JPH0784965B2 - Solar cooling system - Google Patents

Solar cooling system

Info

Publication number
JPH0784965B2
JPH0784965B2 JP3361308A JP36130891A JPH0784965B2 JP H0784965 B2 JPH0784965 B2 JP H0784965B2 JP 3361308 A JP3361308 A JP 3361308A JP 36130891 A JP36130891 A JP 36130891A JP H0784965 B2 JPH0784965 B2 JP H0784965B2
Authority
JP
Japan
Prior art keywords
evaporator
condenser
heat
water
pressure
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 - Lifetime
Application number
JP3361308A
Other languages
Japanese (ja)
Other versions
JPH074775A (en
Inventor
誠之 渡辺
Original Assignee
誠之 渡辺
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 誠之 渡辺 filed Critical 誠之 渡辺
Priority to JP3361308A priority Critical patent/JPH0784965B2/en
Priority to PCT/JP1992/001732 priority patent/WO1993013367A1/en
Publication of JPH074775A publication Critical patent/JPH074775A/en
Publication of JPH0784965B2 publication Critical patent/JPH0784965B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/36Pervaporation; Membrane distillation; Liquid permeation
    • B01D61/362Pervaporation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/14Sorption machines, plants or systems, operating continuously, e.g. absorption type using osmosis

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は太陽熱利用の冷却装置
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling device utilizing solar heat.

【0002】[0002]

【従来の技術】従来は、例えば臭化リチウム水溶液等を
用いた吸収式冷却装置では、蒸発器、吸収器、水蒸気発
生器、太陽熱温水器および凝縮器等の構成機器を配管で
結んでいた。そして、配管の途中にポンプや膨張弁を設
けて、水蒸気吸収のための送液や低圧維持をしていた。
2. Description of the Related Art Conventionally, in an absorption type cooling device using, for example, an aqueous solution of lithium bromide, components such as an evaporator, an absorber, a steam generator, a solar water heater and a condenser are connected by pipes. Then, a pump or an expansion valve was provided in the middle of the pipe to supply liquid for absorbing water vapor and maintain low pressure.

【0003】[0003]

【発明が解決しようとする課題】前記従来装置は、数多
くの配管や機器のため大型の固定設備にならざるを得な
い。そのため、通常は冷水の供給源である間接冷却装置
としての用途に限られている。また、装置の動力源とし
て太陽熱以外に電力も必要とする。この発明はこのよう
な実情に鑑みてなされたもので、太陽熱以外には動力源
は不要で、しかも前記の機能をすべて一体化した、コン
パクトで移動可能な、直接冷却方式の太陽熱冷却装置を
提供することを目的としている。
The above-mentioned conventional device is inevitably a large-scale fixed facility due to many pipes and equipment. Therefore, it is usually limited to the use as an indirect cooling device which is a supply source of cold water. In addition to solar heat, electric power is also required as a power source for the device. The present invention has been made in view of the above circumstances, and provides a compact, movable, direct cooling type solar cooling device that does not require a power source other than solar heat, and that integrates all the functions described above. The purpose is to do.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
に、この発明は、低圧の蒸発器と常圧の蒸気吸収発生器
とを分離する手段、および前記の低圧の蒸発器と常圧の
凝縮器とを分離する手段として、半透膜の隔壁を有する
ことを特徴としている。
In order to solve the above problems, the present invention provides a means for separating a low pressure evaporator and a normal pressure vapor absorption generator, and a low pressure evaporator and a normal pressure separator. It is characterized by having a semipermeable membrane partition as means for separating the condenser.

【0005】[0005]

【作用】この発明の太陽熱冷却装置では、低圧の蒸発器
と、常圧の蒸気吸収発生器および凝縮器との間の隔壁で
ある半透膜は、前記各構成部の壁であると同時に、それ
らを連結する配管の役割も果たしている。
In the solar heat cooling device of the present invention, the semipermeable membrane, which is a partition wall between the low pressure evaporator and the atmospheric pressure vapor absorption generator and the condenser, is the wall of each of the above-mentioned components and at the same time, It also plays the role of piping that connects them.

【0006】低圧の蒸発器で熱を吸収して発生した水蒸
気は、隔壁である前記半透膜を通って、上部の蒸気吸収
発生器に貯留された溶質の水溶液に吸収され、この時、
蒸発器で奪った熱を凝縮顕熱として放出する。前記水蒸
気の凝縮によって生成した水は、凝縮顕熱と蒸気吸収発
生器に輻射される太陽熱によって蒸発させられて、再び
水蒸気となる。
Water vapor generated by absorbing heat in the low-pressure evaporator passes through the semipermeable membrane, which is a partition wall, and is absorbed by the aqueous solution of solute stored in the upper vapor absorption generator.
The heat taken by the evaporator is released as condensation sensible heat. The water generated by the condensation of the water vapor is evaporated by the sensible heat of condensation and the solar heat radiated to the vapor absorption generator, and becomes water vapor again.

【0007】この水蒸気は、同じ常圧の凝縮器上部の輻
射遮蔽板によって守られた放熱板に触れ、放熱板の外側
の外部空気によって冷却されて再度水となる。この水
は、凝縮器と蒸発器を隔てている前記半透膜を通って、
再び蒸発器に戻る。凝縮器内に少量の溶質を加えておく
ことにより、凝縮水によって凝縮器と蒸発器の差圧に等
しい浸透圧以下の水溶液濃度になると、水は蒸発器内に
移動する。
This water vapor comes into contact with the heat radiation plate protected by the radiation shielding plate above the condenser at the same atmospheric pressure, is cooled by the external air outside the heat radiation plate, and becomes water again. This water passes through the semipermeable membrane separating the condenser and the evaporator,
Return to the evaporator again. By adding a small amount of solute in the condenser, when the condensed water brings the aqueous solution concentration below the osmotic pressure equal to the differential pressure between the condenser and the evaporator, the water moves into the evaporator.

【0008】この結果、水溶液濃度は上昇し、上記浸透
圧以上の液濃度になると水の移動は停止する。このよう
にして凝縮器内には、常に希薄水溶液が存在することに
より半透膜の気密性が保たれ、蒸発器内は低圧に維持さ
れ続け、前記の熱の移動が繰り返され、蒸発器は連続的
に冷却される。
As a result, the concentration of the aqueous solution rises, and when the liquid concentration exceeds the osmotic pressure, the movement of water stops. In this way, since the dilute aqueous solution is always present in the condenser, the airtightness of the semipermeable membrane is maintained, the inside of the evaporator is kept at a low pressure, the heat transfer is repeated, and the evaporator is It is continuously cooled.

【0009】このように、低圧の構成部と常圧の構成部
との隔壁に半透膜を用いることにより、太陽熱冷却シス
テム全体を効果的に、しかもコンパクトに一体化するこ
とができる。
As described above, by using the semipermeable membrane for the partition wall of the low pressure component and the normal pressure component, the entire solar heat cooling system can be integrated effectively and compactly.

【0010】[0010]

【実施例】次に、添付図面とともに、この発明の実施例
を詳細に説明する。図中符号1は、太陽熱冷却装置であ
り、蒸発器2、蒸気吸収発生器3および凝縮器4を有し
ている。
Embodiments of the present invention will now be described in detail with reference to the accompanying drawings. Reference numeral 1 in the figure is a solar cooling device, which has an evaporator 2, a vapor absorption generator 3, and a condenser 4.

【0011】圧力が約10mmHgに維持された蒸発器
2には、蒸発冷却板21と高吸水性樹脂22を設け、高
吸水性樹脂22に含浸された水は低圧、低温の下で蒸発
して水蒸気となる。
The evaporator 2 whose pressure is maintained at about 10 mmHg is provided with an evaporative cooling plate 21 and a super absorbent resin 22. The water impregnated in the super absorbent resin 22 evaporates under low pressure and low temperature. Becomes water vapor.

【0012】この水蒸気は、低圧の蒸発器2と常圧の蒸
気吸収発生器3との隔壁である半透膜31を通って、蒸
気吸収発生器3に備えられた高吸水性樹脂32に含浸さ
れた飽和塩化カルシュウム水溶液に吸収される。蒸気吸
収発生器3は、更に、太陽熱吸収板33と半透膜支持床
34を備えている。塩化カルシュウム水溶液中の水は、
太陽熱吸収板33から吸収した熱と、蒸発器2からの水
蒸気の凝縮顕熱によって蒸発して、水蒸気となる。
This water vapor passes through a semipermeable membrane 31 which is a partition wall between the low pressure evaporator 2 and the normal pressure vapor absorption generator 3, and is impregnated into the super absorbent resin 32 provided in the vapor absorption generator 3. It is absorbed by the saturated aqueous solution of calcium chloride. The vapor absorption generator 3 further includes a solar heat absorption plate 33 and a semipermeable membrane supporting floor 34. The water in the calcium chloride solution is
The heat absorbed from the solar heat absorption plate 33 and the condensed sensible heat of the steam from the evaporator 2 evaporate to become steam.

【0013】常圧の部分として、この他に凝縮器4があ
る。凝縮器4には、蒸発器2との隔壁である半透膜4
1、高吸水性樹脂42、放熱板43、遮蔽板44および
半透膜支持床45が設けてある。高吸水性樹脂42に
は、低濃度の塩化カルシウム水溶液が含浸してある。前
記水蒸気は、放熱板43に接触して冷却され凝縮して水
となる。蒸発器2と太陽熱吸収板33にて吸収した熱
は、この時、大気に放出される。前記水は、高吸水性樹
脂42に吸収された後、半透膜41を通って蒸発器2に
戻る。
In addition to this, there is a condenser 4 as a part of the atmospheric pressure. The condenser 4 includes a semipermeable membrane 4 which is a partition wall with the evaporator 2.
1, a highly water-absorbent resin 42, a heat dissipation plate 43, a shielding plate 44, and a semipermeable membrane supporting floor 45 are provided. The super absorbent resin 42 is impregnated with a low concentration calcium chloride aqueous solution. The water vapor comes into contact with the heat dissipation plate 43, is cooled, and is condensed into water. The heat absorbed by the evaporator 2 and the solar heat absorption plate 33 is released to the atmosphere at this time. The water is absorbed by the super absorbent polymer 42 and then returns to the evaporator 2 through the semipermeable membrane 41.

【0014】半透膜31および41は、酢酸セルロース
等の膜で、それぞれ半透膜支持床34および45に支え
られて、低圧の蒸発器2と、常圧の蒸気吸収発生器3お
よび凝縮器4を仕切っている。
The semipermeable membranes 31 and 41 are membranes of cellulose acetate or the like, and are supported by the semipermeable membrane supporting beds 34 and 45, respectively, and the low pressure evaporator 2 and the atmospheric pressure vapor absorption generator 3 and the condenser are provided. Dividing 4

【0015】[0015]

【発明の効果】この発明は以上説明したように、低圧に
保たれた冷却機能をもつ蒸発器と、常圧の蒸気吸収発生
器および凝縮器とを半透膜で仕切ることにより、配管、
ポンプおよび膨張弁が不要でかつ、太陽熱のみを動力源
とするコンパクトな冷却装置を実現することができる。
As described above, the present invention divides the evaporator, which has a cooling function kept at a low pressure, the atmospheric pressure vapor absorption generator and the condenser, by a semipermeable membrane so that piping,
It is possible to realize a compact cooling device that does not require a pump and an expansion valve and that uses only solar heat as a power source.

【0016】このように、必要な構成要素を全て一体化
した構造のため、固定物だけではなく、常に移動する対
象物の冷却にも適している。よって、自動車、住宅、公
衆電話ボックスおよび携帯用クーラーボックス等の数多
くの用途がある。特に、夏季の自動車、住宅、公衆電話
ボックスの中のように、太陽熱そのものが高温化の原因
となる場合には、この発明を用いれば、それを積極的に
防止できる。
As described above, the structure in which all the necessary components are integrated is suitable for cooling not only fixed objects but also constantly moving objects. Thus, it has numerous applications such as automobiles, homes, payphone boxes and portable cooler boxes. In particular, when the heat of the sun itself causes the temperature to rise, such as in a car, a house, or a public telephone box in summer, the use of the present invention can prevent it.

【0017】以上に述べたように、小型のヒートポンプ
であるこの発明を利用すれば、非常に効果的な種々の局
所冷却装置が可能である。
As described above, the use of the present invention, which is a small heat pump, enables various very effective local cooling devices.

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

【図1】図はこの発明の一実施例である太陽熱冷却装置
の概略図である。
FIG. 1 is a schematic diagram of a solar cooling device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 太陽熱冷却装置 2 蒸発器 3 蒸気吸収発生器 4 凝縮器 1 Solar cooling device 2 Evaporator 3 Vapor absorption generator 4 Condenser

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 低圧の蒸発器と常圧の蒸気吸収発生器と
の分離隔壁として、又、同じく前記の低圧の蒸発器と常
圧の凝縮器との分離隔壁として、共に、溶質には不透過
性であるが、その溶媒蒸気および溶媒には透過性である
半透膜の仕切り壁を有することを特徴とする太陽熱冷却
装置。
1. A solute which is not separated from a solute, both as a partition wall between a low-pressure evaporator and a normal-pressure vapor absorption generator and also as a partition wall between the low-pressure evaporator and a normal-pressure condenser. A solar cooling device having a semipermeable membrane partition wall that is permeable but is permeable to the solvent vapor and solvent.
JP3361308A 1991-12-24 1991-12-24 Solar cooling system Expired - Lifetime JPH0784965B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP3361308A JPH0784965B2 (en) 1991-12-24 1991-12-24 Solar cooling system
PCT/JP1992/001732 WO1993013367A1 (en) 1991-12-24 1992-12-21 Solar cooling apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3361308A JPH0784965B2 (en) 1991-12-24 1991-12-24 Solar cooling system

Publications (2)

Publication Number Publication Date
JPH074775A JPH074775A (en) 1995-01-10
JPH0784965B2 true JPH0784965B2 (en) 1995-09-13

Family

ID=18473047

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3361308A Expired - Lifetime JPH0784965B2 (en) 1991-12-24 1991-12-24 Solar cooling system

Country Status (2)

Country Link
JP (1) JPH0784965B2 (en)
WO (1) WO1993013367A1 (en)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005028451B4 (en) 2005-06-17 2017-02-16 Evonik Degussa Gmbh Method of transporting heat
EP2087930A1 (en) 2008-02-05 2009-08-12 Evonik Degussa GmbH Method for the absorption of volatile material in a fluid absorption agent
EP2088389B1 (en) * 2008-02-05 2017-05-10 Evonik Degussa GmbH Absorption cooling machine
DE102009000543A1 (en) 2009-02-02 2010-08-12 Evonik Degussa Gmbh Process, absorption media and apparatus for absorbing CO2 from gas mixtures
DE102009047564A1 (en) 2009-12-07 2011-06-09 Evonik Degussa Gmbh Working medium for an absorption chiller
DE102011077377A1 (en) 2010-11-12 2012-05-16 Evonik Degussa Gmbh Process for the absorption of acid gases from gas mixtures
DE102012200907A1 (en) 2012-01-23 2013-07-25 Evonik Industries Ag Method and absorption medium for absorbing CO2 from a gas mixture
DE102012207509A1 (en) 2012-05-07 2013-11-07 Evonik Degussa Gmbh Method for absorbing CO2 from a gas mixture
DE102015212749A1 (en) 2015-07-08 2017-01-12 Evonik Degussa Gmbh Method for dehumidifying moist gas mixtures
EP3257568B1 (en) 2016-06-14 2019-09-18 Evonik Degussa GmbH Method for the removal of moisture from moist gas mixtures by use of ionic liquids
DE102016210484A1 (en) 2016-06-14 2017-12-14 Evonik Degussa Gmbh Method for dehumidifying moist gas mixtures
DE102016210483A1 (en) 2016-06-14 2017-12-14 Evonik Degussa Gmbh Process and absorbent for dehumidifying moist gas mixtures
DE102016210478A1 (en) 2016-06-14 2017-12-14 Evonik Degussa Gmbh Method for dehumidifying moist gas mixtures
DE102016210481B3 (en) 2016-06-14 2017-06-08 Evonik Degussa Gmbh Process for purifying an ionic liquid
EP3257843A1 (en) 2016-06-14 2017-12-20 Evonik Degussa GmbH Method of preparing a high purity imidazolium salt
FR3117199B1 (en) * 2020-12-04 2022-12-16 Alpinov X Evaporator for refrigeration installation delimiting two evaporation enclosures respectively at high pressure and low pressure and separated by a filtration screen

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5130648A (en) * 1974-09-07 1976-03-16 Kajima Corp HANTOMAKURYONOKYUSHUSHIKI REITOKI
DE3143534A1 (en) * 1981-11-03 1983-06-01 Joachim 2930 Varel Rieder Continuously running absorption refrigeration unit without a refrigerant distillation process
JPS60179103A (en) * 1984-02-27 1985-09-13 Hitachi Ltd Process and apparatus for concentrating aqueous solution and process and apparatus for recovering heat
JPS61107096A (en) * 1984-10-31 1986-05-24 Nippon Oil Co Ltd Method of transferring heat energy

Also Published As

Publication number Publication date
WO1993013367A1 (en) 1993-07-08
JPH074775A (en) 1995-01-10

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