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JPH0128868B2 - - Google Patents
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JPH0128868B2 - - Google Patents

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Publication number
JPH0128868B2
JPH0128868B2 JP58004496A JP449683A JPH0128868B2 JP H0128868 B2 JPH0128868 B2 JP H0128868B2 JP 58004496 A JP58004496 A JP 58004496A JP 449683 A JP449683 A JP 449683A JP H0128868 B2 JPH0128868 B2 JP H0128868B2
Authority
JP
Japan
Prior art keywords
tank
heat
lithium bromide
water
temperature
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
Application number
JP58004496A
Other languages
Japanese (ja)
Other versions
JPS59129361A (en
Inventor
Tadayasu Mitsumata
Minoru Tagashira
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP58004496A priority Critical patent/JPS59129361A/en
Publication of JPS59129361A publication Critical patent/JPS59129361A/en
Publication of JPH0128868B2 publication Critical patent/JPH0128868B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、比較的低い温度の利用分野、たとえ
ば冷凍、冷蔵あるいは冷房と、比較的高い温度の
利用分野、たとえば給湯、暖房あるいは産業用、
家庭用の各種熱利用分野に応用できるケミカルヒ
ートポンプの作動方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Fields of Industrial Application The present invention is applicable to fields of relatively low temperature applications, such as refrigeration, refrigeration, or air conditioning, and fields of relatively high temperature applications, such as hot water supply, space heating, or industrial applications.
This article relates to a method of operating a chemical heat pump that can be applied to various household heat utilization fields.

従来例の構成とその問題点 従来の冷蔵(凍)庫なかで最も広く実用化され
ているのは、フロンやアンモニアを冷媒とする電
動圧縮式冷蔵庫である。効率も高く、量産効果と
相まつてかなり安価となつてきた。ところが用途
によつては、作動音が大きく、また大気熱源を利
用した場合約50℃の吸収温度が限界であり、さら
に電力をかなり多く消費するなどの課題がある。
Conventional configurations and their problems The most widely used conventional refrigerators (freezers) are electric compression refrigerators that use fluorocarbons or ammonia as refrigerants. It has high efficiency, and combined with mass production, it has become quite inexpensive. However, depending on the application, there are problems such as the operation noise is loud, the absorption temperature is limited to about 50°C when using an atmospheric heat source, and it consumes a considerable amount of electricity.

一方吸収式ヒートポンプでは、冷房や暖房に広
く大型装置として実用化されるようになつた。こ
のシステムは、電動圧縮式ヒートポンプと異な
り、太陽熱、排熱あるいは燃焼熱を主なエネルギ
ー源とするため、エネルギー的には有利といえ
る。ところが、吸収材に臭化リチウム水溶液、熱
媒に水を用い、これらの液を循環させてシステム
を作動させるので、常に吸収材と熱媒は液体か気
体でなければならない。そのため臭化リチウムの
溶解度から、この溶液の濃度には限界があり、約
70%の濃度までである。そのほかにシステムの効
率を考えて、通常使用される濃度範囲は約50%以
下であり、これらの理由により、低温度差のヒー
トポンプとなる。すなわち、低温は5℃程度まで
高温は約60℃までとなり、これ以上の低温やこれ
以上の高温を得るためには二重効用とするなどの
特別な配慮が必要であり、高価なシステムとなる
欠点があつた。
On the other hand, absorption heat pumps have come into practical use as large-scale devices for a wide range of cooling and heating applications. Unlike electric compression heat pumps, this system uses solar heat, waste heat, or combustion heat as its main energy source, so it can be said to be advantageous in terms of energy. However, since the system uses an aqueous lithium bromide solution as the absorbent material and water as the heat medium, and these liquids are circulated to operate the system, the absorbent material and heat medium must always be either liquid or gas. Therefore, due to the solubility of lithium bromide, there is a limit to the concentration of this solution, approximately
Up to 70% concentration. In addition, considering the efficiency of the system, the concentration range typically used is approximately 50% or less, and for these reasons it is a heat pump with a low temperature difference. In other words, the low temperature is about 5℃ and the high temperature is about 60℃, and in order to obtain lower temperatures or higher temperatures, special considerations such as dual effect are required, resulting in an expensive system. There were flaws.

これに対し、吸収材が固体でもよい間欠吸収式
といえるケミカルヒートポンプが最近注目される
ようになつた。これはすでに示したように吸収材
が固体でもよく、選択範囲が広くなる利点のほか
に、蓄熱や蓄冷熱を長期間に亘つて用いられるこ
と、作動音が少ないこと、補助電力が不用あるい
は極めて少なくてよいことなどがあげられる。
In contrast, chemical heat pumps, which can be called intermittent absorption type heat pumps in which the absorbent material can be solid, have recently attracted attention. As already mentioned, the absorbing material can be solid, which has the advantage of widening the selection range, as well as being able to use heat storage or cold storage heat for a long period of time, producing little operating noise, and requiring no or very little auxiliary power. There are things that less is better.

冷媒として水を用いたケミカルヒートポンプは
従来より多く研究開発がなされて来た。特に吸収
材(以下吸収材とは吸着材も含んでいるものと解
釈する)の種類は多くのものが開発されており、
硫化ナトリウム(5←→0水塩)、ゼオライトなど
が代表的である。これらはいずれも長所短所を有
している。
Chemical heat pumps that use water as a refrigerant have been researched and developed more than ever before. In particular, many types of absorbent materials (hereinafter "absorbent materials" shall be interpreted as including adsorbents) have been developed.
Representative examples include sodium sulfide (5←→0 hydrate) and zeolite. All of these have advantages and disadvantages.

硫化ナトリウムは強アルカリ性を示し、金属、
ガラス等を腐食するため装置に高価な材料を用い
る必要性があり、また人体に対する毒性もあつて
平易な利用が困難である。ゼオライトの場合は水
蒸気の吸収力が大であり、冷房に利用した時に有
利に働く。反面、一度水蒸気を吸収したゼオライ
トを再生する場合、吸収力が大なるが故に高温の
熱を必要とし、例えば太陽エネルギー等で再生す
る場合は高価な高効率集熱器を利用するか、さも
なくば非常に低能率の再生を行なうことになる。
また、ゼオライトは吸収気体に選択性がないた
め、不純物ガスで容易に失活してしまう。その
他、ゼオライトはそれ自体価格が高いことや、多
孔質の固体であるため熱伝導性が悪くゼオライト
槽内部の伝熱を補なうための内部フインが不可欠
であること等により、やはり安価で簡便なシステ
ムは困難である。塩化カルシウムについては従来
2水素と1水素の間の吸収平衡を利用したケミカ
ルヒートポンプが報告されている。このシステム
の利点は多い。まず塩化カルシウムが一般に広く
用いられている乾燥剤であり、安価で容易に入手
できる。また毒性や腐食性がなく、取扱が簡便で
庫価な装着を必要としない。さらに水蒸気を選択
的に吸収し、少量の不純物ガスに対する配慮を必
要としない。
Sodium sulfide is strongly alkaline and is highly alkaline.
Since it corrodes glass and the like, it is necessary to use expensive materials for the device, and it is also toxic to the human body, making it difficult to use. Zeolite has a high ability to absorb water vapor, making it advantageous when used for air conditioning. On the other hand, when regenerating zeolite that has once absorbed water vapor, high-temperature heat is required due to its large absorption capacity.For example, when regenerating using solar energy, an expensive high-efficiency collector must be used, or else If this happens, regeneration will be performed with extremely low efficiency.
Moreover, since zeolite does not have selectivity in absorbing gas, it is easily deactivated by impurity gas. In addition, zeolite itself is expensive, and since it is a porous solid, it has poor thermal conductivity and requires internal fins to compensate for heat transfer inside the zeolite tank. system is difficult. Regarding calcium chloride, chemical heat pumps that utilize absorption equilibrium between dihydrogen and monohydrogen have been reported. The advantages of this system are many. First, calcium chloride is a commonly used desiccant, and is inexpensive and easily available. It is also non-toxic and corrosive, easy to handle, and does not require expensive installation. Furthermore, it selectively absorbs water vapor and does not require consideration for small amounts of impurity gas.

ところが、この系においても、同一蒸気圧での
水との温度差が約40℃であり、非常に低い低温
や、極めて高い高温は得られない。すなわち大気
温度が冬期に5℃とすると、理論的な最高温度が
45℃となり、これでは不充分な場合が多い。また
夏期の外気温度が30℃とすると、理論的には−10
℃まで得られることになるが、熱交換による温度
差が10〜15℃生ずるので、実際には0〜5℃の範
囲内となり、冷凍には不充分である。
However, even in this system, the temperature difference with water at the same vapor pressure is about 40°C, making it impossible to obtain extremely low temperatures or extremely high temperatures. In other words, if the atmospheric temperature is 5℃ in winter, the theoretical maximum temperature is
The temperature reaches 45℃, which is often insufficient. Also, if the outside temperature in summer is 30℃, theoretically -10
C., but since a temperature difference of 10 to 15.degree. C. occurs due to heat exchange, the temperature is actually within the range of 0 to 5.degree. C., which is insufficient for freezing.

発明の目的 本発明は、上記のケミカルヒートポンプの特徴
を生かしながら、冬期において70℃以上の高温給
湯を可能にするとか、あるいは夏期においては−
10℃という冷凍に充分な温度が得られるというよ
うに、高温度差のケミカルヒートポンプを得るこ
とを目的とする。
Purpose of the Invention The present invention makes it possible to supply high-temperature hot water of 70°C or higher in the winter, or -
The aim is to create a chemical heat pump with a high temperature difference, such as 10°C, which is sufficient for freezing.

発明の構成 本発明は一方の容器に熱媒である水、他方の容
器に吸収材である常温で固定の臭化リチウムを入
れ、両容器間をストツプバルブで連結し、臭化リ
チウムの完全乾燥時は無水塩、完全吸収時は1水
塩として、水の入つている容器を凝縮器あるいは
蒸発器として、臭化リチウムの入つている容器を
再生器あるいは吸収器として交互に動作させるも
のである。
Structure of the Invention The present invention involves putting water as a heating medium in one container and lithium bromide, which is fixed at room temperature as an absorbent, in the other container, and connecting both containers with a stop valve. is used as an anhydrous salt, and when completely absorbed as a monohydrate salt, the container containing water is operated as a condenser or evaporator, and the container containing lithium bromide is operated alternately as a regenerator or absorber.

実施例の説明 第1図に従来例、本発明ともに共通なケミカル
ヒートポンプの基本的な装置を示してある。装置
はA,B2つの槽をストツプバルブで連結したも
のであり、A槽には水2、B槽には吸収材3が入
つている。A,B両槽には内部に熱交換器4が装
着されていて、熱エネルギーを容易に入出力でき
る。また装置は脱気後気密が保たれ内部には水蒸
気以外の気体は存在しない。吸収・脱着の際に臭
化リチウムに含まれる水の量の最大値は、最初A
槽に入れた水の量とB槽内の臭化リチウムが最初
に含んでいた水の量との和で決定される。
DESCRIPTION OF EMBODIMENTS FIG. 1 shows a basic device of a chemical heat pump that is common to both the conventional example and the present invention. The device consists of two tanks A and B connected by a stop valve, with tank A containing 2 water and tank B containing 3 absorbents. A heat exchanger 4 is installed inside both tanks A and B, so that thermal energy can be easily input and output. Furthermore, the device remains airtight after degassing, and there is no gas other than water vapor inside. The maximum amount of water contained in lithium bromide during absorption and desorption is initially A.
It is determined by the sum of the amount of water put into the tank and the amount of water initially contained in lithium bromide in tank B.

装置の作動方法はいわゆるバツチ式であり、蓄
熱行程と放熱行程の2行程で1サイクルを成す。
蓄熱行程とは、熱源より熱を得てB槽が加熱さ
れ、B槽内より熱水蒸気が出てA槽で凝縮しA槽
より熱を出力する行程であり、このときA槽は凝
縮器、B槽は再生器として働く。この行程の後で
はB槽内の吸収材は高エネルギー状態にあり、こ
のときバルブを閉じればエネルギーは保存され
る。放熱行程とは再生後の吸収剤がA槽に貯えら
れた水を水蒸気として吸収し、A槽より蒸発潜熱
をうばう行程である。このときA槽は蒸発器、B
槽は吸収器として働く。放熱行程は冷房用と暖房
用の2通りの使い方がある。冷房用として使う場
合はB槽を室温付近で冷却するとA槽は室温より
も低い温度で蒸気を出すので冷房が行なえる。暖
房として使う場合はA槽を室温付近で加熱すると
B槽では室温よりも高い温度で吸収熱を出すので
暖房効果が得られる。
The operating method of the device is a so-called batch type, and one cycle consists of two steps: a heat storage step and a heat radiation step.
The heat storage process is a process in which tank B is heated by obtaining heat from a heat source, hot steam comes out from tank B, is condensed in tank A, and heat is output from tank A. At this time, tank A is a condenser, Tank B acts as a regenerator. After this stroke, the absorbent material in tank B is in a high energy state, and if the valve is closed at this time, the energy is conserved. The heat dissipation process is a process in which the regenerated absorbent absorbs the water stored in tank A as water vapor and takes away the latent heat of vaporization from tank A. At this time, tank A is the evaporator, tank B
The tank acts as an absorber. The heat dissipation process can be used in two ways: for cooling and for heating. When used for air conditioning, if tank B is cooled to around room temperature, tank A will emit steam at a lower temperature than room temperature, so cooling can be performed. When used for heating, if tank A is heated near room temperature, tank B will emit absorbed heat at a higher temperature than room temperature, resulting in a heating effect.

以上のようなケミカルヒートポンプの吸収材と
して臭化リチウム(固体状)、熱媒として水を用
いると、簡単な装置で容易に冷凍庫用冷熱源、あ
るいは70℃以上という比較的高温の給湯用などの
熱源が得られることがわかつた。
By using lithium bromide (solid) as the absorbing material and water as the heating medium in the chemical heat pump described above, it can be easily used as a cold source for freezers, or for hot water supply at relatively high temperatures of 70°C or higher, with a simple device. It turned out that a heat source could be obtained.

第1図に示す構成においてケミカルヒートポン
プを形成した。すなわちA槽には水180g、B槽
には無水臭化リチウム結晶870gを入れた。そし
て全体を排気ポンプで真空とし、作動テストを行
なつた。
A chemical heat pump was formed with the configuration shown in FIG. That is, 180 g of water was placed in tank A, and 870 g of anhydrous lithium bromide crystal was placed in tank B. Then, the entire structure was evacuated using an exhaust pump and an operational test was performed.

まず、B槽の温度を30℃におさえ、A槽の温度
がどこまで低下するかを求めた。その結果を第2
図の曲線Cに示す。すなわち、約8時間に亘り−
20℃の低温を得ることができた。当然水は凍結
し、氷から直接水蒸気に昇華している。これに対
し、従来例として、臭化リチウムの代りに塩化リ
チウム無水塩を用いる以外は全く上記ヒートポン
プと同じヒートポンプを組立て、そのときの蒸発
器温度変化を第2図の曲線C′に示す。この両者よ
り、本発明による臭化リチウム一水系では、より
低い温度が、しかも長時間に亘つて維持できた。
First, we kept the temperature of tank B at 30°C and determined how far the temperature of tank A would drop. The second result is
This is shown in curve C in the figure. That is, for about 8 hours -
We were able to obtain temperatures as low as 20℃. Naturally, water freezes and sublimates directly from ice to water vapor. On the other hand, as a conventional example, a heat pump that is completely the same as the above heat pump except that lithium chloride anhydrous salt is used instead of lithium bromide is assembled, and the evaporator temperature change at that time is shown by curve C' in FIG. From both of these, the lithium bromide monoaqueous system according to the present invention was able to maintain a lower temperature for a longer period of time.

また、A槽の蒸発温度を10℃と一定とし、B槽
の吸収温度の変化を求めた。本発明による固体状
臭化リチウムと―水系と従来例としての固体状塩
化カルシウム―水系での結晶を、第2図の曲線D
およびD′に示す。この曲線から、本発明による
吸収温度は約80℃となり、従来品よりも約30℃だ
け高温とすることができた。これにより、約80℃
近くの高温給湯が可能となり、蓄熱槽の小型化、
床暖房用への適応なども可能となるなどの利点が
多い。
In addition, the evaporation temperature of tank A was kept constant at 10°C, and the change in absorption temperature of tank B was determined. Curve D in FIG.
and shown in D′. From this curve, the absorption temperature according to the present invention was about 80°C, which was about 30°C higher than that of the conventional product. This results in approximately 80℃
It is now possible to supply high-temperature hot water nearby, making the heat storage tank more compact,
It has many advantages, such as being able to be adapted to underfloor heating.

発明の効果 以上のように、比較的低い冷熱源、あるいは比
較的高い高温熱源を必要とする場合には吸収材と
して固体状臭化リチウム、熱媒として水を用い、
臭化リチウムの作動範囲が無水塩と1水塩の間で
用いることにより、実用的な効果が得られる。
Effects of the Invention As described above, when a relatively low cold heat source or a relatively high high temperature heat source is required, solid lithium bromide is used as an absorbent and water is used as a heat medium.
Practical effects can be obtained by using lithium bromide in the operating range between anhydrous and monohydrate salts.

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

第1図は本発明の一実施例であるケミカルヒー
トポンプの基本構成を示す模式図、第2図は固体
状臭化リチウム一水系のケミカルヒートポンプの
性能を示す図である。 1…ストツプバルブ、2…水、3…吸収材、4
…熱交換器。
FIG. 1 is a schematic diagram showing the basic configuration of a chemical heat pump that is an embodiment of the present invention, and FIG. 2 is a diagram showing the performance of a solid lithium bromide monoaqueous chemical heat pump. 1...stop valve, 2...water, 3...absorbent material, 4
…Heat exchanger.

Claims (1)

【特許請求の範囲】[Claims] 1 熱媒として水、吸収材として常温で固体の臭
化リチウムを構成要素とし、水を吸収した臭化リ
チウムを脱水して再生するために、臭化リチウム
が無水塩になるまで加熱するとともに、再生した
無水臭化リチウムが水を吸収してケミカルヒート
ポンプを作動させるときは、臭化リチウムが1水
塩になつた時点で停止させ、再度再生させること
を特徴とするケミカルヒートポンプの作動方法。
1. Water is used as a heating medium, and lithium bromide, which is solid at room temperature, is used as an absorbing material. In order to dehydrate and regenerate the lithium bromide that has absorbed water, the lithium bromide is heated until it becomes an anhydrous salt. A method for operating a chemical heat pump, characterized in that when the regenerated anhydrous lithium bromide absorbs water to operate the chemical heat pump, the process is stopped when the lithium bromide becomes monohydrate, and the process is regenerated again.
JP58004496A 1983-01-14 1983-01-14 Chemical heat pump Granted JPS59129361A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58004496A JPS59129361A (en) 1983-01-14 1983-01-14 Chemical heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58004496A JPS59129361A (en) 1983-01-14 1983-01-14 Chemical heat pump

Publications (2)

Publication Number Publication Date
JPS59129361A JPS59129361A (en) 1984-07-25
JPH0128868B2 true JPH0128868B2 (en) 1989-06-06

Family

ID=11585675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58004496A Granted JPS59129361A (en) 1983-01-14 1983-01-14 Chemical heat pump

Country Status (1)

Country Link
JP (1) JPS59129361A (en)

Also Published As

Publication number Publication date
JPS59129361A (en) 1984-07-25

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