JP3138784B2 - Adsorption refrigeration system with heat storage function and its operation method - Google Patents

Adsorption refrigeration system with heat storage function and its operation method

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Publication number
JP3138784B2
JP3138784B2 JP04357178A JP35717892A JP3138784B2 JP 3138784 B2 JP3138784 B2 JP 3138784B2 JP 04357178 A JP04357178 A JP 04357178A JP 35717892 A JP35717892 A JP 35717892A JP 3138784 B2 JP3138784 B2 JP 3138784B2
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JP
Japan
Prior art keywords
heat
heat storage
adsorption
refrigerant
refrigeration system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP04357178A
Other languages
Japanese (ja)
Other versions
JPH06193994A (en
Inventor
治男 久木
聰 伊部
泰夫 米沢
昌生 松下
淳 森川
章義 酒井
正佳 秦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP04357178A priority Critical patent/JP3138784B2/en
Publication of JPH06193994A publication Critical patent/JPH06193994A/en
Application granted granted Critical
Publication of JP3138784B2 publication Critical patent/JP3138784B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、コージェネレーション
システムに好適な吸着式冷凍システムに係り、詳しく
は、ガスエンジン等から排出される低レベルの排熱源を
利用して、大気温度より低温レベルの熱エネルギーを蓄
積し、必要なときにはこれを取り出して冷房等の低温熱
源に利用できる、蓄熱機能を有した吸着式冷凍システム
とその運転方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorption type refrigeration system suitable for a cogeneration system, and more particularly, to a system having a temperature lower than the atmospheric temperature by using a low level exhaust heat source discharged from a gas engine or the like. The present invention relates to an adsorption-type refrigeration system having a heat storage function, which can store thermal energy, take it out when necessary, and use it for a low-temperature heat source such as cooling, and a method of operating the same.

【0002】[0002]

【従来の技術】近年、省エネルギーシステムの一環とし
て、ガスエンジン等により発電機を回転させ、同時にガ
スエンジンの排熱により冷凍機器等を駆動するいわゆる
コージェネレーションシステムが注目されている。とこ
ろで、コージェネレーションシステムは、一般的に電力
と熱の需要が十分にある昼間を想定して設計されている
ため、電力需要だけが多くて、熱需要がほとんどない夜
間は効率的な運転ができず、利用者の多くは、昼間だけ
このシステムを使用し、夜間になると買電に切り換える
使い方をしている。しかし、このことからコージェネレ
ーションシステムの運転時間は短くなり、それにつれて
償却年数が長くなり、そのために、システム導入を見合
わすケースもしばしばみられるようになってきている。
2. Description of the Related Art In recent years, as a part of an energy saving system, a so-called cogeneration system in which a generator is rotated by a gas engine or the like, and at the same time, refrigeration equipment or the like is driven by exhaust heat of the gas engine has attracted attention. By the way, cogeneration systems are generally designed for the daytime when power and heat demands are sufficient, so that efficient operation can be performed at night when there is only a large demand for power and little heat demand. Many users use this system only in the daytime and switch to power purchase at night. However, the operation time of the cogeneration system has been shortened, and the depreciation period has been lengthened accordingly. As a result, there are many cases in which the introduction of the system is delayed.

【0003】そこで、コージェネレーションシステムを
夜間も効率的に運転可能とすることが求められ、その解
決手段として、例えば実開平3ー46165号公報に、
蓄熱機能を備えたコージェネレーションシステムが記載
されている。具体的に述べると、熱需要のない夜間等
は、エンジンシステムより排出される排熱を熱源として
吸収式冷凍機を運転し、そのとき発生する冷熱を冷水と
して蓄熱槽に溜めておき、これを昼間等の冷熱必要時に
利用可能としたシステムである。
Therefore, it is required that the cogeneration system can be operated efficiently even at night, and as a solution to this problem, for example, Japanese Utility Model Laid-Open No. 3-46165 discloses
A cogeneration system with a heat storage function is described. Specifically, at night or the like when there is no demand for heat, the absorption refrigerator is operated using the exhaust heat discharged from the engine system as a heat source, and the cold generated at that time is stored in a heat storage tank as cold water, and this is stored. This system can be used when cold heat is required, such as during the day.

【0004】[0004]

【発明が解決しようとする課題】しかし、このシステム
の場合、前記運転上の問題は解決されるにしても、その
蓄熱方法が冷凍機生成の冷熱を顕熱として蓄熱するもの
であるため、蓄熱槽が大型化し、システムが巨大化する
という問題があった。本発明は係る実状に対処して、蓄
熱に際して、蓄熱材を相変化させて蓄熱をはかるように
した吸着式冷凍機利用の冷凍システムを提案して、蓄熱
槽の小型化、軽量化をはかり、コージェネレーションシ
ステムの一層の普及に寄与することを目的とするもので
ある。
However, in the case of this system, even if the above-mentioned operational problem is solved, since the heat storage method is to store cold heat generated by the refrigerator as sensible heat, heat is stored. There was a problem that the tank became large and the system became huge. The present invention addresses such a situation, and proposes a refrigeration system using an adsorption-type refrigerator in which heat is stored by changing the phase of a heat storage material during heat storage, to reduce the size and weight of the heat storage tank. The purpose is to contribute to the further spread of cogeneration systems.

【0005】[0005]

【課題を解決するための手段】すなわち、上記目的に適
合する本発明の特徴は、吸着剤を充填した複数の吸着塔
を使用し、各吸着塔内を冷媒が循環可能なる如く凝縮器
及び蒸発器に接続すると共に、少なくとも一基の吸着塔
が他と異なる工程となる如く、吸着、脱着工程切換え運
転される吸着式冷凍機の前記蒸発器と、前記吸着式冷凍
機の冷媒に比して凝固点の高い物質を蓄熱材として充填
した蓄熱槽とを、熱媒体の循環する配管により接続し、
該配管途中に冷熱取り出し部を三方弁を介して並列接続
して、蓄熱機能を有した吸着式冷凍システムを構成した
ことにある。
That is, a feature of the present invention that meets the above-mentioned object is that a plurality of adsorption towers filled with an adsorbent are used, and a condenser and an evaporator are provided so that a refrigerant can circulate in each adsorption tower. Along with the evaporator of the adsorption refrigerating machine operated to switch the adsorption and desorption processes so that at least one of the adsorption towers is in a different step from the other, and the refrigerant of the adsorption refrigerating machine, A heat storage tank filled with a material with a high freezing point as a heat storage material is connected by a pipe that circulates a heat medium,
A cooling heat extraction unit is connected in parallel in the middle of the pipe via a three-way valve to constitute an adsorption refrigeration system having a heat storage function.

【0006】請求項2、請求項3に記載した発明は、上
記構成における吸着剤、活性炭及び冷媒を具体的に示し
たもので、請求項2の場合は、吸着剤として活性炭、冷
媒としてアルコール、蓄熱材として水を用い、また、請
求項3記載の発明では、吸着剤としてシリカゲル、冷媒
として水、蓄熱材としてクラスレートを用いることを特
徴とする。
The inventions described in claims 2 and 3 specifically show the adsorbent, activated carbon and refrigerant in the above configuration. In the case of claim 2, activated carbon as the adsorbent, alcohol as the refrigerant, Water is used as the heat storage material, and the invention according to claim 3 is characterized in that silica gel is used as the adsorbent, water is used as the refrigerant, and clathrate is used as the heat storage material.

【0007】また、請求項4記載の発明は、上記冷凍シ
ステムの運転方法を示したもので、蒸発器より出力され
る冷熱を熱媒体を介し蓄熱槽内へ循環させることにより
蓄熱材を凝固させて蓄熱をはかり、その後、三方弁を切
り換えて、蒸発器より出力される冷熱と蓄熱した冷熱と
を、または、蓄熱した冷熱のみを、熱媒体を介して冷熱
取り出し部より利用側へ取り出す運転方法を特徴として
いる。
The invention according to a fourth aspect of the present invention relates to a method of operating the refrigeration system, wherein the heat storage material is solidified by circulating the cold output from the evaporator through the heat medium into the heat storage tank. An operation method in which the three-way valve is switched and then the three-way valve is switched, and the cold heat output from the evaporator and the stored cold heat, or only the stored cold heat, is extracted from the cold heat extraction unit to the utilization side via a heat medium. It is characterized by.

【0008】[0008]

【作用】本発明システムを上記本発明方法により運転す
るとき、吸着式冷凍機生成の冷熱は、熱媒体配管により
蓄熱槽内へ伝えられ、これにより蓄熱槽内の蓄熱材が相
変化して冷熱が蓄熱される。なお、このとき、蓄熱材と
冷媒との凝固点の違いにより、蓄熱槽内での蓄熱材の凝
固に対しても、吸着式冷凍機内では冷媒が凝固せず、そ
の結果、同冷凍機は不都合なく冷熱を発生し続け、上記
蓄熱をスムーズに進行させる。
When the system of the present invention is operated according to the above-described method of the present invention, the cold generated by the adsorption type refrigerator is transmitted to the heat storage tank by the heat medium pipe, whereby the heat storage material in the heat storage tank undergoes a phase change and the cold heat is generated. Is stored. At this time, due to the difference in the freezing point between the heat storage material and the refrigerant, the refrigerant does not solidify in the adsorption refrigerator even with the solidification of the heat storage material in the heat storage tank, and as a result, the refrigerator has no inconvenience. Cold heat is continuously generated, and the heat storage proceeds smoothly.

【0009】また、吸着式冷凍機は、吸収式冷凍機等と
異なり内部で結晶化が起こらないため、かなり低温の冷
熱を生成可能である。具体的には、請求項2に記載した
ように、冷媒にアルコールを使用した場合であれば−1
0℃、請求項3に記載したように、冷媒に水を使用した
場合では3℃という温度レベルの冷熱も出力できる。従
って、夫々の場合の蓄熱材であるクラスレート(凝固点
約5℃)、水(凝固点0℃)を十分凝固させることがで
きる。
In addition, unlike an absorption refrigerator or the like, an adsorption refrigerator does not cause crystallization inside, and therefore can generate considerably low-temperature cold heat. Specifically, as described in claim 2, -1 if alcohol is used as the refrigerant.
As described in claim 3, when water is used as the refrigerant, it is possible to output cold heat at a temperature level of 3 ° C. Therefore, the clathrate (solidification point of about 5 ° C.) and water (solidification point of 0 ° C.), which are the heat storage materials in each case, can be sufficiently solidified.

【0010】さらに、冷熱を利用する場合は、熱媒体配
管に介設された三方弁を切り換えれば、冷熱取り出し部
より蓄熱冷熱を容易に取り出し可能となるが、このとき
吸着式冷凍機を駆動しておけば、蓄熱分はもとより、冷
凍機生成の冷熱をも取り出され、効率的な利用運転が実
現される。
[0010] Further, when utilizing cold heat, by switching the three-way valve interposed in the heat medium pipe, it is possible to easily take out the stored cold heat from the cold heat take-out portion. If this is done, not only the heat stored but also the cold generated by the refrigerator is taken out, and efficient utilization operation is realized.

【0011】[0011]

【実施例】以下、本発明の実施例を図面にもとづき説明
する。図1は、本発明に係る吸着式冷凍システムの配管
系統図である。図中、(1)は吸着式冷凍機、(2)は
蓄熱槽、(3)は熱交換器である。また、(4)は、前
記熱交換器(3)を介して吸着式冷凍システムに接続さ
れた利用側機器である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a piping diagram of the adsorption refrigeration system according to the present invention. In the figure, (1) is an adsorption refrigerator, (2) is a heat storage tank, and (3) is a heat exchanger. (4) is a user-side device connected to the adsorption refrigeration system via the heat exchanger (3).

【0012】まず、吸着式冷凍機(1)は、複数の吸着
塔(5)、例えば2基の吸着塔(図ではそのうちの1基
のみを示す)を備えた公知のものである。吸着塔(5)
内には、所定量の活性炭が吸着材(図示しない)が充填
され、この吸着材を加熱、冷却するために加熱用伝熱面
(6)と、冷却用伝熱面(7)とが配設されている。
First, the adsorption refrigerator (1) is a known type provided with a plurality of adsorption towers (5), for example, two adsorption towers (only one of them is shown in the figure). Adsorption tower (5)
A predetermined amount of activated carbon is filled with an adsorbent (not shown), and a heating heat transfer surface (6) and a cooling heat transfer surface (7) are arranged for heating and cooling the adsorbent. Has been established.

【0013】加熱用伝熱面(6)は、温水系配管(8)
に接続されたものであり、本システムをコージェネレー
ションシステムの一要素として活用する場合は、この温
水系配管(8)の先端に、例えばガスエンジンの排熱供
給機構が接続されることになる。一方、冷却用伝熱面
(7)は、冷却水系配管(9)を介して、クーリングタ
ワー(10)に接続されている。なお、(11)、(1
2)は、各配管(8)、(9)に介設された温水ポン
プ、冷却水ポンプである。
The heat transfer surface for heating (6) is a hot water system pipe (8).
When the present system is used as an element of a cogeneration system, for example, an exhaust heat supply mechanism of a gas engine is connected to the end of the hot water system piping (8). On the other hand, the cooling heat transfer surface (7) is connected to a cooling tower (10) via a cooling water system pipe (9). (11), (1)
2) is a hot water pump and a cooling water pump provided in each of the pipes (8) and (9).

【0014】また、この他、各吸着塔(5)と連通可能
に蒸発器(13)と凝縮器(図示を省略する)が配設さ
れ、各吸着塔(5)とこれら蒸発器(13)及び凝縮器
を接続する系内に冷媒として、所定量のアルコールが封
入されている。
In addition, an evaporator (13) and a condenser (not shown) are provided so as to be able to communicate with each adsorption tower (5), and each adsorption tower (5) and these evaporators (13) are provided. A predetermined amount of alcohol is sealed as a refrigerant in a system connecting the condenser and the condenser.

【0015】以上の冷凍機は、温水系配管(8)及び冷
却水系配管(9)を介して、各吸着塔(5)ごとに異な
る順序で温水、冷却水が供給されて作動する。すなわ
ち、温水、冷却水により各吸着材の加熱、冷却が繰り返
されると、一方の吸着材から冷媒が脱着されて凝縮器で
凝縮され、かつ他方では、他の吸着材により蒸発器(1
3)に付着した冷媒が吸着されて、蒸発器(13)から
冷媒が蒸発し、周知の冷凍サイクルが開始されることに
なる。
The above refrigerator operates by supplying hot water and cooling water in different orders for each adsorption tower (5) via a hot water system pipe (8) and a cooling water system pipe (9). That is, when heating and cooling of each adsorbent are repeated with hot water and cooling water, the refrigerant is desorbed from one adsorbent and condensed in the condenser, and on the other hand, the evaporator (1) is adsorbed by the other adsorbent.
The refrigerant adhering to 3) is adsorbed, the refrigerant evaporates from the evaporator (13), and a known refrigeration cycle is started.

【0016】次に、蓄熱槽(2)は、液体の蓄熱材を貯
溜したものである。その場合、例えば内部に多数の製氷
皿(図示せず)が配設されていて、各製氷皿に蓄熱材が
貯溜された形態となっている。蓄熱槽(2)中、(1
4)は伝熱管であり、前記製氷皿を巡って配設される。
Next, the heat storage tank (2) stores liquid heat storage material. In this case, for example, a number of ice trays (not shown) are provided inside, and a heat storage material is stored in each ice tray. In the heat storage tank (2), (1
4) is a heat transfer tube, which is disposed around the ice tray.

【0017】なお、本発明の場合、蓄熱槽(2)の中に
貯溜する蓄熱材の選定については特に重要で、その条件
として、前記吸着式冷凍機(1)の冷媒に比して凝固点
の高いことが求められる。例えば、冷媒として前記アル
コールを使用している場合は、その凝固点−100℃よ
りも高い、凝固点0℃の水が使用される。また、一般的
に冷媒として水を使用し、吸着剤としてシリカゲルを用
いた吸着式冷凍機も多く、こうした冷凍機に対しては、
凝固点5℃のクラスレートが蓄熱材として使用される。
In the case of the present invention, the selection of the heat storage material to be stored in the heat storage tank (2) is particularly important, and the condition is that the solidification point of the heat storage material is lower than that of the refrigerant of the adsorption refrigerator (1). It is required to be high. For example, when the alcohol is used as a refrigerant, water having a freezing point of 0 ° C. higher than its freezing point of −100 ° C. is used. Also, in general, there are many adsorption refrigerators using water as a refrigerant and silica gel as an adsorbent.
A clathrate with a freezing point of 5 ° C. is used as the heat storage material.

【0018】そして、以上の吸着式冷凍機(1)、蓄熱
槽(2)及び前記熱交換器(3)により、本発明冷凍シ
ステムが構成されることになるが、その場合、吸着式冷
凍機(1)の蒸発器(13)及び蓄熱槽(2)の伝熱管
(14)を経て、前記熱交換器(3)へと循環する熱媒
液配管(15)が設けられ、さらにこの熱媒液配管(1
5)に、伝熱管(14)をバイパスするバイパス配管
(16)と、熱交換器(3)をバイパスするバイパス配
管(17)とが、夫々三方弁(18)、(19)を介し
て接続されて、全体のシステムが構成される。なお、
(20)は熱媒液を循環させるための循環ポンプであ
る。
The refrigeration system of the present invention is constituted by the adsorption refrigerator (1), the heat storage tank (2) and the heat exchanger (3). In this case, the adsorption refrigerator is used. A heat medium liquid pipe (15) that circulates through the evaporator (13) of (1) and the heat transfer pipe (14) of the heat storage tank (2) to the heat exchanger (3) is provided. Liquid piping (1
5), a bypass pipe (16) that bypasses the heat transfer pipe (14) and a bypass pipe (17) that bypasses the heat exchanger (3) are connected via three-way valves (18) and (19), respectively. Thus, the entire system is configured. In addition,
(20) is a circulation pump for circulating the heat medium liquid.

【0019】次に、以上の吸着式冷凍システムの運転方
法として、夜間等に行われる蓄熱運転について、まず説
明する。この場合、三方弁(18)については、バイパ
ス配管(16)を閉鎖する方向へ、すなわち熱媒体が伝
熱管(14)を流れる方向に切り換える。また、三方弁
(19)については、バイパス配管(17)を開放する
方向へ、すなわち熱媒体が熱交換器(3)を流れない方
向へ切り換える。
Next, as an operation method of the adsorption refrigeration system, a heat storage operation performed at night or the like will be described first. In this case, the three-way valve (18) is switched to a direction in which the bypass pipe (16) is closed, that is, a direction in which the heat medium flows through the heat transfer pipe (14). Further, the three-way valve (19) is switched to a direction in which the bypass pipe (17) is opened, that is, a direction in which the heat medium does not flow through the heat exchanger (3).

【0020】そしてこの状態で吸着式冷凍機(1)を運
転し、循環ポンプ(20)を駆動すると、吸着式冷凍機
(1)の蒸発器(13)において、−10℃程度の冷熱
が発生し、これが熱媒体を介して伝熱管(14)へと伝
えられ、凝固点0℃の蓄熱材は、冷却されて氷へと相変
化する。この結果、蓄熱槽(2)内に冷熱が氷となって
蓄熱されることになる。なお、冷媒として水を使用して
いる場合は、冷凍機(1)側で3℃程度の冷熱が生成さ
れ、これが凝固点5℃のクラスレートを凝固させて、蓄
熱がなされる。
In this state, when the adsorption type refrigerator (1) is operated and the circulation pump (20) is driven, cold heat of about -10 ° C. is generated in the evaporator (13) of the adsorption type refrigerator (1). This is transmitted to the heat transfer tube (14) via the heat medium, and the heat storage material having a freezing point of 0 ° C. is cooled and changes into ice. As a result, the cold heat is stored in the heat storage tank (2) as ice. In the case where water is used as the refrigerant, cold heat of about 3 ° C. is generated on the side of the refrigerator (1), and this cools the clathrate having a freezing point of 5 ° C. to store heat.

【0021】一方、昼間等に行う、この蓄熱槽(2)か
ら冷熱を取り出す利用運転については、三方弁(18)
を、バイパス配管(16)を開放する方向へ、すなわち
熱媒体が伝熱管(14)を流れない方向へ切り換え、三
方弁(19)を、バイパス配管(17)を閉鎖する方
向、すなわち熱媒体が熱交換器(3)を流れる方向へ切
り換える。そして、冷凍機(1)駆動と共に、循環ポン
プ(20)を駆動する。
On the other hand, in the utilization operation for extracting cold heat from the heat storage tank (2) during the daytime or the like, a three-way valve (18)
To the direction in which the bypass pipe (16) is opened, that is, the direction in which the heat medium does not flow through the heat transfer pipe (14), and the three-way valve (19) is closed in the direction to close the bypass pipe (17), that is, the heat medium is Switch to the direction of flow through the heat exchanger (3). Then, the circulation pump (20) is driven together with the driving of the refrigerator (1).

【0022】以上の操作により、熱媒体は、蒸発器(1
3)、伝熱面(14)を経て熱交換器(3)へ至り、そ
の間に蓄熱槽(2)内の蓄熱材を解氷して、冷凍機
(1)生成の冷熱と共に、蓄熱冷熱をも熱交換器(3)
へ送る。これにより、利用側(4)へは、冷凍機生成の
冷熱と蓄熱した冷熱の双方が取り出されることになる。
その場合、吸着式冷凍機(1)を停止すれば、蓄熱分だ
けを利用側(4)へ取り出すことも可能であり、適宜、
その利用方法は選択できる。
By the above operation, the heat medium is supplied to the evaporator (1).
3), reaching the heat exchanger (3) via the heat transfer surface (14), during which the heat storage material in the heat storage tank (2) is thawed, and together with the cold generated by the refrigerator (1), the heat storage cold is generated. Also heat exchanger (3)
Send to As a result, both the cold generated by the refrigerator and the stored cold are extracted to the use side (4).
In that case, if the adsorption refrigerator (1) is stopped, it is possible to take out only the heat storage to the use side (4).
You can choose how to use it.

【0023】また、吸着式冷凍機(1)を運転しつつ、
三方弁(18)をバイパス配管(16)開放側へ切り換
えれば、蓄熱量を保存したまま、冷凍機(1)生成の冷
熱だけを取り出すこともでき、利用運転時の能力制御が
簡単に行えることになる。
Further, while operating the adsorption refrigerator (1),
If the three-way valve (18) is switched to the open side of the bypass pipe (16), only the cold generated by the refrigerator (1) can be taken out while keeping the heat storage amount, and the capacity control during the use operation can be easily performed. Will be.

【0024】[0024]

【発明の効果】本発明は、以上説明したように、吸着式
冷凍機の蒸発器と、前記吸着式冷凍機の冷媒に比して凝
固点の高い物質を蓄熱材として充填した蓄熱槽とを、熱
媒体の循環する配管により接続し、該配管途中に三方弁
を介して冷熱取り出し部を並列接続したものであるか
ら、熱需要のない時間帯の排熱により吸着式冷凍機を駆
動して、その冷熱を蓄熱しておくことができ、コージェ
ネレーションシステム等の排熱利用システムにおける連
続運転が可能となる。従って、こうした排熱利用システ
ムの経済性向上、用途拡大に効果を奏する。
As described above, the present invention comprises an evaporator of an adsorption refrigerator and a heat storage tank filled with a substance having a higher freezing point than the refrigerant of the adsorption refrigerator as a heat storage material. It is connected by piping that circulates the heat medium, and since the cold heat extraction unit is connected in parallel via a three-way valve in the middle of the piping, the adsorption refrigerator is driven by exhaust heat during the time when there is no heat demand, The cold heat can be stored, and continuous operation in a waste heat utilization system such as a cogeneration system can be performed. Therefore, it is effective in improving the economic efficiency and expanding the use of such a waste heat utilization system.

【0025】また、本発明システムにおいて、その蓄熱
は、蓄熱材の相変化による潜熱の大きい蓄熱であるか
ら、蓄熱槽の小型化、軽量化が達成され、ひいては、シ
ステムの運転費、設備費が軽減される。
In the system of the present invention, the heat storage is a large amount of latent heat due to the phase change of the heat storage material, so that the heat storage tank can be reduced in size and weight, and the operating and equipment costs of the system can be reduced. It is reduced.

【0026】なお、請求項2及び3記載の発明は、冷
媒、蓄熱材等を具体的に示したもので、上記効果が同様
に達成される。
The invention according to claims 2 and 3 specifically shows a refrigerant, a heat storage material, and the like, and the above-mentioned effects can be similarly achieved.

【0027】さらに、請求項3記載の方法により以上の
吸着式冷凍システムを運転することにより、上記システ
ムにおける蓄熱運転も利用運転も容易にでき、とりわ
け、冷熱を取り出す際に蓄熱分と共に冷凍機生成の冷熱
を取り出せば、利用側へ極めて多大の冷熱を、簡単かつ
効率的に供給することができる。そしてまた、こうした
利用運転ができることから、本発明システムでは、夜間
蓄熱しておけば、その蓄熱分で昼間の負荷の略半分をま
かなえることになり、従って、設置する吸着式冷凍機容
量は従来の1/2でもよく、設備費軽減にも効果を発揮
する。
Further, by operating the above adsorption type refrigeration system by the method according to the third aspect, the heat storage operation and the utilization operation in the system can be facilitated. In particular, when the cold heat is taken out, the refrigerator is generated together with the heat storage component. , It is possible to easily and efficiently supply an extremely large amount of cold heat to the user side. Further, since such utilization operation can be performed, in the system of the present invention, if the heat is stored at night, the heat storage can cover approximately half of the load in the daytime, and therefore, the capacity of the installed adsorbent chiller is the conventional capacity. It may be 1/2, which is also effective for reducing equipment costs.

【0028】なお、以上のように、本発明に係る吸着冷
凍システムは、低温で相変化する蓄熱材を使用するた
め、食品加工や冷蔵等の産業用の低温用途に好適であ
る。
As described above, the adsorption refrigeration system according to the present invention uses a heat storage material that changes phase at a low temperature, and thus is suitable for industrial low temperature applications such as food processing and refrigeration.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明に係る蓄熱機能を有した吸着式冷凍シス
テムの説明図である。
FIG. 1 is an explanatory diagram of an adsorption refrigeration system having a heat storage function according to the present invention.

【符号の説明】[Explanation of symbols]

(1) 吸着式冷凍機 (2) 蓄熱槽 (3) 熱交換器 (4) 利用側機器 (5) 吸着塔 (13) 蒸発器 (15) 熱媒液循環配管 (19) 三方弁 (1) Adsorption type refrigerator (2) Heat storage tank (3) Heat exchanger (4) User side equipment (5) Adsorption tower (13) Evaporator (15) Heat medium liquid circulation pipe (19) Three-way valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊部 聰 大阪市中央区平野町4丁目1番2号 大 阪瓦斯株式会社内 (72)発明者 米沢 泰夫 大阪市西淀川区姫里1丁目5番10号 西 淀空調機株式会社内 (72)発明者 松下 昌生 大阪市西淀川区姫里1丁目5番10号 西 淀空調機株式会社内 (72)発明者 森川 淳 大阪市西淀川区姫里1丁目5番10号 西 淀空調機株式会社内 (72)発明者 酒井 章義 大阪市西淀川区姫里1丁目5番10号 西 淀空調機株式会社内 (72)発明者 秦 正佳 大阪市西淀川区姫里1丁目5番10号 西 淀空調機株式会社内 (56)参考文献 特開 平4−236076(JP,A) 特開 昭63−194165(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 17/08 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Satoshi Ibe 4-1-2, Hirano-cho, Chuo-ku, Osaka-shi Inside Osaka Gas Co., Ltd. Inside Nishiyodo Air Conditioner Co., Ltd. (72) Inventor Masao Matsushita 1-5-10 Himezato, Nishiyodogawa-ku, Osaka City Inside Nishiyodo Air Conditioner Co., Ltd. Inside Nishi-Yodo Air Conditioner Co., Ltd. (72) Inventor Akiyoshi Sakai 1-5-10 Himezato, Nishiyodogawa-ku, Osaka City Inside Nishi-Yodo Air Conditioner Co., Ltd. (56) References JP-A-4-236076 (JP, A) JP-A-63-194165 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F25B 17/08

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 吸着剤を充填した複数の吸着塔を使用
し、各吸着塔内を冷媒が循環可能なる如く凝縮器及び蒸
発器に接続すると共に、少なくとも一基の吸着塔が他と
異なる工程となる如く、吸着、脱着工程切換え運転を可
能ならしめた吸着式冷凍機の前記蒸発器と、前記吸着式
冷凍機の冷媒に比して凝固点の高い物質を蓄熱材として
充填した蓄熱槽とを、熱媒体の循環する配管により接続
し、該循環配管途中に三方弁を介して利用側への冷熱取
り出し部を並列に設けたことを特徴とする蓄熱機能を有
した吸着式冷凍システム。
1. A process in which a plurality of adsorption towers filled with an adsorbent are used and connected to a condenser and an evaporator so that a refrigerant can circulate in each of the adsorption towers, and at least one of the adsorption towers is different from the others. Thus, the adsorption, the evaporator of the adsorption refrigerator that enabled the desorption process switching operation, and a heat storage tank filled with a substance having a higher freezing point than the refrigerant of the adsorption refrigerator as a heat storage material. An adsorption-type refrigeration system having a heat storage function, characterized in that the cooling medium is connected by a pipe through which a heat medium circulates, and a cold heat extraction section is provided in parallel in the middle of the circulation pipe via a three-way valve.
【請求項2】 吸着剤として活性炭、冷媒としてアルコ
ール、蓄熱材として水を用いたことを特徴とする請求項
1記載の蓄熱機能を有した吸着式冷凍システム。
2. The adsorption type refrigeration system having a heat storage function according to claim 1, wherein activated carbon is used as an adsorbent, alcohol is used as a refrigerant, and water is used as a heat storage material.
【請求項3】 吸着剤としてシリカゲル、冷媒として
水、蓄熱材としてクラスレートを用いたことを特徴とす
る請求項1記載の蓄熱機能を有した吸着式冷凍システ
ム。
3. The adsorptive refrigeration system having a heat storage function according to claim 1, wherein silica gel is used as an adsorbent, water is used as a refrigerant, and clathrate is used as a heat storage material.
【請求項4】 請求項1、2または3記載の蓄熱機能を
有した吸着式冷凍システムシステムを使用し、蒸発器よ
り出力される冷熱を熱媒体を介し蓄熱槽へ循環させるこ
とにより蓄熱材を凝固させて蓄熱をはかり、その後、三
方弁を切り換えて、蒸発器より出力される冷熱と蓄熱し
た冷熱とを、または、蓄熱した冷熱のみを、熱媒体を介
して冷熱取り出し部より、利用側へ取り出すことを特徴
とする運転方法。
A heat storage material is circulated by circulating cold heat output from an evaporator to a heat storage tank via a heat medium using the adsorption refrigeration system having a heat storage function according to claim 1, 2 or 3. The solidified heat is measured, and then the three-way valve is switched, and the cold heat output from the evaporator and the stored cold heat, or only the stored cold heat, is transferred to the use side from the cold heat extraction unit via the heat medium. Driving method characterized by taking out.
JP04357178A 1992-12-21 1992-12-21 Adsorption refrigeration system with heat storage function and its operation method Expired - Fee Related JP3138784B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04357178A JP3138784B2 (en) 1992-12-21 1992-12-21 Adsorption refrigeration system with heat storage function and its operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04357178A JP3138784B2 (en) 1992-12-21 1992-12-21 Adsorption refrigeration system with heat storage function and its operation method

Publications (2)

Publication Number Publication Date
JPH06193994A JPH06193994A (en) 1994-07-15
JP3138784B2 true JP3138784B2 (en) 2001-02-26

Family

ID=18452792

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3138784B2 (en)

Also Published As

Publication number Publication date
JPH06193994A (en) 1994-07-15

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