from the lower floor to the radiator on the upper floor. A heat storage device characterized in that a second step of cooling or heating by flowing in a direction opposite to the flow from the first pump can be selected.
とを特徴とする請求項1または請求項2に記載の蓄熱装
置。3. The heat storage device according to claim 1, wherein the heat source device is a cooling / heating / heating refrigerator.
とを特徴とする請求項1〜請求項3のいずれかに記載の
蓄熱装置。4. The heat storage device according to claim 1, wherein a control valve is provided upstream of each of the radiators.
気開放型であり、該回路内には蓄熱槽と循環ポンプと切
替え弁とを備えてなることを特徴とする請求項1〜請求
項4のいずれかに記載の蓄熱装置。5. The heat storage fluid circuit connected to the heat exchanger is open to the atmosphere, and the circuit includes a heat storage tank, a circulation pump, and a switching valve. Item 5. A heat storage device according to any one of Items 4.
じ断面積からなることを特徴とする請求項1〜請求項5
のいずれかに記載の蓄熱装置。6. A pipeline constituting the closed fluid circuit has substantially the same cross-sectional area.
A heat storage device according to any one of the above.
び熱交換器と接続する管路の合流部には第2切替え弁を
設けるとともに前記第2ポンプの吐出側と熱交換器とを
接続する管路内には第1切替え弁を設け、さらに第1切
替え弁は第2切替え弁と第1ポンプ吸入側とを接続する
管路に接続されていることを特徴とする請求項1〜請求
項6のいずれかに記載の蓄熱装置。7. A second switching valve is provided at a junction of a first pump suction side, a second pump suction side, and a pipe connected to a heat exchanger, and a discharge side of the second pump is connected to the heat exchanger. A first switching valve is provided in the connecting pipe, and the first switching valve is connected to a pipe connecting the second switching valve and the first pump suction side. The heat storage device according to claim 6.
略同じであることを特徴とする請求項1〜請求項7のい
ずれかに記載の蓄熱装置。8. The heat storage device according to claim 1, wherein said first pump and said second pump have substantially the same capacity.
の略対称位置に配置されていることを特徴とする請求項
1〜請求項8のいずれかに記載の蓄熱装置。9. The heat storage device according to claim 1, wherein the heat source unit and the heat exchanger are arranged at substantially symmetric positions in a closed fluid circuit.
ことを特徴とする請求項1〜請求項9のいずれかに記載
の蓄熱装置。10. The heat storage device according to claim 1, wherein a check valve is disposed on a discharge side of the heat source device.
求項1〜請求項10のいずれかに記載の蓄熱装置。11. The heat storage device according to claim 1, wherein the fluid is water.
第一ポンプ、第2ポンプの吐出流量を変化することがで
きるようにしたことを特徴とする請求項1〜請求項11
のいずれかに記載の蓄熱装置。12. The method according to claim 1, wherein in the second step, the discharge flow rates of the first pump and the second pump can be changed according to the amount of heat radiation.
A heat storage device according to any one of the above.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28229799A JP3689283B2 (en) | 1999-10-04 | 1999-10-04 | Heat storage device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28229799A JP3689283B2 (en) | 1999-10-04 | 1999-10-04 | Heat storage device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001108385A true JP2001108385A (en) | 2001-04-20 |
| JP3689283B2 JP3689283B2 (en) | 2005-08-31 |
Family
ID=17650598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28229799A Expired - Fee Related JP3689283B2 (en) | 1999-10-04 | 1999-10-04 | Heat storage device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3689283B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004012025A (en) * | 2002-06-06 | 2004-01-15 | Sapio Kk | Hybrid energy system |
| KR20120039275A (en) * | 2010-10-15 | 2012-04-25 | 주식회사 삼양발부종합메이커 | Automatic control system of constant flow considering in apartment com-plex |
| KR101348250B1 (en) | 2013-11-06 | 2014-01-08 | 이창흠 | Multipurpose cooling system by controlling flow of brine |
| JP2015090246A (en) * | 2013-11-06 | 2015-05-11 | 株式会社ササクラ | Air conditioning system |
| WO2016113937A1 (en) * | 2015-01-15 | 2016-07-21 | 三菱電機株式会社 | Thermal storage air conditioning system |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013036658A (en) * | 2011-08-08 | 2013-02-21 | Yamato:Kk | Cooling system |
-
1999
- 1999-10-04 JP JP28229799A patent/JP3689283B2/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004012025A (en) * | 2002-06-06 | 2004-01-15 | Sapio Kk | Hybrid energy system |
| KR20120039275A (en) * | 2010-10-15 | 2012-04-25 | 주식회사 삼양발부종합메이커 | Automatic control system of constant flow considering in apartment com-plex |
| KR101674202B1 (en) | 2010-10-15 | 2016-11-09 | 주식회사 삼양발브종합메이커 | Automatic control system of constant flow considering in apartment com-plex |
| KR101348250B1 (en) | 2013-11-06 | 2014-01-08 | 이창흠 | Multipurpose cooling system by controlling flow of brine |
| JP2015090246A (en) * | 2013-11-06 | 2015-05-11 | 株式会社ササクラ | Air conditioning system |
| WO2016113937A1 (en) * | 2015-01-15 | 2016-07-21 | 三菱電機株式会社 | Thermal storage air conditioning system |
| JPWO2016113937A1 (en) * | 2015-01-15 | 2017-06-01 | 三菱電機株式会社 | Thermal storage air conditioning system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3689283B2 (en) | 2005-08-31 |
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