JPH1114183A - Freezer device - Google Patents

Freezer device

Info

Publication number
JPH1114183A
JPH1114183A JP9161618A JP16161897A JPH1114183A JP H1114183 A JPH1114183 A JP H1114183A JP 9161618 A JP9161618 A JP 9161618A JP 16161897 A JP16161897 A JP 16161897A JP H1114183 A JPH1114183 A JP H1114183A
Authority
JP
Japan
Prior art keywords
core
refrigerant
auxiliary
adsorption
heat exchanger
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
Application number
JP9161618A
Other languages
Japanese (ja)
Other versions
JP3740794B2 (en
Inventor
Seiji Inoue
誠司 井上
Yoshiaki Tanaka
攻明 田中
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.)
Denso Corp
Original Assignee
Denso Corp
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 Denso Corp filed Critical Denso Corp
Priority to JP16161897A priority Critical patent/JP3740794B2/en
Publication of JPH1114183A publication Critical patent/JPH1114183A/en
Application granted granted Critical
Publication of JP3740794B2 publication Critical patent/JP3740794B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • 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
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • 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
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable a gas liquid separation between an evaporating core and an adsorption core to be carried out in a superior manner for a long period of time. SOLUTION: This freezer device is constructed such that refrigerant vapour evaporated at a main evaporating condenser core 14 contacted with liquid refrigerant L is adsorbed with an adsorption core 12 arranged under non- contacted state, heat exchanging fluid cooled by the main evaporating condenser core 14 is circulated in an indoor heat exchanger 26 to cool an interior side of a room. In this case, an auxiliary evaporating core 13 is arranged between the main evaporating condenser core 14 and the adsorption core 12 under a non-contacted state with the liquid refrigerant L. Accordingly, refrigerant in liquid droplet form adheres to the auxiliary evaporating condenser core 13 and is evaporated at this auxiliary evaporating condenser core 13. In addition, heat exchanging fluid absorbing heat at the indoor heat exchanger 26 is flowed at first to the auxiliary evaporating condenser core 13, thereafter the fluid is flowed at the main evaporating condenser core 14, resulting in that it is possible to perform a superior evaporating of refrigerant at the auxiliary evaporating condenser core 13.

Description

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

【０００１】[0001]

【発明の属する技術分野】本発明は、吸着剤あるいは吸
収液により水等の冷媒を吸着あるいは吸収することを利
用した冷凍装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigerating apparatus utilizing the adsorption or absorption of a refrigerant such as water by an adsorbent or an absorbent.

【０００２】[0002]

【従来の技術】例えば冷蔵庫や家庭用エアコン、カーエ
アコン等に用いられる冷凍装置として、水などを冷媒と
した吸着式冷凍装置が知られている。これは、シリカゲ
ル、ゼオライト等の吸着剤が、冷却状態にあって気冷媒
（水蒸気）を高能力で吸着し、加熱状態にあっては吸着
した気冷媒を脱着して吸着能力が再生されることを利用
したものである。2. Description of the Related Art As a refrigerating device used for a refrigerator, a home air conditioner, a car air conditioner, etc., an adsorption refrigerating device using water as a refrigerant is known. This means that adsorbents such as silica gel and zeolite adsorb gas refrigerant (water vapor) with high capacity in the cooling state, and desorb the adsorbed gas refrigerant in the heating state to regenerate the adsorption capacity. It is a thing using.

【０００３】そして、この種の冷凍装置として、特開平
９−２６２２４号公報には、図７に示すような吸着式冷
凍装置１が提案されている。この装置１は、１つの密閉
空間を形成する密閉回路１１を備え、この密閉回路１１
内には、吸着コア１２、蒸発コア１４１、凝縮コア１４
２が収容されている。吸着コア１２は、周知の熱交換器
形状をなす熱交換部（図示しない）の周囲に多数の吸着
剤Ｓを保持させたものからなり、上記熱交換部の入口部
１２ａから出口部１２ｂにかけて熱交換流体（加熱流
体、冷却流体）が流れる。[0003] As this type of refrigeration apparatus, Japanese Patent Application Laid-Open No. 9-226224 proposes an adsorption refrigeration apparatus 1 as shown in FIG. The device 1 includes a closed circuit 11 forming one closed space.
Inside, the adsorption core 12, the evaporation core 141, the condensation core 14
2 are accommodated. The adsorption core 12 is formed by holding a large number of adsorbents S around a heat exchange section (not shown) having a well-known heat exchanger shape, and heats the heat exchange section from the inlet 12a to the outlet 12b. The exchange fluid (heating fluid, cooling fluid) flows.

【０００４】また、蒸発コア１４１は液冷媒Ｌと接触し
て設けられ、凝縮コア１４２は液冷媒Ｌと非接触な状態
で設けられる。これらの蒸発コア１４１、凝縮コア１４
２は周知の熱交換器形状をなし、入口部１４１ａ、１４
２ａから出口部１４１ｂ、１４２ｂにかけて熱交換流体
が流れる。なお、密閉回路１１は、吸着コア１２を収容
する吸着コア収容部１１１と、蒸発コア１４１を収容す
る蒸発コア収容部１１２と、凝縮コア１４２を収容する
凝縮コア収容部１１３とを有している。そして、密閉回
路１１は、吸着コア収容部１１１と蒸発コア収容部１１
２との間、吸着コア収容部１１１と凝縮コア収容部１１
３との間、および、蒸発コア収容部１１２と凝縮コア収
容部１１３との間を、冷媒蒸気通路１１４、１１５、お
よび、液冷媒通路１１６にて連通した形態である。[0004] Further, the evaporation core 141 is provided in contact with the liquid refrigerant L, and the condensing core 142 is provided in a non-contact state with the liquid refrigerant L. These evaporating core 141 and condensing core 14
2 has a well-known heat exchanger shape, and has inlet portions 141a, 14a.
The heat exchange fluid flows from 2a to outlets 141b and 142b. In addition, the closed circuit 11 includes an adsorbing core accommodating section 111 that accommodates the adsorbing core 12, an evaporating core accommodating section 112 that accommodates the evaporating core 141, and a condensing core accommodating section 113 that accommodates the condensing core 142. . The closed circuit 11 includes the suction core housing 111 and the evaporation core housing 11.
2, the adsorption core accommodating section 111 and the condensing core accommodating section 11
3 and between the evaporating core accommodating portion 112 and the condensing core accommodating portion 113 through refrigerant vapor passages 114 and 115 and a liquid refrigerant passage 116.

【０００５】また、吸着コア収容部１１１と冷媒蒸気通
路１１４、１１５との連結部である、吸着コア収容部１
１１の冷媒出入口１１１ａ、１１１ｂには、これら冷媒
出入口１１１ａ、１１１ｂを開閉するドア手段１１１
ｃ、１１１ｄが設けてある。また、液冷媒通路１１６に
は、凝縮コア収容部１１３内の液冷媒Ｌから蒸発コア収
容部１１２内の液冷媒Ｌへ液冷媒を送液するポンプ手段
１１７が設けてある。The adsorbing core housing 1 is a connecting portion between the adsorbing core housing 111 and the refrigerant vapor passages 114 and 115.
11 are provided with door means 111 for opening and closing the refrigerant ports 111a, 111b.
c and 111d are provided. Further, the liquid refrigerant passage 116 is provided with a pump means 117 for feeding the liquid refrigerant from the liquid refrigerant L in the condensing core housing 113 to the liquid refrigerant L in the evaporating core housing 112.

【０００６】そして、ドア手段１１１ｃにて冷媒出入口
１１１ａを開口し、ドア手段１１１ｄにて冷媒出入口１
１１ｂを閉塞して、吸着コア３の上記熱交換部に冷却流
体を循環させると、吸着剤Ｓが冷却されて冷媒蒸気を吸
着するとともに、蒸発コア１４１と接触する液冷媒Ｌが
蒸発する。これにより、蒸発コア１４１を循環する熱交
換流体が冷却され、この冷却された熱交換流体を室内熱
交換器に循環させることにより、室内冷房を行なってい
る。[0006] The refrigerant port 111a is opened by the door means 111c, and the refrigerant port 1a is opened by the door means 111d.
When the cooling fluid is circulated through the heat exchange section of the adsorption core 3 by closing the 11b, the adsorbent S is cooled and adsorbs the refrigerant vapor, and the liquid refrigerant L in contact with the evaporation core 141 evaporates. As a result, the heat exchange fluid circulating in the evaporation core 141 is cooled, and the cooled heat exchange fluid is circulated through the indoor heat exchanger to perform indoor cooling.

【０００７】ところで、冷媒蒸気が吸着されることによ
り吸着コア収容部１１１から蒸発コア収容部１１２にか
けての密閉回路１１内が低圧（例えば１０ｔｏｒｒ程
度）となり、液冷媒Ｌが沸騰するような状態となる。し
かも、液冷媒Ｌの蒸発は、液冷媒Ｌの表面だけでなく内
部においても活発に行なわれる。このため、液冷媒Ｌ内
部に生じた気泡が液冷媒Ｌの表面において弾けることに
より、例えば１００〜２００μ程度の粒径の微細な液滴
が飛び出す。このような液滴状の冷媒が吸着コア１２の
吸着剤Ｓや熱交換部に付着すると、吸着剤Ｓの吸着能力
や熱交換部の熱交換能力が低下する恐れがある。When the refrigerant vapor is adsorbed, the pressure in the closed circuit 11 from the adsorbing core accommodating section 111 to the evaporating core accommodating section 112 becomes low (for example, about 10 torr), and the liquid refrigerant L is brought into a state of boiling. . Moreover, the evaporation of the liquid refrigerant L is actively performed not only on the surface of the liquid refrigerant L but also inside the liquid refrigerant L. For this reason, bubbles generated inside the liquid refrigerant L pop on the surface of the liquid refrigerant L, so that fine droplets having a particle size of, for example, about 100 to 200 μ fly out. If such a droplet-shaped refrigerant adheres to the adsorbent S and the heat exchange unit of the adsorption core 12, there is a possibility that the adsorption capacity of the adsorbent S and the heat exchange capacity of the heat exchange unit are reduced.

【０００８】これに対して上記公報に記載の従来技術で
は、密閉回路１１の蒸発コア収容部１１２内を仕切るよ
うに、液滴通過阻止部材３１を設けている。この液滴通
過阻止部材３１は、金網（メッシュ）の表面に撥水処理
を施して構成され、この場合、例えば２００メッシュの
金網に、４フッ化エチレン樹脂からなる撥水剤を塗布し
て構成されている。これにより、蒸発コア１４１と接触
する液冷媒Ｌから蒸発した冷媒蒸気は、液滴通過阻止部
材３１の網の目を通って吸着コア１２側へ流入すること
が可能となるが、液滴状の冷媒は、液滴通過阻止部材３
１により跳ね返されて通過が阻止される。On the other hand, in the prior art described in the above-mentioned publication, the droplet passage preventing member 31 is provided so as to partition the inside of the evaporation core accommodating portion 112 of the closed circuit 11. The droplet passage preventing member 31 is formed by applying a water-repellent treatment to the surface of a wire mesh (mesh). In this case, for example, a water-repellent agent made of tetrafluoroethylene resin is applied to a wire mesh of 200 mesh. Have been. This allows the refrigerant vapor evaporated from the liquid refrigerant L in contact with the evaporating core 141 to flow toward the adsorption core 12 through the mesh of the droplet passage preventing member 31, but the droplet-shaped refrigerant The coolant is supplied to the droplet passage preventing member 3.
It is bounced off by 1 to prevent passage.

【０００９】[0009]

【発明が解決しようとする課題】ところが、撥水処理は
時間が経過すると効果が劣る恐れがあり、蒸発コア１４
１と吸着コア１２との間の気液分離を長期にわたって良
好に行なえなくなる恐れがあった。本発明は上記点に鑑
みてなされたもので、蒸発コアと吸着コアとの間の気液
分離を長期にわたって良好に行なうことが可能な冷凍装
置を提供することを目的とする。However, the effect of the water-repellent treatment may be inferior over time.
There is a possibility that gas-liquid separation between the core 1 and the adsorption core 12 cannot be performed well over a long period of time. The present invention has been made in view of the above, and an object of the present invention is to provide a refrigeration apparatus capable of performing gas-liquid separation between an evaporation core and an adsorption core satisfactorily over a long period of time.

【００１０】[0010]

【課題を解決するための手段】上記目的を達成するため
に、請求項１および２に記載の発明では、液冷媒（Ｌ）
と接触して配される主蒸発コア（１４、１４１）にて蒸
発させた冷媒蒸気を、液冷媒（Ｌ）と非接触状態で配さ
れる吸着コア（１２）にて吸着し、主蒸発コア（１４、
１４１）にて冷却される熱交換流体を熱交換器（２６）
に流すことにより、被冷却部を冷却する冷凍装置におい
て、主蒸発コア（１４、１４１）と吸着コア（１２）と
の間に、冷媒を蒸発させる補助蒸発コア（１３、１３
０）を、液冷媒（Ｌ）と非接触状態で設け、熱交換器
（２６）において吸熱した熱交換流体を、先に補助蒸発
コア（１３、１３０）に流し、その後、主蒸発コア（１
４、１４１）に流すことを特徴としている。In order to achieve the above object, according to the first and second aspects of the present invention, a liquid refrigerant (L) is provided.
The refrigerant vapor evaporated in the main evaporation core (14, 141) arranged in contact with the liquid refrigerant (L) is adsorbed by the adsorption core (12) arranged in a non-contact state with the liquid refrigerant (L), and (14,
The heat exchange fluid cooled in 141) is transferred to a heat exchanger (26).
In the refrigerating apparatus that cools the part to be cooled, the auxiliary evaporation cores (13, 13) that evaporate the refrigerant are provided between the main evaporation cores (14, 141) and the adsorption cores (12).
0) is provided in a non-contact state with the liquid refrigerant (L), the heat exchange fluid absorbed in the heat exchanger (26) is first passed through the auxiliary evaporation cores (13, 130), and then the main evaporation core (1) is discharged.
4, 141).

【００１１】従って、主蒸発コア（１４、１４１）と接
触する液冷媒（Ｌ）から蒸発した冷媒蒸気は、補助蒸発
コア（１３、１３０）を通過して吸着コア（１２）側へ
流入することが可能となるが、液滴状の冷媒は、補助蒸
発コア（１３、１３０）に付着し、この補助蒸発コア
（１３、１３０）において蒸発される。よって、液滴状
の冷媒が吸着コア（１２）側へ移動することを抑制で
き、吸着コア（１２）の吸着能力を良好に維持できる。Therefore, the refrigerant vapor evaporated from the liquid refrigerant (L) in contact with the main evaporation cores (14, 141) passes through the auxiliary evaporation cores (13, 130) and flows into the adsorption core (12). However, the droplet-shaped refrigerant adheres to the auxiliary evaporation core (13, 130) and is evaporated in the auxiliary evaporation core (13, 130). Therefore, it is possible to suppress the droplet-shaped refrigerant from moving to the adsorption core (12) side, and it is possible to maintain the adsorption capability of the adsorption core (12) in a good condition.

【００１２】しかも、熱交換器（２６）において吸熱し
た比較的高温な熱交換流体を、先に補助蒸発コア（１
３、１３０）に流すので、この補助蒸発コア（１３、１
３０）における冷媒の蒸発を良好に行なうことができ
る。また、液滴状の冷媒を蒸発させるときの蒸発潜熱に
より、熱交換器（２６）に循環させる熱交換流体を冷却
できるので、冷熱のロスを低減できる。Further, the relatively high-temperature heat exchange fluid that has absorbed heat in the heat exchanger (26) is first supplied to the auxiliary evaporation core (1).
3, 130), so that the auxiliary evaporation cores (13, 1)
The refrigerant can be satisfactorily evaporated in 30). Further, since the heat exchange fluid circulated through the heat exchanger (26) can be cooled by the latent heat of vaporization when the droplet-shaped refrigerant is evaporated, the loss of cold heat can be reduced.

【００１３】そして、補助蒸発コア（１３、１３０）
は、上記した撥水処理のような、時間の経過により効果
が劣るようなものではないため、主蒸発コア（１４、１
４１）と吸着コア（１２）との間の気液分離を長期にわ
たって良好に行なうことができる。また、請求項２に記
載の発明では、主蒸発コア（１４１）と吸着コア（１
２）との間の冷媒蒸気通路（１１２）の全面を横断する
ように、補助蒸発コア（１３、１３０）を設けているの
で、液滴状の冷媒が吸着コア（１２）側へ移動すること
をより確実に抑制できる。And an auxiliary evaporation core (13, 130).
Is not such that the effect is not inferior with the passage of time as in the water-repellent treatment described above.
Gas-liquid separation between 41) and the adsorption core (12) can be favorably performed over a long period of time. Further, in the invention described in claim 2, the main evaporation core (141) and the adsorption core (1)
Since the auxiliary evaporation cores (13, 130) are provided so as to traverse the entire surface of the refrigerant vapor passage (112) between 2), the droplet-shaped refrigerant moves to the adsorption core (12) side. Can be suppressed more reliably.

【００１４】また、請求項３および４に記載の発明で
は、上記した吸着コア（１２）の替わりに吸収コア
（５）にて冷媒蒸気を吸収する冷凍装置に、上記請求項
１および２に記載の補助蒸発コア（１３、１３０）を適
用している。これによれば、液滴状の冷媒が吸収コア
（５）側へ移動することを抑制でき、吸収コア（５）の
吸収能力を良好に維持できる。According to the third and fourth aspects of the present invention, there is provided a refrigeration apparatus that absorbs refrigerant vapor with an absorption core (5) instead of the adsorption core (12). Of the auxiliary evaporation cores (13, 130). According to this, it is possible to suppress the droplet-like refrigerant from moving to the absorption core (5) side, and it is possible to maintain the absorption capacity of the absorption core (5) satisfactorily.

【００１５】また、補助蒸発コア（１３、１３０）は、
上記した撥水処理のような、時間の経過により効果が劣
るようなものではないため、主蒸発コア（１４、１４
１）と吸収コア（５）との間の気液分離を長期にわたっ
て良好に行なうことができる。また、請求項４に記載の
発明では、主蒸発コア（１４１）と吸収コア（５）との
間の冷媒蒸気通路（１１２）の全面を横断するように、
補助蒸発コア（１３０）を設けているので、液滴状の冷
媒が吸収コア（５）側へ移動することをより確実に抑制
できる。The auxiliary evaporation cores (13, 130) are
Since the effect is not inferior over time as in the above-described water-repellent treatment, the main evaporation cores (14, 14)
The gas-liquid separation between 1) and the absorbent core (5) can be favorably performed over a long period of time. According to the fourth aspect of the present invention, the refrigerant vapor passage (112) between the main evaporation core (141) and the absorption core (5) is traversed over the entire surface.
Since the auxiliary evaporation core (130) is provided, it is possible to more reliably prevent the droplet-shaped refrigerant from moving toward the absorption core (5).

【００１６】[0016]

【発明の実施の形態】以下に、本発明の実施形態につい
て図に基づいて説明する。 （第１の実施形態）まず、本発明の第１の実施形態は、
図１に示すような吸着式冷凍装置１に本発明を適用した
ものである。この吸着式冷凍装置１は、１つの密閉空間
を形成する密閉容器（密閉回路）１１の内部に、吸着コ
ア１２、補助蒸発凝縮コア（補助蒸発コア）１３、およ
び、主蒸発凝縮コア（主蒸発コア）１４を、上方から順
に収容してなるユニット１０を有している。なお、密閉
容器１１は、吸着コア１２を収容する吸着コア収容部１
１１と、上記両蒸発凝縮コア１３、１４を収容する蒸発
凝縮コア収容部１１２と、これら収容部１１１、１１２
の間に位置する冷媒蒸気通路１１０とを有している。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. (First Embodiment) First, a first embodiment of the present invention is as follows.
The present invention is applied to an adsorption refrigeration apparatus 1 as shown in FIG. The adsorption-type refrigeration apparatus 1 includes an adsorption core 12, an auxiliary evaporation / condensation core (auxiliary evaporation core) 13, and a main evaporation / condensation core (main evaporation) inside a closed vessel (sealed circuit) 11 forming one closed space. The core 10 has a unit 10 that is housed in order from above. In addition, the closed container 11 includes the suction core housing unit 1 that houses the suction core 12.
11, an evaporating and condensing core accommodating portion 112 for accommodating the evaporating and condensing cores 13 and 14, and accommodating portions 111 and 112.
And a refrigerant vapor passage 110 located therebetween.

【００１７】密閉容器１１の蒸発凝縮コア収容部１１２
の内部には、所定量の液冷媒Ｌが封入されている。そし
て、主蒸発凝縮コア１４の全体あるいは一部が液冷媒Ｌ
と接触して設けられ、補助蒸発凝縮コア１３および吸着
コア１２の全体が液冷媒Ｌと非接触状態で（つまり、液
冷媒Ｌの表面よりも上方に）設けられている。そして、
冷媒として、例えば水、アルコール、フロン等が用いら
れている。The evaporating and condensing core accommodating portion 112 of the closed vessel 11
Is filled with a predetermined amount of liquid refrigerant L. The entire or a part of the main evaporative condensing core 14 is a liquid refrigerant L.
The auxiliary evaporation condensing core 13 and the adsorption core 12 are entirely provided in a non-contact state with the liquid refrigerant L (that is, above the surface of the liquid refrigerant L). And
As the refrigerant, for example, water, alcohol, chlorofluorocarbon or the like is used.

【００１８】吸着コア１２は、周知の熱交換器形状を有
する熱交換器１２１に、多数の吸着剤Ｓを保持させたも
のである。熱交換器１２１は、一対のタンク１２１ａ、
１２１ｂの間に、複数の流体配管１２１ｃと、複数の蛇
行状伝熱フィン１２１ｄとを交互に並列配置してなる。
なお、一対のタンク１２１ａ、１２１ｂの一方１２１ａ
側に、熱交換流体が流入する入口部１２ａを有し、他方
１２１ｂ側に、熱交換流体が流出する出口部１２ｂを有
している。そして、入口部１２ａからの熱交換流体は、
タンク１２１ａ→複数の流体配管１２１ｃ→タンク１２
１ｂの順に流れて、出口部１２ｂから流出される。ここ
で、熱交換流体としては、水にエチレングリコール等を
混入させたいわゆる不凍液を用いている。The adsorbing core 12 has a large number of adsorbents S held in a heat exchanger 121 having a well-known heat exchanger shape. The heat exchanger 121 includes a pair of tanks 121a,
A plurality of fluid pipes 121c and a plurality of meandering heat transfer fins 121d are alternately arranged in parallel between 121b.
One of the pair of tanks 121a and 121b 121a
Side has an inlet 12a through which the heat exchange fluid flows in, and the other 121b side has an outlet 12b through which the heat exchange fluid flows out. And the heat exchange fluid from the inlet 12a
Tank 121a → a plurality of fluid pipes 121c → tank 12
1b, and flows out of the outlet 12b. Here, as the heat exchange fluid, a so-called antifreeze obtained by mixing ethylene glycol or the like in water is used.

【００１９】吸着剤Ｓは、冷却されることにより冷媒蒸
気を吸着し、加熱されることにより吸着していた冷媒蒸
気を脱着するものであり、例えば、シリカゲル、ゼオラ
イト、活性炭、活性アルミナ等からなる。そして、上記
した熱交換器１２１のうち、タンク１２１ａ、１２１ｂ
や、複数の流体配管１２１ｃや、複数の伝熱フィン１２
１ｄの間に充填され、接着固定してある。なお、吸着コ
ア１２は上下方向に平行に配置されている。これによ
り、冷媒蒸気通路１１０からの冷媒蒸気が、吸着コア１
２の両面から吸着剤Ｓに供給される。The adsorbent S adsorbs the refrigerant vapor when cooled and desorbs the adsorbed refrigerant vapor when heated, and is made of, for example, silica gel, zeolite, activated carbon, activated alumina and the like. . And among the heat exchangers 121, the tanks 121a and 121b
And a plurality of fluid pipes 121c, a plurality of heat transfer fins 12
It is filled during 1d and is adhesively fixed. Note that the suction cores 12 are arranged in parallel in the vertical direction. As a result, the refrigerant vapor from the refrigerant vapor passage 110 is
2 to the adsorbent S from both sides.

【００２０】補助蒸発凝縮コア１３は、周知の熱交換器
形状を有しており、図２に示すように、一対のタンク１
３１、１３２の間に、複数の流体配管１３３と、複数の
蛇行状伝熱フィン１３４を交互に並列配置してなる。そ
して、この補助蒸発凝縮コア１３は、蒸発凝縮コア収容
部１１２のうち液冷媒Ｌの上方において、全面を横断す
るように（換言すれば、水平方向に平行に）設けられて
いる。なお、本実施形態では、主蒸発凝縮コア１４と所
定距離（例えば１０ｍｍ）を隔てた位置に、補助蒸発凝
縮コア１３を配置している。The auxiliary evaporation condensing core 13 has a well-known heat exchanger shape, and as shown in FIG.
A plurality of fluid pipes 133 and a plurality of meandering heat transfer fins 134 are alternately arranged in parallel between 31 and 132. The auxiliary evaporation / condensation core 13 is provided above the liquid refrigerant L in the evaporation / condensation core accommodating portion 112 so as to cross the entire surface (in other words, parallel to the horizontal direction). In the present embodiment, the auxiliary evaporative condensing core 13 is disposed at a position separated from the main evaporative condensing core 14 by a predetermined distance (for example, 10 mm).

【００２１】ここで、蒸発凝縮コア収容部１１２のうち
液冷媒Ｌの上方は、液冷媒Ｌから蒸発した冷媒蒸気が通
る冷媒蒸気通路（請求項でいう冷媒蒸気通路）を構成し
ている。なお、蒸発凝縮コア収容部１１２の内壁と補助
蒸発凝縮コア１３の外縁部（タンク１３１、１３２や、
端部に位置する流体配管１３３）との間の距離が微少
（例えば３ｍｍ）となるように構成されている。Here, a portion above the liquid refrigerant L in the evaporative condensation core accommodating portion 112 constitutes a refrigerant vapor passage (refrigerant vapor passage) through which the refrigerant vapor evaporated from the liquid refrigerant L passes. Note that the inner wall of the evaporative condensing core housing 112 and the outer edge of the auxiliary evaporating condensing core 13 (tanks 131 and 132,
The distance to the fluid pipe 133) located at the end is configured to be very small (for example, 3 mm).

【００２２】なお、一対のタンク１３１、１３２の一方
１３１は、仕切り板１３０にて２つのタンク１３１ａ、
１３１ｂに仕切られている。そして、２つのタンク１３
１ａ、１３１ｂの一方１３１ａ側に、熱交換流体が流入
する入口部１３ａを有し、他方１３１ｂ側に、熱交換流
体が流出する出口部１３ｂを有している。そして、入口
部１３ａからの熱交換流体は、タンク１３１ａ→複数の
流体配管１３３のうちタンク１３１ａに対応する配管→
タンク１３２→複数の流体配管１３３のうちタンク１３
１ｂに対応する配管→タンク１３１ｂの順に流れて、出
口部１３ｂから流出される。One of the pair of tanks 131, 132 is connected to two tanks 131a,
131b. And two tanks 13
On one 131a side of 1a and 131b, there is an inlet 13a into which the heat exchange fluid flows, and on the other 131b side, there is an outlet 13b from which the heat exchange fluid flows out. Then, the heat exchange fluid from the inlet 13a is supplied to the tank 131a → the pipe corresponding to the tank 131a among the plurality of fluid pipes 133 →
Tank 132 → tank 13 of the plurality of fluid pipes 133
It flows in the order of the pipe corresponding to 1b → the tank 131b, and flows out of the outlet 13b.

【００２３】主蒸発凝縮コア１４は、具体的な構造の図
示は省略するが、補助蒸発凝縮コア１３と同じ形状であ
る。そして、主蒸発凝縮コア１４は、蒸発凝縮コア収容
部１１２のうち液冷媒Ｌと接触するように、かつ、水平
方向に平行に設けられている。なお、主蒸発凝縮コア１
４の方が補助蒸発凝縮コア１３よりも熱交換面積が大き
くなるように（つまり、能力が大きくなるように）、主
蒸発凝縮コア１４の方が補助蒸発凝縮コア１３よりも厚
みが大きく構成されている。Although the specific structure of the main evaporative condensing core 14 is not shown, it has the same shape as the auxiliary evaporative condensing core 13. The main evaporative condensing core 14 is provided in contact with the liquid refrigerant L in the evaporating condensing core accommodating portion 112 and in parallel with the horizontal direction. The main evaporative condensing core 1
The main evaporative condensing core 14 is configured to be thicker than the auxiliary evaporative condensing core 13 so that the heat exchanging area of the main evaporating condensing core 13 is larger than that of the auxiliary evaporating condensing core 13. ing.

【００２４】そして、吸着コア１２の熱交換器１２１の
入口部１２ａと三方切替弁２１の出口ポート２１ｃとが
流体配管にて接続され、吸着コア１２の熱交換器１２１
の出口部１２ｂと三方切替弁２３の入口ポート２３ａと
が流体配管にて接続されている。また、三方切替弁２１
の第１入口ポート２１ａと室外熱交換器（放熱コア）２
４の出口部２４ｂとが流体配管にて接続され、三方切替
弁２１の第２入口ポート２１ｂとエンジン２２の出口部
２２ｂとが流体配管にて接続されている。また、三方切
替弁２３の第１出口ポート２３ｂと室外熱交換器２４の
入口部２４ａとが流体配管にて接続され、三方切替弁２
３の第２出口ポート２３ｃとエンジン２２の入口部２２
ａとが流体配管にて接続されている。The inlet 12a of the heat exchanger 121 of the adsorption core 12 and the outlet port 21c of the three-way switching valve 21 are connected by a fluid pipe.
The outlet 12b is connected to the inlet port 23a of the three-way switching valve 23 by a fluid pipe. Also, the three-way switching valve 21
First inlet port 21a and outdoor heat exchanger (radiation core) 2
The fourth outlet 24b is connected by a fluid pipe, and the second inlet port 21b of the three-way switching valve 21 and the outlet 22b of the engine 22 are connected by a fluid pipe. Further, the first outlet port 23b of the three-way switching valve 23 and the inlet 24a of the outdoor heat exchanger 24 are connected by a fluid pipe, and the three-way switching valve 2
3 and the inlet 22 of the engine 22
a is connected by a fluid pipe.

【００２５】なお、三方切替弁２１の出口ポート２１ｃ
と吸着コア１２の入口部１２ａとの間に設けた電動ポン
プ２５により、吸着コア１２の熱交換器１２１→三方切
替弁２３→エンジン２２または室外熱交換器２４→三方
切替弁２１の順に熱交換流体が循環される。ここで、吸
着コア１２の熱交換器１２１→三方切替弁２３→エンジ
ン２２→三方切替弁２１からなる流体循環路を第１流体
循環路Ａとし、吸着コア１２の熱交換器１２１→三方切
替弁２３→室外熱交換器２４→三方切替弁２１からなる
流体循環路を第２流体循環路Ｂとする。The outlet port 21c of the three-way switching valve 21
Heat is exchanged in the order of the heat exchanger 121 of the adsorption core 12, the three-way switching valve 23, the engine 22 or the outdoor heat exchanger 24, and the three-way switching valve 21 by the electric pump 25 provided between the suction core 12 and the inlet 12a of the adsorption core 12. Fluid is circulated. Here, the fluid circulation path including the heat exchanger 121 of the adsorption core 12 → the three-way switching valve 23 → the engine 22 → the three-way switching valve 21 is defined as a first fluid circulation path A, and the heat exchanger 121 of the adsorption core 12 → the three-way switching valve. A fluid circulation path composed of 23 → the outdoor heat exchanger 24 → the three-way switching valve 21 is referred to as a second fluid circulation path B.

【００２６】また、補助蒸発凝縮コア１３の入口部１３
ａと三方切替弁２７の出口ポート２７ｃとが流体配管に
て接続され、補助蒸発凝縮コア１３の出口部１３ｂと蒸
発凝縮コア１４の入口部１４ａとが流体配管にて接続さ
れ、蒸発凝縮コア１４の出口部１４ｂと三方切替弁２８
の入口ポート２８ａとが流体配管にて接続されている。
また、三方切替弁２７の第１入口ポート２７ａと室外熱
交換器２９の出口部２９ｂとが流体配管にて接続され、
三方切替弁２７の第２入口ポート２７ｂと室内熱交換器
２６の出口部２６ｂとが流体配管にて接続されている。
また、三方切替弁２８の第１出口ポート２８ｂと室内熱
交換器２６の入口部２６ａとが流体配管にて接続され、
三方切替弁２８の第２出口ポート２８ｃと室外熱交換器
２９の入口部２９ａとが流体配管にて接続されている。The inlet 13 of the auxiliary evaporative condensation core 13
a and an outlet port 27c of the three-way switching valve 27 are connected by a fluid pipe, an outlet 13b of the auxiliary evaporative condensing core 13 and an inlet 14a of the evaporative condensing core 14 are connected by a fluid pipe, and the evaporative condensing core 14 is connected. Outlet 14b and three-way switching valve 28
And an inlet port 28a is connected by a fluid pipe.
Further, the first inlet port 27a of the three-way switching valve 27 and the outlet 29b of the outdoor heat exchanger 29 are connected by a fluid pipe,
The second inlet port 27b of the three-way switching valve 27 and the outlet 26b of the indoor heat exchanger 26 are connected by a fluid pipe.
Further, a first outlet port 28b of the three-way switching valve 28 and an inlet 26a of the indoor heat exchanger 26 are connected by a fluid pipe,
A second outlet port 28c of the three-way switching valve 28 and an inlet 29a of the outdoor heat exchanger 29 are connected by a fluid pipe.

【００２７】なお、主蒸発凝縮コア１４の出口部１４ｂ
と三方切替弁２８の入口ポート２８ａとの間に設けた電
動ポンプ３０により、室内熱交換器２６または室外熱交
換器２９→三方切替弁２７→補助蒸発凝縮コア１３→主
蒸発凝縮コア１４→三方切替弁２８の順に熱交換流体が
循環される。ここで、室内熱交換器２６→三方切替弁２
７→補助蒸発凝縮コア１３→主蒸発凝縮コア１４→三方
切替弁２８からなる流体循環路を第３流体循環路Ｃと
し、室外熱交換器２９→三方切替弁２７→補助蒸発凝縮
コア１３→主蒸発凝縮コア１４→三方切替弁２８からな
る流体循環路を第４流体循環路Ｄとする。The outlet 14b of the main evaporative condensing core 14
The indoor heat exchanger 26 or the outdoor heat exchanger 29 → the three-way switching valve 27 → the auxiliary evaporative condensation core 13 → the main evaporative condensation core 14 → the three-way The heat exchange fluid is circulated in the order of the switching valve 28. Here, the indoor heat exchanger 26 → the three-way switching valve 2
7 → Auxiliary evaporative condensing core 13 → Main evaporative condensing core 14 → The fluid circulation path including the three-way switching valve 28 is the third fluid circulation path C, and the outdoor heat exchanger 29 → Three-way switching valve 27 → Auxiliary evaporating / condensing core 13 → Main The fluid circulation path composed of the evaporative condensation core 14 and the three-way switching valve 28 is referred to as a fourth fluid circulation path D.

【００２８】次に、上記構成による作動を説明する。ま
ず、本実施形態の吸着式冷凍装置１を作動させるとき
は、電動ポンプ２５、３０を駆動させる。そして、吸着
コア１２の吸着剤Ｓに冷媒蒸気を吸着させる吸着モード
を実行するときは、三方切替弁２１、２３、２７、２８
を図１中実線位置とする。これにより、第２流体循環路
Ｂおよび第３流体循環路Ｃに熱交換流体が循環して、吸
着剤Ｓが冷媒蒸気を吸着するとともに、液冷媒Ｌが蒸発
する。なお、この液冷媒が蒸発して形成される冷媒蒸気
は、補助蒸発凝縮コア１３の複数の流体配管１３３や伝
熱フィン１３４の間を通過して、吸着コア１２の吸着剤
Ｓへ吸着される。Next, the operation of the above configuration will be described. First, when operating the adsorption refrigeration apparatus 1 of the present embodiment, the electric pumps 25 and 30 are driven. Then, when executing the adsorption mode in which the refrigerant vapor is adsorbed by the adsorbent S of the adsorption core 12, the three-way switching valves 21, 23, 27, 28
Is a solid line position in FIG. Thereby, the heat exchange fluid circulates through the second fluid circulation path B and the third fluid circulation path C, and the adsorbent S adsorbs the refrigerant vapor and the liquid refrigerant L evaporates. The refrigerant vapor formed by evaporating the liquid refrigerant passes between the plurality of fluid pipes 133 and the heat transfer fins 134 of the auxiliary evaporation condensing core 13 and is adsorbed on the adsorbent S of the adsorption core 12. .

【００２９】そして、液冷媒が蒸発するときに発生する
蒸発潜熱により、主蒸発凝縮コア１４を循環する熱交換
流体が冷却され、この冷却された熱交換流体を、第３流
体循環路Ｃを経て室内熱交換器２６に循環させることに
より室内（被冷却部）を冷房（冷却）する。また、吸着
熱により吸着コア１２の熱交換器１２１を循環する熱交
換流体が加熱され、この加熱された熱交換流体を、第２
流体循環路Ｂを経て室内熱交換器２４に循環させること
により室外へ放熱（冷却）する。Then, the heat exchange fluid circulating in the main evaporative condensing core 14 is cooled by the latent heat of vaporization generated when the liquid refrigerant evaporates, and the cooled heat exchange fluid is passed through the third fluid circulation path C. By circulating through the indoor heat exchanger 26, the room (the part to be cooled) is cooled (cooled). Further, the heat exchange fluid circulating through the heat exchanger 121 of the adsorption core 12 is heated by the heat of adsorption, and the heated heat exchange fluid is supplied to the second heat exchange fluid.
Heat is radiated (cooled) to the outside by circulating through the fluid circulation path B to the indoor heat exchanger 24.

【００３０】ここで、冷媒蒸気が吸着されることにより
密閉容器１１内は低圧（例えば１０ｔｏｒｒ程度）とな
るため液冷媒Ｌが沸騰するような状態となり、しかも、
液冷媒の蒸発は、液冷媒Ｌの表面だけでなく内部におい
ても活発に行なわれる。このため、液冷媒Ｌ内部に生じ
た気泡が液冷媒Ｌの表面において弾けることにより、例
えば１００〜２００μ程度の粒径の微細な液滴が飛び出
す。Here, the inside of the closed vessel 11 is set to a low pressure (for example, about 10 torr) due to the adsorption of the refrigerant vapor, so that the liquid refrigerant L is brought into a state of boiling.
Evaporation of the liquid refrigerant is actively performed not only on the surface of the liquid refrigerant L but also inside. For this reason, bubbles generated inside the liquid refrigerant L pop on the surface of the liquid refrigerant L, so that fine droplets having a particle size of, for example, about 100 to 200 μ fly out.

【００３１】これに対して本実施形態では、液冷媒Ｌの
表面よりも上方に設けた補助蒸発凝縮コア１３（具体的
には、複数の流体配管１３３や伝熱フィン１３４の壁
面）に液滴状の冷媒が付着し、この補助蒸発凝縮コア１
３において蒸発するので、補助蒸発凝縮コア１３よりも
上方に設けた吸着コア１２側に液滴状の冷媒が移動する
ことを抑制でき、吸着剤Ｓや熱交換器１２１に液滴状の
冷媒が付着することを抑制できる。よって、吸着剤Ｓの
吸着、脱着能力や、熱交換器１２１の熱交換能力を良好
に維持できるため、吸着コア１２の吸着能力を良好に維
持できる。On the other hand, in the present embodiment, droplets are deposited on the auxiliary evaporation / condensation core 13 (specifically, the wall surfaces of the plurality of fluid pipes 133 and the heat transfer fins 134) provided above the surface of the liquid refrigerant L. Refrigerant is attached to the auxiliary evaporative condensing core 1
3, the droplet-shaped refrigerant can be prevented from moving to the side of the adsorption core 12 provided above the auxiliary evaporation condensation core 13, and the droplet-shaped refrigerant is transferred to the adsorbent S and the heat exchanger 121. Adhesion can be suppressed. Therefore, the ability to adsorb and desorb the adsorbent S and the ability to exchange heat of the heat exchanger 121 can be favorably maintained, so that the ability to adsorb the adsorption core 12 can be favorably maintained.

【００３２】しかも、室内熱交換器２６において吸熱し
た比較的高温な（例えば２０℃の）熱交換流体を、先に
補助蒸発凝縮コア１３に流すので、この補助蒸発凝縮コ
ア１３における冷媒の蒸発を良好に行なうことができ
る。また、液滴状の冷媒を蒸発させるときの蒸発潜熱に
より、室内熱交換器２６を含む第３流体循環路Ｃに循環
させる熱交換流体を冷却できるので、冷熱のロスを低減
できる。Moreover, since the relatively high-temperature (eg, 20 ° C.) heat exchange fluid that has absorbed heat in the indoor heat exchanger 26 flows first to the auxiliary evaporation and condensation core 13, the refrigerant in the auxiliary evaporation and condensation core 13 is evaporated. It can be performed well. Further, since the heat exchange fluid circulated through the third fluid circulation path C including the indoor heat exchanger 26 can be cooled by the latent heat of vaporization when the droplet-shaped refrigerant is evaporated, the loss of cold heat can be reduced.

【００３３】そして、このような吸着モードを所定時間
行なうと、吸着剤Ｓの吸着能力が低下するため、吸着剤
Ｓから冷媒蒸気を脱着させる脱着モードを実行する。こ
のときは、三方切替弁２１、２３、２７、２８を図１中
一点鎖線位置とする。これにより、第１流体循環路Ａお
よび第４流体循環路Ｄに熱交換流体が循環して、吸着コ
ア１２の熱交換器１２１に、エンジン２２のエンジン冷
却水（熱交換流体）が循環されるので、吸着剤Ｓが加熱
されて、吸着剤Ｓが吸着していた冷媒を脱着する。If such an adsorption mode is performed for a predetermined time, the adsorption capacity of the adsorbent S is reduced, so that a desorption mode for desorbing refrigerant vapor from the adsorbent S is executed. At this time, the three-way switching valves 21, 23, 27, and 28 are set to the position indicated by the one-dot chain line in FIG. Thereby, the heat exchange fluid circulates through the first fluid circulation path A and the fourth fluid circulation path D, and the engine coolant (heat exchange fluid) of the engine 22 circulates through the heat exchanger 121 of the adsorption core 12. Therefore, the adsorbent S is heated, and the refrigerant on which the adsorbent S is adsorbed is desorbed.

【００３４】この脱着された冷媒蒸気は、補助蒸発凝縮
コア１３および主蒸発凝縮コア１４近傍において凝縮さ
れる。このときの凝縮熱により、補助蒸発凝縮コア１３
および主蒸発凝縮コア１４を流れる熱交換流体が加熱さ
れ、この加熱された熱交換流体を、第４流体循環路Ｄを
経て室内熱交換器２９に循環させることにより室外へ放
熱（冷却）される。The desorbed refrigerant vapor is condensed in the vicinity of the auxiliary evaporative condensing core 13 and the main evaporative condensing core 14. Due to the heat of condensation at this time, the auxiliary evaporation condensing core 13
The heat exchange fluid flowing through the main evaporative condensing core 14 is heated, and the heated heat exchange fluid is circulated to the indoor heat exchanger 29 via the fourth fluid circulation path D to be radiated (cooled) to the outside of the room. .

【００３５】そして、このような脱着モードを所定時間
行なうと、吸着剤Ｓの吸着能力が再生されるため、再び
上記吸着モードを実行させる。以降、吸着モードと脱着
モードとを、所定時間毎に交互に実行させることによ
り、室内の冷房を連続的に行なう。 （第２の実施形態）本実施形態では、補助蒸発凝縮コア
１３として、図３に示すようなものを採用している。す
なわち、補助蒸発凝縮コア１３は、入口部１３ａから出
口部１３ｂにかけて、細長な流体配管を蛇行状に曲げ加
工してなる蛇行チューブ１３５を備えている。ここで、
蛇行チューブ１３５は、複数の直線的な流体配管部１３
５ａを、所定距離を隔てて並列的に配置したような構造
をなしており、これら流体配管１３５ａの間のそれぞれ
に、蛇行状の伝熱フィン１３４を配している。このよう
な補助蒸発凝縮コア１３を採用しても、上記第１の実施
形態と同様の効果が得られる。When the desorption mode is performed for a predetermined time, the adsorption capacity of the adsorbent S is regenerated, so that the adsorption mode is executed again. Thereafter, the indoor mode is continuously cooled by alternately executing the adsorption mode and the desorption mode at predetermined time intervals. (Second Embodiment) In this embodiment, the auxiliary evaporation condensing core 13 as shown in FIG. 3 is employed. That is, the auxiliary evaporation condensing core 13 includes a meandering tube 135 formed by bending an elongated fluid pipe in a meandering shape from the inlet 13a to the outlet 13b. here,
The serpentine tube 135 includes a plurality of linear fluid pipes 13.
5a are arranged in parallel at a predetermined distance from each other, and meandering heat transfer fins 134 are arranged between the fluid pipes 135a. Even if such an auxiliary evaporation condensing core 13 is employed, the same effect as in the first embodiment can be obtained.

【００３６】（第３の実施形態）本実施形態では、図４
に示すように、補助蒸発凝縮コア１３の上方および下方
に、従来技術と同様の液滴通過阻止部材３１を設けてい
る。この液滴通過阻止部材３１１は、金網（メッシュ）
の表面に撥水処理を施して構成され、この場合、例えば
２００メッシュの金網に、４フッ化エチレン樹脂からな
る撥水剤を塗布して構成されている。(Third Embodiment) In the present embodiment, FIG.
As shown in (1), above the auxiliary evaporation / condensation core 13, a droplet passage preventing member 31 similar to the prior art is provided. The droplet passage preventing member 311 is made of a wire mesh (mesh).
In this case, for example, a 200-mesh wire net is coated with a water-repellent agent made of tetrafluoroethylene resin.

【００３７】これにより、蒸発凝縮１４近傍にて蒸発し
た冷媒蒸気は、液滴通過阻止部材３１の網の目を通って
吸着コア１２に流入するが、上記微細な液滴は、液滴通
過阻止部材３１により跳ね返されて通過が阻止される。
このため、上記第１、第２の実施形態よりも確実に、液
滴が吸着コア１２側へ移動することを抑制でき、吸着剤
Ｓに液滴が付着することを抑制できる。As a result, the refrigerant vapor evaporated near the evaporative condensate 14 flows into the adsorption core 12 through the mesh of the droplet passage preventing member 31, but the fine droplets are prevented from passing through the droplet. It is bounced back by the member 31 and passage is prevented.
For this reason, it is possible to more reliably suppress the droplet from moving to the adsorption core 12 side than in the first and second embodiments, and it is possible to suppress the droplet from adhering to the adsorbent S.

【００３８】なお、液滴通過阻止部材３１の網の目の大
きさは、細かいほど液滴通過阻止の効果は高いが、その
反面通気抵抗ともなる事情があり、３０メッシュから２
００メッシュの間が好適する。また、撥水処理として
も、例えば撥水剤の塗布や含浸、撥水性シートの貼付け
等を用いることができ、このときの撥水剤としては、４
フッ化エチレン樹脂以外にも、４フッ化エチレンと６フ
ッ化プロピレンとの共重合樹脂、シリコン樹脂、パラフ
ィンやワセリン等の鉱油、これら鉱油にステアリン酸、
ラウリン酸等の脂肪酸を加えた溶液等を用いることがで
きる。The smaller the mesh size of the droplet passage preventing member 31 is, the higher the effect of preventing the passage of the droplet is. However, on the other hand, the mesh also has a resistance to air flow.
Between 00 mesh is preferred. Also, as the water repellent treatment, for example, application or impregnation of a water repellent, application of a water repellent sheet, or the like can be used.
In addition to fluorinated ethylene resins, copolymer resins of tetrafluoroethylene and propylene hexafluoride, silicone resins, mineral oils such as paraffin and petrolatum, stearic acid,
A solution to which a fatty acid such as lauric acid is added can be used.

【００３９】（第４の実施形態）図５に示す本実施形態
は、上記した従来技術（図７参照）と同様の吸着式冷凍
装置１に本発明を適用したものである。このため、上記
した従来技術において、変更部分についての説明を補足
する。すなわち、上記第１、第２の実施形態における補
助蒸発凝縮コア１３と同様の構造をした補助蒸発コア１
３０を、蒸発凝縮コア収容部１１２のうち液冷媒Ｌの上
方（請求項でいう冷媒蒸気通路）において、全面を横断
するように（換言すれば、水平方向に平行に）設けてい
る。そして、補助蒸発コア１３０の出口部１３０ｂと、
蒸発コア１４１（以下、主蒸発コアという）の入口部１
４１ａとを流体配管にて接続しており、補助蒸発コア１
３０の入口部１３０ａと図示しない室内熱交換器の出口
部、蒸発コア１４１の出口部１４１ｂと図示しない室内
熱交換器の入口部とを、流体配管にて接続している。ま
た、凝縮コア１４２の入口部１４２ａと図示しない室外
熱交換器の出口部、凝縮コア１４１の出口部１４２ｂと
図示しない室外熱交換器の入口部とを、流体配管にて接
続している。(Fourth Embodiment) In the present embodiment shown in FIG. 5, the present invention is applied to the adsorption refrigeration system 1 similar to the above-described prior art (see FIG. 7). Therefore, in the above-described related art, a description of a changed portion will be supplemented. That is, the auxiliary evaporation core 1 having the same structure as the auxiliary evaporation and condensation core 13 in the first and second embodiments.
30 is provided above the liquid refrigerant L (the refrigerant vapor passage in the claims) in the evaporative condensation core accommodating portion 112 so as to cross the entire surface (in other words, parallel to the horizontal direction). And an outlet 130b of the auxiliary evaporation core 130;
Inlet 1 of evaporation core 141 (hereinafter referred to as main evaporation core)
41a is connected to the auxiliary evaporation core 1 by a fluid pipe.
The inlet portion 130a of 30 and the outlet portion of the indoor heat exchanger (not shown), the outlet portion 141b of the evaporation core 141 and the inlet portion of the indoor heat exchanger (not shown) are connected by fluid piping. In addition, an inlet 142a of the condensing core 142 and an outlet of an unillustrated outdoor heat exchanger, and an outlet 142b of the condensing core 141 and an inlet of an unillustrated outdoor heat exchanger are connected by a fluid pipe.

【００４０】そして、ドア手段１１１ｃにて冷媒出入口
１１１ａを開口し、ドア手段１１１ｄにて冷媒出入口１
１１ｂを閉塞して、吸着コア３の熱交換器に冷却流体を
循環させると、吸着剤Ｓが冷却されて冷媒蒸気を吸着す
るとともに、蒸発コア１４１と接触する液冷媒Ｌが蒸発
する。これにより、蒸発コア１４１を循環する熱交換流
体が冷却され、この冷却された熱交換流体を室内熱交換
器に循環させることにより、室内冷房を行なっている。The refrigerant port 111a is opened by the door means 111c, and the refrigerant port 1 is opened by the door means 111d.
When the cooling fluid is circulated through the heat exchanger of the adsorption core 3 by closing the 11b, the adsorbent S is cooled to adsorb the refrigerant vapor, and the liquid refrigerant L in contact with the evaporation core 141 evaporates. As a result, the heat exchange fluid circulating in the evaporation core 141 is cooled, and the cooled heat exchange fluid is circulated through the indoor heat exchanger to perform indoor cooling.

【００４１】このとき、液冷媒Ｌの表面よりも上方に設
けた補助蒸発コア１３０に、上記液滴状の冷媒が付着
し、この補助蒸発コア１３０において蒸発するので、補
助蒸発コア１３０よりも上方に設けた吸着コア１２側へ
液滴状の冷媒が移動することを抑制でき、吸着剤Ｓや熱
交換器に液滴状の冷媒が付着することを抑制できる。よ
って、吸着剤Ｓの吸着、脱着能力や、熱交換器の熱交換
能力を良好に維持できるため、吸着コア１２の吸着能力
を良好に維持できる。At this time, the droplet-shaped refrigerant adheres to the auxiliary evaporation core 130 provided above the surface of the liquid refrigerant L and evaporates in the auxiliary evaporation core 130. It is possible to suppress the movement of the droplet-shaped refrigerant to the side of the adsorption core 12 provided in the above, and it is possible to suppress the droplet-shaped refrigerant from adhering to the adsorbent S and the heat exchanger. Therefore, the ability to adsorb and desorb the adsorbent S and the ability to exchange heat of the heat exchanger can be favorably maintained, so that the ability to adsorb the adsorption core 12 can be favorably maintained.

【００４２】しかも、室内熱交換器２６において吸熱し
た比較的高温な熱交換流体を、先に補助蒸発コア１３０
に流すので、この補助蒸発コア１３０における冷媒の蒸
発を良好に行なうことができる。そして、ドア手段１１
１ｃにて冷媒出入口１１１ａを閉塞し、ドア手段１１１
ｄにて冷媒出入口１１１ｂを開口して、吸着コア３の熱
交換器に加熱流体を循環させると、吸着剤Ｓが加熱され
て冷媒蒸気を脱着するとともに、凝縮コア１４２におい
て冷媒蒸気を凝縮させる。これにより、吸着剤Ｓが再生
される。Further, the relatively high-temperature heat exchange fluid that has absorbed heat in the indoor heat exchanger 26 is
, The refrigerant in the auxiliary evaporation core 130 can be favorably evaporated. And the door means 11
1c, the refrigerant port 111a is closed, and the door means 111 is closed.
When the refrigerant inlet / outlet 111b is opened at d and the heating fluid is circulated through the heat exchanger of the adsorption core 3, the adsorbent S is heated to desorb the refrigerant vapor and condense the refrigerant vapor in the condensing core 142. Thereby, the adsorbent S is regenerated.

【００４３】（第５の実施形態）本実施形態は、図６に
示すような吸収式冷凍装置１に本発明を適用したもので
ある。すなわち、密閉回路１１内には、吸収コア５、再
生コア６、主蒸発コア１４１、補助蒸発コア１３０、お
よび、凝縮コア１４２が収容されている。吸収コア５お
よび再生コア６は、吸収液Ｍと、この吸収液Ｍと接触し
て設けられる周知の熱交換器形状をなす熱交換器５１、
６１とを有している。吸収液Ｍは、冷却されることによ
り冷媒蒸気を吸収し、加熱されることにより吸収してい
た冷媒蒸気を分離するものであり、例えば、ＬｉＢｒ水
溶液からなる。(Fifth Embodiment) In this embodiment, the present invention is applied to an absorption refrigeration apparatus 1 as shown in FIG. That is, in the closed circuit 11, the absorption core 5, the regeneration core 6, the main evaporation core 141, the auxiliary evaporation core 130, and the condensing core 142 are accommodated. The absorption core 5 and the regeneration core 6 are provided with an absorption liquid M and a heat exchanger 51 having a well-known heat exchanger shape provided in contact with the absorption liquid M,
61. The absorbing liquid M absorbs the refrigerant vapor when cooled, and separates the absorbed refrigerant vapor when heated, and is made of, for example, an aqueous LiBr solution.

【００４４】そして、吸収コア５の熱交換器５１の入口
部５ａから出口部５ｂにかけて熱交換流体（冷却流体）
が流れ、さらに、熱交換器５１の出口部５ｂからの熱交
換流体が、凝縮コア１４２の入口部１４２ａから出口部
１４２ｂにかけて流れる。また、再生コア６の熱交換器
６１の入口部６ａから出口部６ｂにかけて熱交換流体
（加熱流体）が流れる。本実施形態では、上記冷却流体
として、図示しない室外熱交換器にて放熱した熱交換流
体を用い、上記加熱流体として、図示しないエンジンの
エンジン冷却水を用いている。The heat exchange fluid (cooling fluid) flows from the inlet 5a to the outlet 5b of the heat exchanger 51 of the absorption core 5.
Then, the heat exchange fluid from the outlet 5b of the heat exchanger 51 flows from the inlet 142a to the outlet 142b of the condensing core 142. A heat exchange fluid (heating fluid) flows from the inlet 6a to the outlet 6b of the heat exchanger 61 of the regenerating core 6. In the present embodiment, a heat exchange fluid radiated by an outdoor heat exchanger (not shown) is used as the cooling fluid, and engine cooling water of an engine (not shown) is used as the heating fluid.

【００４５】なお、密閉回路１１には、上記した蒸発コ
ア収容部１１２および凝縮コア収容部１１３の他に、吸
収コア５を収容する吸収コア収容部１１８と、再生コア
６を収容する再生コア収容部１１９とを有している。そ
して、密閉容器１１は、吸収コア収容部１１８内の吸収
液Ｍと再生コア収容部１１９内の吸収液Ｍとの間を、吸
収液供給通路１２０、吸収液排出通路１２１にて連通し
た形態であり、さらに、吸収コア収容部１１８と蒸発コ
ア収容部１１２との間、および、再生コア収容部１１９
と凝縮コア収容部１１３との間を、冷媒蒸気通路１２
２、１２３にて連通した形態である。The closed circuit 11 includes, in addition to the evaporating core housing 112 and the condensing core housing 113 described above, an absorbing core housing 118 for housing the absorbing core 5 and a recycled core housing for housing the reproducing core 6. A part 119 is provided. The closed container 11 is configured so that the absorbing liquid M in the absorbing core housing section 118 and the absorbing liquid M in the regenerating core housing section 119 communicate with each other through an absorbing liquid supply passage 120 and an absorbing liquid discharge passage 121. Yes, further, between the absorbing core housing section 118 and the evaporating core housing section 112, and the regenerating core housing section 119.
Between the refrigerant vapor passage 12 and
This is a form in which communication is made at 2, 123.

【００４６】そして、吸収液供給通路１２０と吸収液排
出通路１２１とは、途中の熱交換部１２４において熱交
換がなされるようになっている。また、再生コア６の熱
交換器６１と接触する吸収液Ｍから分離された冷媒蒸気
は、冷媒蒸気通路１２３を通って凝縮コア１４２側へ供
給され、蒸発コア１４１において蒸発された冷媒蒸気
は、冷媒蒸気通路１２３を通って吸収コア５の吸収液Ｍ
に吸収されるようになっている。Then, heat is exchanged between the absorption liquid supply passage 120 and the absorption liquid discharge passage 121 in the heat exchange section 124 on the way. The refrigerant vapor separated from the absorbing liquid M that comes into contact with the heat exchanger 61 of the regeneration core 6 is supplied to the condensing core 142 through the refrigerant vapor passage 123, and the refrigerant vapor evaporated in the evaporation core 141 is Through the refrigerant vapor passage 123, the absorption liquid M of the absorption core 5
Is to be absorbed.

【００４７】なお、吸収コア５の熱交換器５１と接触す
る吸収液Ｍが、この熱交換器５１を流れる冷却流体によ
って冷却されることにより、冷媒蒸気を吸収し、再生コ
ア６の熱交換器６１と接触する吸収液Ｍが、この熱交換
器６１を流れる加熱流体によって加熱されることによ
り、冷媒蒸気を分離する。また、吸収コア５の熱交換器
５１から流出された冷却流体は、さらに凝縮コア１４２
を流れて凝縮熱を吸熱する。The absorption liquid M coming into contact with the heat exchanger 51 of the absorption core 5 is cooled by the cooling fluid flowing through the heat exchanger 51 to absorb the refrigerant vapor, and the heat exchanger 51 of the regeneration core 6 The absorbing liquid M in contact with 61 is heated by the heating fluid flowing through the heat exchanger 61 to separate the refrigerant vapor. Further, the cooling fluid flowing out of the heat exchanger 51 of the absorption core 5 further condenses the condensing core 142
To absorb heat of condensation.

【００４８】そして、本実施形態においても、液冷媒Ｌ
の表面よりも上方に設けた補助蒸発コア１３０に、上記
液滴状の冷媒が付着し、この補助蒸発コア１３０におい
て蒸発するので、冷媒通路１２２を経て吸収コア５側へ
液滴状の冷媒が移動することを抑制できる。よって、吸
収コア５と接触する吸収液Ｍに液滴状の冷媒が吸収され
ることを抑制できる。なお、吸収液Ｍに液滴が吸収され
ると、蒸発潜熱が発生しないため、吸収能力が活用され
ない、といった問題がある。In this embodiment, the liquid refrigerant L
The droplet-shaped refrigerant adheres to the auxiliary evaporation core 130 provided above the surface of the core and evaporates in the auxiliary evaporation core 130, so that the droplet-shaped refrigerant flows to the absorption core 5 side through the refrigerant passage 122. Movement can be suppressed. Therefore, it is possible to prevent the droplet-shaped refrigerant from being absorbed by the absorbing liquid M that comes into contact with the absorbing core 5. When the liquid droplets are absorbed by the absorbing liquid M, there is a problem that the latent heat of vaporization is not generated, so that the absorbing ability is not utilized.

【００４９】また、本実施形態では、冷媒蒸気通路１２
２の全面を横断するように、液滴通過阻止部材３１を配
している。これにより、吸収コア５の吸収液Ｍに液滴状
の冷媒が吸収されることをより効果的に抑制できる。 （他の実施形態）まず、上記第１、第２の実施形態にお
いて、補助蒸発凝縮コア１３と主蒸発凝縮コア１４とを
一体に設けてもよいし、上記第３ないし第５の実施形態
において、補助蒸発コア１３０と主蒸発コア１４１とを
一体に設けてもよい。ただし、一体の蒸発凝縮コア（蒸
発コア）のうち、液冷媒Ｌに接触していない部位に、室
内熱交換器２６にて吸熱した比較的高温な熱交換流体を
先に流すようにする。これにより、上記液冷媒Ｌに接触
していない部位に液滴状の冷媒が付着して蒸発するの
で、上記実施形態と同様の効果が得られる。In this embodiment, the refrigerant vapor passage 12
The liquid drop passage preventing member 31 is arranged so as to cross the entire surface of the liquid crystal 2. Thereby, it is possible to more effectively suppress the droplet-like refrigerant from being absorbed by the absorbing liquid M of the absorbing core 5. (Other Embodiments) First, in the first and second embodiments, the auxiliary evaporative condensing core 13 and the main evaporative condensing core 14 may be provided integrally, or in the third to fifth embodiments. The auxiliary evaporation core 130 and the main evaporation core 141 may be provided integrally. However, a relatively high-temperature heat exchange fluid that has absorbed heat in the indoor heat exchanger 26 flows first to a portion of the integral evaporative condensation core (evaporation core) that is not in contact with the liquid refrigerant L. Thereby, the droplet-shaped refrigerant adheres to the portion not in contact with the liquid refrigerant L and evaporates, so that the same effect as in the above embodiment can be obtained.

【００５０】また、上記第１の実施形態において、上記
したユニット１０を２つ設けてもよい。これによれば、
一方のユニットにおいて、吸着コアが冷媒を吸着し、補
助蒸発凝縮コアおよび主蒸発凝縮コアが冷媒を蒸発させ
るとともに、他方のユニットにおいて、吸着コアが冷媒
を脱着し、補助蒸発凝縮コアおよび主蒸発凝縮コアが冷
媒を凝縮させる行程を、交互に行なわせることにより、
連続的に室内冷房を行なうことができる。In the first embodiment, two units 10 may be provided. According to this,
In one unit, the adsorption core adsorbs the refrigerant, the auxiliary evaporative condensing core and the main evaporative condensing core evaporate the refrigerant, and in the other unit, the adsorbing core desorbs the refrigerant, and the auxiliary evaporative condensing core and the main evaporative condensing core. By alternately performing the process in which the core condenses the refrigerant,
Indoor cooling can be performed continuously.

【００５１】また、上記第５の実施形態において、吸収
液としては、ＮＨ3 、ＬｉＣｌ、グリコール系溶液等を
用いることができる。その他、本発明は上記した各実施
形態に限定されるものではなく、例えば蒸発コアを収容
する蒸発コア収容部１１２において直接的に外部（外
気）と熱交換するような構成であっても良い等、要旨を
逸脱しない範囲内で適宜変更して実施し得るものであ
る。In the fifth embodiment, NH 3, LiCl, a glycol-based solution or the like can be used as the absorbing solution. In addition, the present invention is not limited to each of the above-described embodiments. For example, a configuration may be employed in which the heat exchange with the outside (outside air) is directly performed in the evaporating core accommodating portion 112 accommodating the evaporating core. However, the present invention can be implemented with appropriate changes without departing from the scope of the present invention.

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

【図１】本発明の第１の実施形態に係わる吸着式冷凍装
置の概略構成図である。FIG. 1 is a schematic configuration diagram of an adsorption-type refrigeration apparatus according to a first embodiment of the present invention.

【図２】本発明の第１の実施形態に係わる補助蒸発凝縮
コアの上面取付図である。FIG. 2 is a top view of the auxiliary evaporative condensing core according to the first embodiment of the present invention.

【図３】本発明の第２の実施形態に係わる補助蒸発凝縮
コアの上面取付図である。FIG. 3 is a top view of an auxiliary evaporative condensation core according to a second embodiment of the present invention.

【図４】本発明の第３の実施形態に係わる吸着式冷凍装
置の概略構成図である。FIG. 4 is a schematic configuration diagram of an adsorption refrigeration apparatus according to a third embodiment of the present invention.

【図５】本発明の第４の実施形態に係わる吸着式冷凍装
置の概略構成図である。FIG. 5 is a schematic configuration diagram of an adsorption refrigeration apparatus according to a fourth embodiment of the present invention.

【図６】本発明の第５の実施形態に係わる吸収式冷凍装
置の概略構成図である。FIG. 6 is a schematic configuration diagram of an absorption refrigeration apparatus according to a fifth embodiment of the present invention.

【図７】従来技術に係わる吸着式冷凍装置の概略構成図
である。FIG. 7 is a schematic configuration diagram of an adsorption refrigeration apparatus according to a conventional technique.

【符号の説明】[Explanation of symbols]

１２…吸着コア、Ｓ…吸着剤、１３…補助蒸発凝縮コア
（補助蒸発コア）、１４…主蒸発凝縮コア（主蒸発コ
ア）、Ｌ…液冷媒、２６…室内熱交換器。12: adsorption core, S: adsorbent, 13: auxiliary evaporative condensing core (auxiliary evaporating core), 14: main evaporative condensing core (main evaporating core), L: liquid refrigerant, 26: indoor heat exchanger.

Claims (4)

【特許請求の範囲】[Claims] 【請求項１】 液冷媒（Ｌ）と接触して配される主蒸発
コア（１４、１４１）にて蒸発させた冷媒蒸気を、前記
液冷媒（Ｌ）と非接触状態で配される吸着コア（１２）
にて吸着し、前記主蒸発コア（１４、１４１）にて冷却
される熱交換流体を熱交換器（２６）に流すことによ
り、被冷却部を冷却する冷凍装置において、 前記主蒸発コア（１４、１４１）と前記吸着コア（１
２）との間に、冷媒を蒸発させる補助蒸発コア（１３、
１３０）を、前記液冷媒（Ｌ）と非接触状態で設け、 前記熱交換器（２６）において吸熱した熱交換流体を、
先に前記補助蒸発コア（１３、１３０）に流し、その
後、前記主蒸発コア（１４、１４１）に流すことを特徴
とする冷凍装置。1. An adsorption core disposed in a non-contact state with the liquid refrigerant (L), wherein refrigerant vapor evaporated in a main evaporation core (14, 141) disposed in contact with the liquid refrigerant (L) is disposed. (12)
In a refrigerating apparatus that cools a portion to be cooled by flowing a heat exchange fluid that is adsorbed at a temperature and cooled by the main evaporation core (14, 141) to a heat exchanger (26), , 141) and the adsorption core (1).
2), an auxiliary evaporation core (13,
130) is provided in a non-contact state with the liquid refrigerant (L), and the heat exchange fluid that has absorbed heat in the heat exchanger (26) is
A refrigeration system characterized by flowing first to the auxiliary evaporation cores (13, 130) and then to the main evaporation cores (14, 141). 【請求項２】 前記主蒸発コア（１４１）と前記吸着コ
ア（１２）との間の冷媒蒸気通路（１１２）の全面を横
断するように、前記補助蒸発コア（１３、１３０）を設
けることを特徴とする請求項１に記載の冷凍装置。2. The method according to claim 1, wherein the auxiliary evaporation cores (13, 130) are provided to traverse the entire surface of the refrigerant vapor passage (112) between the main evaporation core (141) and the adsorption core (12). The refrigeration apparatus according to claim 1, wherein 【請求項３】 液冷媒（Ｌ）と接触して配される主蒸発
コア（１４１）にて蒸発させた冷媒蒸気を、前記液冷媒
（Ｌ）と非接触状態で配される吸収コア（５）にて吸収
し、前記主蒸発コア（１４１）にて冷却される熱交換流
体を熱交換器（２６）に流すことにより、被冷却部を冷
却する冷凍装置において、 前記主蒸発コア（１４１）と前記吸収コア（５）との間
に、冷媒を蒸発させる補助蒸発コア（１３０）を、前記
液冷媒（Ｌ）と非接触状態で設け、 前記熱交換器（２６）において吸熱した熱交換流体を、
先に前記補助蒸発コア（１３０）に流し、その後、前記
主蒸発コア（１４１）に流すことを特徴とする冷凍装
置。3. An absorption core (5) which is provided in a non-contact state with the liquid refrigerant (L) in a state where the refrigerant vapor evaporated in a main evaporation core (141) disposed in contact with the liquid refrigerant (L) is not contacted. ), And a heat exchange fluid that is cooled by the main evaporation core (141) flows through the heat exchanger (26) to cool the portion to be cooled. An auxiliary evaporating core (130) for evaporating refrigerant is provided in a non-contact state between the liquid refrigerant (L) and the heat exchange fluid absorbed in the heat exchanger (26). To
A refrigeration system characterized by flowing first to the auxiliary evaporation core (130) and then to the main evaporation core (141). 【請求項４】 前記主蒸発コア（１４１）と前記吸収コ
ア（５）との間の冷媒蒸気通路（１１２）の全面を横断
するように、前記補助蒸発コア（１３０）を設けること
を特徴とする請求項３に記載の冷凍装置。4. The auxiliary evaporation core (130) is provided so as to cross the entire surface of the refrigerant vapor passage (112) between the main evaporation core (141) and the absorption core (5). The refrigeration apparatus according to claim 3, wherein
JP16161897A 1997-06-18 1997-06-18 Refrigeration equipment Expired - Fee Related JP3740794B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16161897A JP3740794B2 (en) 1997-06-18 1997-06-18 Refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16161897A JP3740794B2 (en) 1997-06-18 1997-06-18 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JPH1114183A true JPH1114183A (en) 1999-01-22
JP3740794B2 JP3740794B2 (en) 2006-02-01

Family

ID=15738607

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16161897A Expired - Fee Related JP3740794B2 (en) 1997-06-18 1997-06-18 Refrigeration equipment

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Country Link
JP (1) JP3740794B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001227839A (en) * 2000-02-16 2001-08-24 Fuji Silysia Chemical Ltd Air conditioning system
CN103822396A (en) * 2014-02-08 2014-05-28 河南科技大学 Heat exchanger running auxiliary system and heat exchanger system using same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001227839A (en) * 2000-02-16 2001-08-24 Fuji Silysia Chemical Ltd Air conditioning system
CN103822396A (en) * 2014-02-08 2014-05-28 河南科技大学 Heat exchanger running auxiliary system and heat exchanger system using same
CN103822396B (en) * 2014-02-08 2016-03-09 河南科技大学 Heat exchanger runs accessory system and uses the heat exchanger system of this system

Also Published As

Publication number Publication date
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