JPH07208826A - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JPH07208826A
JPH07208826A JP6002987A JP298794A JPH07208826A JP H07208826 A JPH07208826 A JP H07208826A JP 6002987 A JP6002987 A JP 6002987A JP 298794 A JP298794 A JP 298794A JP H07208826 A JPH07208826 A JP H07208826A
Authority
JP
Japan
Prior art keywords
pipe
absorption
liquid refrigerant
air conditioner
liquid
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.)
Pending
Application number
JP6002987A
Other languages
Japanese (ja)
Inventor
Masayuki Fujimoto
正之 藤本
Toshiya Okano
俊也 岡野
Hideki Tani
英樹 谷
Kazuya Imai
和哉 今井
Yasushi Sano
易司 佐野
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.)
Takagi Industrial Co Ltd
Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Original Assignee
Takagi Industrial Co Ltd
Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takagi Industrial Co Ltd, Osaka Gas Co Ltd, Tokyo Gas Co Ltd filed Critical Takagi Industrial Co Ltd
Priority to JP6002987A priority Critical patent/JPH07208826A/en
Publication of JPH07208826A publication Critical patent/JPH07208826A/en
Pending 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

Abstract

PURPOSE:To make manufacturing cost, facility cost and construction cost low by reducing in size, simplifying a structure to be adapted for a domestic product, decreasing number of components, and facilitating manufacture and assembling. CONSTITUTION:An evaporating tube 4B is provided at an evaporating tube 4A disposed at a passage 2 for passing indoor air via a bent part 4C, and an absorbent injector 8 from a regenerator 31 is provided at the tube side from the bent part. Thus, the absorbent injected from the injector flows down on an inner surface of the tube to absorb vapor refrigerant at an absorbing tube to be recovered.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は空気調和装置に関し、小
型にして例えば家庭用の吸収式冷凍機、冷房・暖房兼用
機、および冷房専用機として最適であり、蒸発器内に生
ずる液冷媒としての水蒸気を効率よく回収し、運転を行
うものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner, which is suitable for use as an absorption refrigerating machine for home use, a combined cooling / heating machine, and a dedicated cooling machine, for example, as a liquid refrigerant generated in an evaporator. The steam is efficiently collected and operated.

【0002】[0002]

【従来の技術】従来、中型または大型の空調(空気調
和)機には水などの液冷媒を真空下で蒸発させ、この気
化熱による熱交換現象によって循環水を冷却する。そし
てこの循環水を各部屋に循環させて室内機よりファンに
て冷風を送り、冷房を行うものがあった。すなわち図4
に示すように、一端が液冷媒供給管20に接続され、他
端には吸収管21が接続され、10torr程度の真空
状態に内部が維持されて循環水22が流入している蒸発
管23が蛇行して内部に収容された蒸発器1′と、前記
吸収管21が一端に接続されて内部には臭化リチウム濃
溶液Liが収容され、さらに放熱ファン24によって冷
却可能な吸収器5′よりなる臭化リチウム収容タンク2
6と、該臭化リチウム収容タンク26の下端部に接続さ
れるポンプ27を備えた連通管28の他端が一側下端に
接続され、また前記臭化リチウム収容タンク26の一側
上部に挿入可能な有孔の一端29aを有する回収管29
の他端が上部一側に接続され、下面にはバーナ30を加
熱可能に設けた再生器31と、一端が連通管32を介し
て前記再生器31に接続され、他端には前記液冷媒供給
管20が接続されるとともに冷却ファン33により冷却
可能になる凝縮器34とから形成される。
2. Description of the Related Art Conventionally, a medium- or large-sized air conditioner (air conditioner) evaporates a liquid refrigerant such as water under vacuum, and cools circulating water by a heat exchange phenomenon due to the heat of vaporization. Then, there has been a system in which this circulating water is circulated in each room and cool air is sent from an indoor unit by a fan to cool the room. That is, FIG.
As shown in FIG. 1, one end is connected to the liquid refrigerant supply pipe 20, the other end is connected to the absorption pipe 21, and the evaporation pipe 23 in which the circulating water 22 flows in is maintained in a vacuum state of about 10 torr. An evaporator 1'which meanders and is housed inside, and an absorber 5'which is connected to one end of the absorption pipe 21 and contains therein a concentrated solution of lithium bromide Li, and which can be cooled by a radiating fan 24. Lithium bromide storage tank 2
6, and the other end of a communication pipe 28 having a pump 27 connected to the lower end of the lithium bromide storage tank 26 is connected to the lower end on one side, and is inserted in the upper part of the one side of the lithium bromide storage tank 26. Recovery pipe 29 with one perforated end 29a possible
The other end of which is connected to one side of the upper part, a lower surface of which is provided with a regenerator 31 that is capable of heating the burner 30, and one end of which is connected to the regenerator 31 through a communication pipe 32, and the other end of which is the liquid refrigerant. It is formed of a condenser 34 to which the supply pipe 20 is connected and which can be cooled by a cooling fan 33.

【0003】そして循環水22が流入し、蒸発器1′内
に蛇行している蒸発管23の表面に液冷媒供給管20か
ら液冷媒3としての水を滴下すると、蒸発管23の表面
に拡散された液冷媒3は蒸発してその気化熱によって蒸
発管23内に流入している循環水22を冷却する。そし
て、蒸発器1′内に蒸気冷媒Aが充満して来るので、臭
化リチウム収容タンク26内に収容されている臭化リチ
ウム濃溶液Li により吸収器5′内で充満している蒸気
冷媒Aが吸収される。そして蒸気冷媒Aを吸収した臭化
リチウム希溶液Li′をポンプ27にて再生器31に送
出する。
When the circulating water 22 flows in and the water as the liquid refrigerant 3 is dropped from the liquid refrigerant supply pipe 20 onto the surface of the evaporation pipe 23 meandering in the evaporator 1 ', it diffuses on the surface of the evaporation pipe 23. The liquid refrigerant 3 thus evaporated evaporates and cools the circulating water 22 flowing into the evaporation pipe 23 by its heat of vaporization. Then, since the vapor refrigerant A is filled in the evaporator 1 ', the vapor refrigerant A filled in the absorber 5'by the concentrated lithium bromide solution Li stored in the lithium bromide storage tank 26. Is absorbed. Then, the lithium bromide dilute solution Li ′ having absorbed the vapor refrigerant A is sent to the regenerator 31 by the pump 27.

【0004】この再生器31において臭化リチウム希溶
液Li′はバーナ30による加熱により濃縮されて臭化
リチウム濃溶液Liと蒸気冷媒Aとは分離され、その後
蒸気冷媒Aは再生器31から連通管32を介して凝縮器
34にて冷却ファン33により冷却され、液冷媒供給管
20を通じて蒸発器1′内へ再び送り込まれる。しかも
再生器31から回収される臭化リチウム濃溶液Liは回
収管29を通じて有孔の一端29aから臭化リチウム収
容タンク26内に散布されて回収される。そして液冷媒
3が滴下されることにより冷却され、前記蒸発器1′内
に配列された複数の蒸発管23内に流入されている循環
水22は各部屋内に供給され、循環することにより冷房
として使用に供する。
In the regenerator 31, the diluted lithium bromide solution Li 'is concentrated by heating by the burner 30 to separate the concentrated lithium bromide solution Li and the vapor refrigerant A, and then the vapor refrigerant A is connected from the regenerator 31 to a communication pipe. After being cooled by the cooling fan 33 in the condenser 34 via the condenser 32, it is fed again into the evaporator 1 ′ through the liquid refrigerant supply pipe 20. Moreover, the concentrated lithium bromide solution Li recovered from the regenerator 31 is dispersed through the recovery pipe 29 from the one end 29a having the hole into the lithium bromide accommodation tank 26 and recovered. Then, the liquid refrigerant 3 is dropped to cool the water, and the circulating water 22 flowing into the plurality of evaporation pipes 23 arranged in the evaporator 1'is supplied to each room and circulates to cool the room. To use as.

【0005】また空気調和装置の他の従来例として室内
空気が通る通路内に蒸発器を位置させ、室内空気を直
接、冷却し、その冷気をダクトを通して室内に送風し、
冷却を行う方式があった。
Further, as another conventional example of an air conditioner, an evaporator is positioned in a passage through which indoor air passes, the indoor air is directly cooled, and the cold air is blown into the room through a duct.
There was a method of cooling.

【0006】しかも家庭用もしくはその近辺容量の吸収
式冷凍機用の吸収器の改良として例えば図5に示すもの
がある。すなわち吸収器Tは、上下方向に多数、設けた
フィンaと、これらのフィンaとに接触して設けられた
伝熱管bとで構成され、この伝熱管bには吸収液を導く
導入孔cを設け、該伝熱管bに前記導入孔cと連通する
環状溝dが外周壁に形成され且つ環状溝dと連通する複
数の分散孔eが下壁に形成された液分散管fを設けた構
成である。gは冷媒蒸気導入管である。
Further, as an improvement of the absorber for home use or for an absorption refrigerator having a capacity in the vicinity thereof, there is, for example, one shown in FIG. That is, the absorber T is composed of a large number of fins a provided in the vertical direction and a heat transfer tube b provided in contact with these fins a, and an introduction hole c for guiding the absorbing liquid to the heat transfer tube b. The heat transfer tube b is provided with a liquid dispersion tube f having an annular groove d communicating with the introduction hole c formed on the outer peripheral wall and a plurality of dispersion holes e communicating with the annular groove d formed on the lower wall. It is a composition. g is a refrigerant vapor introduction pipe.

【0007】そして吸収液は、導入孔cより入り、吸収
器Tの伝熱管bと、液分散管fとの間の空間を通って分
散孔eより分散される。この導入孔cから分散孔eまで
は半密閉構造で、且つ容積的には大変小さいので、供給
された吸収液は液量の大小にかかわらず、複数の分散孔
eから均等に噴出させ、蒸気冷媒を効率良く、吸収する
ものである。
The absorbing liquid enters through the introduction hole c, passes through the space between the heat transfer pipe b of the absorber T and the liquid dispersion pipe f, and is dispersed through the dispersion hole e. Since the introduction hole c to the dispersion hole e has a semi-closed structure and is very small in volume, the supplied absorption liquid is uniformly ejected from the plurality of dispersion holes e regardless of the amount of liquid, and vapor is generated. It efficiently absorbs the refrigerant.

【0008】[0008]

【発明が解決しようとする課題】しかしながら図4に示
す上記従来の冷房用の空気調和装置は、業務用の大型製
品を対象としたものであり、蒸発器および蒸気冷媒を回
収するのに吸収液を散布するための構造が、大型化する
原因になっていた。しかも循環水を使用することから配
管が複雑になり、製作および組立が容易には行なえなか
った。
However, the conventional air conditioner for cooling shown in FIG. 4 is intended for a large-scale product for business use, and the absorbing liquid is used for recovering the evaporator and the vapor refrigerant. The structure for spraying was a cause of increasing the size. Moreover, since the circulating water is used, the piping becomes complicated, and the manufacture and assembly cannot be performed easily.

【0009】また臭化リチウムを吸収液として使用する
場合、吸収器での吸収液温度を40度前後に保つ必要が
あるので、通常、戸外に冷却筒を用いて蒸気冷媒を冷さ
なければならなかった。従って設備が大型になるととも
に配管等にも長い距離と多くの時間および手間がかか
り、家庭用あるいは小規模住宅用の冷房機等の空気調和
機として採用するには不利である。また室内機と室外機
とは、冷熱媒循環用の配管で結ぶ必要があるから、工事
費、設備費が高額になっていた。
When lithium bromide is used as the absorbing liquid, the temperature of the absorbing liquid in the absorber needs to be maintained at around 40 ° C. Therefore, it is usually necessary to cool the vapor refrigerant by using a cooling cylinder outside. There wasn't. Therefore, the equipment becomes large, and the piping and the like take a long distance and a lot of time and labor, which is disadvantageous to be adopted as an air conditioner such as an air conditioner for a home or a small-scale house. Further, since it is necessary to connect the indoor unit and the outdoor unit with a pipe for circulating the cooling / heating medium, the construction cost and the equipment cost are high.

【0010】そこで本発明は、設備が小型化されて簡素
化が達成され、配管等も最小限で時間および手間がかか
らず、しかも製作コスト、工事費、設備費は廉価であ
り、家庭用あるいは小規模住宅用に適した空気調和装置
を提供することを目的とする。
In view of the above, according to the present invention, the equipment is reduced in size and simplification is achieved, the piping and the like are minimized, and the time and effort are minimized, and the manufacturing cost, construction cost, and equipment cost are low, and it is for household use. Another object is to provide an air conditioner suitable for small-scale homes.

【0011】[0011]

【課題を解決するための手段】本発明は上記課題に鑑み
なされたものであり、蒸発管部内に液冷媒を流下するこ
とにより蒸発がなされ、室内外に通気可能な通路に位置
して設けた蒸発器と、前記液冷媒を回収可能に設けた吸
収器と、冷媒を含む吸収液を再生可能に設けた再生器と
を備え、前記蒸発管部は、吸収管部に対して屈曲部を介
して傾斜して設けられ、該屈曲部より前記蒸発管部側に
再生器からの吸収液の注入部を設け、該注入部は注入す
る吸収液が管内面に流下される位置に設けられるという
手段を採用した。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and is provided at a passage where air is vaporized by flowing a liquid refrigerant into an evaporation pipe portion and can be ventilated indoors or outdoors. An evaporator, an absorber capable of recovering the liquid refrigerant, and a regenerator capable of regenerating the absorbing liquid containing the refrigerant are provided, and the evaporation pipe portion is provided with a bent portion with respect to the absorption pipe portion. A means for injecting the absorption liquid from the regenerator on the side of the evaporation pipe with respect to the bent portion, and the injection portion is provided at a position where the absorption liquid to be injected flows down to the inner surface of the pipe. It was adopted.

【0012】[0012]

【作用】液冷媒を滴下して冷媒を蒸発させる時の気化熱
により冷却される蒸発管部を液冷媒の吸収管部に対して
屈曲部を介して傾斜して室内外に通気可能な通路内に設
けることにより、蒸発器と吸収器とをまとめて設置スペ
ースを小型化する。そして吸収液としての臭化リチウム
濃溶液は前記屈曲部より蒸発管部側に設けた注入部から
管内面を流下し、蒸気冷媒を吸収する。
In the passage in which the evaporation pipe portion cooled by the heat of vaporization when the liquid refrigerant is dropped to evaporate the refrigerant is inclined with respect to the absorption pipe portion of the liquid refrigerant through the bent portion to allow indoor / outdoor ventilation. The installation space can be reduced by collectively installing the evaporator and the absorber. Then, the concentrated lithium bromide solution as the absorbing liquid flows down the inner surface of the pipe from the injection portion provided on the side of the evaporation pipe portion with respect to the bent portion, and absorbs the vapor refrigerant.

【0013】[0013]

【実施例】以下図1乃至図4に従って本発明の一実施例
の詳細を説明する。本実施例において図4に示す部分と
同一部分は同一符号で示すものとし、冷房・暖房兼用の
空気調和装置として適用した場合につき説明する。1は
蒸発器であり、この蒸発器1は室内Nと室外N′とに通
気可能な吸気通路2と排気通路3との接合部に位置して
設けられ、蒸発管部4A内に液冷媒5を滴下機構部6に
より滴下して液冷媒5を真空状態にて蒸発し、その気化
熱により室R内を冷却する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of one embodiment of the present invention will be described below with reference to FIGS. In this embodiment, the same parts as those shown in FIG. 4 are designated by the same reference numerals, and the case of application as an air conditioner for both cooling and heating will be described. Reference numeral 1 denotes an evaporator. The evaporator 1 is provided at a joint portion between an intake passage 2 and an exhaust passage 3 which can ventilate the inside N and the outside N ', and a liquid refrigerant 5 is provided in an evaporation pipe portion 4A. Is dropped by the dropping mechanism unit 6 to evaporate the liquid refrigerant 5 in a vacuum state, and the inside of the chamber R is cooled by the heat of vaporization.

【0014】7は吸収器であり、この吸収器7は前記液
冷媒5を吸収管部4B内で回収するためのものである。
Reference numeral 7 is an absorber, and this absorber 7 is for collecting the liquid refrigerant 5 in the absorption pipe portion 4B.

【0015】前記滴下機構部6は、図4に示すように液
冷媒5を吸収した臭化リチウム希溶液Li ′を再び臭化
リチウム濃溶液Li に濃縮するために吸収器7に接続さ
れ、バーナ30を備えた再生器31と、該再生器31に
接続されて冷却を行う冷却ファン33を備えた凝縮器3
4とよりなる従来の循環再生形式の装置を使用しても良
く、この場合には資源の再利用が容易に行える。
As shown in FIG. 4, the dropping mechanism portion 6 is connected to the absorber 7 for concentrating the diluted lithium bromide solution Li 'which has absorbed the liquid refrigerant 5 into the concentrated lithium bromide solution Li again, and the burner 7 is used. A condenser 3 including a regenerator 31 including 30 and a cooling fan 33 connected to the regenerator 31 for cooling.
It is also possible to use a conventional circulating regeneration type apparatus consisting of 4 and in this case, the resource can be easily reused.

【0016】前記蒸発管部4Aは前記吸収管部4Bに対
して屈曲部4Cを介して傾斜して設けられ、この蒸発管
部4Aと吸収管部4Bとは1本の金属性パイプ、好まし
くは銅パイプ、ステンレスパイプ、アルミパイプを図1
乃至図3に示すように略く字形に折り曲げることにより
形成される。この蒸発管部4Aの長さL1 は本実施例に
おいては好ましくは略360mm程であり、また吸収管
部4Bの長さL2 は好ましくは略500mm程度であ
る。そして前記吸収管部4Bに対する蒸発管部4Aの折
り曲げ角度θは最適には140°程度である。
The evaporation pipe portion 4A is provided so as to be inclined with respect to the absorption pipe portion 4B via a bent portion 4C, and the evaporation pipe portion 4A and the absorption pipe portion 4B are one metallic pipe, preferably. Figure 1 shows copper pipe, stainless steel pipe, and aluminum pipe.
It is formed by bending it into a substantially V shape as shown in FIG. In this embodiment, the length L 1 of the evaporation pipe portion 4A is preferably about 360 mm, and the length L 2 of the absorption pipe portion 4B is preferably about 500 mm. The optimum bending angle θ of the evaporation tube portion 4A with respect to the absorption tube portion 4B is about 140 °.

【0017】8は前記蒸発管部4Aの外周に多数、好ま
しくは320枚ほど、適宜の間隔をあけて取付けられた
フィンであり、このフィン8は好ましくはその長さが3
2mm程度であり、蒸発管部4Aの外周方向に設けた送
風ファン9からの送風と相まって効率よく、放熱を行
い、蒸発管部4Aを冷却する。この際、フィン8の長さ
を加減し、フィン8相互の上下方向の設置間隔を加減す
ることにより放熱状態を調整することができる。
A large number of fins 8, preferably about 320, are attached to the outer circumference of the evaporation pipe portion 4A at appropriate intervals, and the fins 8 preferably have a length of 3 pieces.
The length is about 2 mm, and in combination with the air blow from the air blower fan 9 provided in the outer peripheral direction of the evaporation pipe portion 4A, heat is efficiently radiated and the evaporation pipe portion 4A is cooled. At this time, the heat dissipation state can be adjusted by adjusting the length of the fins 8 and adjusting the vertical installation interval between the fins 8.

【0018】8′は前記吸収管部4Bの外周に多数、好
ましくは360枚ほど、適宜の間隔をあけて取付けられ
たフィンであり、このフィン8′は好ましくはその長さ
が32mm程度であり、吸収管部4Bの外周方向に設け
た送風ファン9′からの送風と相まって効率よく放熱を
行い、吸収管部4Bを冷却する。
A large number of fins 8'are attached to the outer circumference of the absorption tube portion 4B, preferably about 360 sheets, at appropriate intervals, and the fins 8'are preferably about 32 mm in length. The heat is efficiently dissipated in combination with the air blown from the blower fan 9'provided in the outer peripheral direction of the absorption tube portion 4B to cool the absorption tube portion 4B.

【0019】10は前記屈曲部4Cより前記蒸発管部4
A側に再生器31からの吸収液としての臭化リチウム濃
溶液Liを注入するための注入部であり、この注入部1
0は注入される臭化リチウム濃溶液Liが屈曲部4Cと
吸収管部4Bとの管内面を流下する位置、好ましくは臭
化リチウム濃溶液Liが管の反対内面に直接、滴下され
る位置に設けられるが、勿論注入部10を屈曲部4Cの
側面に設けることによって蒸発管部4Aの管内面に臭化
リチウム濃溶液Liが流下する位置に設けてもよい。
Reference numeral 10 indicates the evaporation pipe portion 4 from the bent portion 4C.
It is an injection part for injecting a concentrated solution of lithium bromide Li from the regenerator 31 into the A side.
0 is the position where the injected lithium bromide concentrated solution Li flows down the inner surface of the bent portion 4C and the absorption tube portion 4B, preferably the position where the lithium bromide concentrated solution Li is dropped directly on the inner surface opposite to the tube. Although it is provided, of course, the injection part 10 may be provided at a position where the concentrated lithium bromide solution Li flows down to the inner surface of the evaporation tube portion 4A by providing the injection portion 10 on the side surface of the bent portion 4C.

【0020】11は前記注入部10より下方に位置する
吸収管部4B側の管内部に介装されるコイルばねであ
り、このコイルばね11は耐食性があり、加工が容易な
材料、例えばステンレス鋼材製であり、注入部10から
注入される臭化リチウム濃溶液Liはコイルばね11に
て攪拌されて隅々まで平均的に管内に行き渡って流下さ
れ、効率良く液冷媒を吸収する。コイルばね11の直径
はこの実施例においては1mmほどである。また蒸発器
1の蒸発管部4A内に滴下されて蒸発する冷媒は、屈曲
部4Cを経て吸収管部4Bに流下されて来るが、前記コ
イルばね11の攪拌により臭化リチウム濃溶液Liとな
じみあって吸収され、臭化リチウム収容タンク26内に
流下される。
Reference numeral 11 denotes a coil spring disposed below the injection portion 10 inside the tube on the side of the absorption tube portion 4B. The coil spring 11 has corrosion resistance and is easy to machine, for example, stainless steel material. The lithium bromide concentrated solution Li injected from the injection part 10 is agitated by the coil spring 11 and evenly flows down to every corner of the tube, and efficiently absorbs the liquid refrigerant. The diameter of the coil spring 11 is about 1 mm in this embodiment. Further, the refrigerant that has dropped into the evaporation pipe portion 4A of the evaporator 1 and evaporates flows down to the absorption pipe portion 4B through the bent portion 4C, but is agitated by the coil spring 11 and becomes familiar with the lithium bromide concentrated solution Li. It is absorbed and is flowed down into the lithium bromide storage tank 26.

【0021】12は前記吸気通路2と排気通路3との接
合部に位置して設けられたケースであり、このケース1
2内には前記送風ファン9と、蒸発器1と、後記冷房・
暖房兼用の熱交換器13が収納され、上方一側には冷気
又は暖気が吹き出して各室内に分配するための吹出口1
2aが設けられている。
Reference numeral 12 is a case provided at the joint between the intake passage 2 and the exhaust passage 3, and this case 1
The blower fan 9, the evaporator 1, and the cooling and
A heat exchanger 13 that also serves as a heating is accommodated, and an outlet 1 for discharging cool air or warm air to the upper one side to distribute it to each room.
2a is provided.

【0022】13は冷房・暖房兼用の熱交換器であり、
この熱交換器13は前記ケース12内において前記蒸発
器1に隣接して前記送風ファン9の後段に位置して設け
られる。そしてこの熱交換器13は前記再生器31に往
路と復路としての液冷媒供給管20a,20bにより連
結されることにより、液冷媒(水蒸気)が供給され、暖
気を排気通路3から室内Nへ吹き出して暖房用として使
用する。
Reference numeral 13 is a heat exchanger for both cooling and heating,
The heat exchanger 13 is provided in the case 12 adjacent to the evaporator 1 and at a subsequent stage of the blower fan 9. The heat exchanger 13 is connected to the regenerator 31 by liquid refrigerant supply pipes 20a and 20b serving as an outward path and a return path, so that the liquid refrigerant (water vapor) is supplied and warm air is blown from the exhaust passage 3 into the room N. Used for heating.

【0023】また熱交換器13は、前記液冷媒供給管2
0aから分岐したバルブVを有する液冷媒供給管20c
と液冷媒供給管20dを介して再生器31からの液冷媒
5を液冷媒供給管20c、凝縮器34、液冷媒供給管2
0dを経て送風ファン9′により冷却した後に、熱交換
器13内に送り、熱交換する。そして冷気を吹出口12
aから室内Nに吹き出すという冷房用として使用され
る。
Further, the heat exchanger 13 includes the liquid refrigerant supply pipe 2
Liquid refrigerant supply pipe 20c having a valve V branched from 0a
Liquid refrigerant 5 from the regenerator 31 via the liquid refrigerant supply pipe 20d and the liquid refrigerant supply pipe 20c, the condenser 34, the liquid refrigerant supply pipe 2
After passing through 0d and cooled by the blower fan 9 ', it is sent into the heat exchanger 13 for heat exchange. And cold air is blown out 12
It is used for cooling by blowing out from a to the room N.

【0024】本発明の一実施例は以上の構成からなり、
先ず本装置を冷房用の空気調和装置として用いる場合に
は、バーナ30を燃焼することにより発生する液冷媒
(水蒸気)を液冷媒供給管20aに対し分枝し、バルブ
Vが開かれた液冷媒供給管20cから凝縮器34に移送
する。その後に、液冷媒供給管20dを通じて滴下機構
部6から蒸発管部4A内に液冷媒5を滴下し、蒸発管部
4Aの内部で液冷媒5を蒸発させ、その気化熱によって
蒸発管部4Aを冷却させる。
An embodiment of the present invention has the above-mentioned structure,
First, when this device is used as an air conditioner for cooling, the liquid refrigerant (water vapor) generated by burning the burner 30 is branched to the liquid refrigerant supply pipe 20a, and the valve V is opened. Transfer from the supply pipe 20c to the condenser 34. After that, the liquid refrigerant 5 is dropped from the dropping mechanism portion 6 into the evaporation pipe portion 4A through the liquid refrigerant supply pipe 20d to evaporate the liquid refrigerant 5 inside the evaporation pipe portion 4A, and the evaporation heat of the evaporation heats the evaporation pipe portion 4A. Allow to cool.

【0025】この蒸発管部4Aの外周部には多数のフィ
ン8が設けられて放熱が行われ、送風ファン9により蒸
発管部4Aが冷やされることにより、蒸発管部4Aの周
囲の冷却風がケース12の上方一側に設けた吹出口12
aから室内機(図に示さず)に供給され、冷房が行われ
る。
A large number of fins 8 are provided on the outer peripheral portion of the evaporation pipe portion 4A to radiate heat, and the blower fan 9 cools the evaporation pipe portion 4A, so that cooling air around the evaporation pipe portion 4A is generated. Air outlet 12 provided on one side above case 12
The air is supplied from a to an indoor unit (not shown in the figure) to perform cooling.

【0026】本装置を暖房機として使用する場合には、
液冷媒供給管20cのバルブVを閉め、再生器31にて
バーナ30を燃焼することにより発生する液冷媒(水蒸
気)を液冷媒供給管20aから熱交換器13へと送り、
再び液冷媒供給管20bを経て再生器31に戻すことに
より、熱交換し、送風ファン9により暖気を排気通路3
から室内Nへ送り、暖房を行う。
When this device is used as a heater,
The valve V of the liquid refrigerant supply pipe 20c is closed, and the liquid refrigerant (water vapor) generated by burning the burner 30 in the regenerator 31 is sent from the liquid refrigerant supply pipe 20a to the heat exchanger 13.
By returning to the regenerator 31 via the liquid refrigerant supply pipe 20b again, heat is exchanged and warm air is blown by the blower fan 9 into the exhaust passage 3
To the room N to heat the room.

【0027】ところで本実施例の蒸発器1と吸収器7と
はその蒸発管部4Aが吸収管部4Bに対して1本の金属
パイプを用いて屈曲部4Cを介して傾斜して設けられて
いるので、蒸発器1と吸収器7との設置スペースがコン
パクトになるのと、蒸発器1と吸収器7とが一纏めにな
るのとから小型化されるとともに構造が簡素化され、部
品点数が少なくなり、製作および組立が容易で家庭用の
空気調和機の蒸気冷媒吸収装置として使用に適する。
By the way, in the evaporator 1 and the absorber 7 of this embodiment, the evaporation pipe portion 4A is provided so as to be inclined with respect to the absorption pipe portion 4B through the bent portion 4C using one metal pipe. Since the installation space between the evaporator 1 and the absorber 7 is compact, and the evaporator 1 and the absorber 7 are integrated, the structure is simplified and the number of parts is reduced. Since it is less and easy to manufacture and assemble, it is suitable for use as a vapor refrigerant absorption device for a home air conditioner.

【0028】また屈曲部4Cより蒸発管部4A側には注
入部10が位置して設けられているので、この注入部1
0にて再生器31から供給されて来る吸収液としての臭
化リチウム濃溶液Liが管内の反対内面に直接、注入さ
れて流下される。そして管内面に流される臭化リチウム
濃溶液Liは管内面を伝ってその下方に位置するコイル
ばね11によって攪拌されることにより管内の隅々まで
平均的に行き渡り、液冷媒5が蒸発することにより蒸発
管部4Aから生ずる蒸気冷媒Aを効率良く吸収する。従
って図4に示すような従来の吸収器7′における臭化リ
チウム濃溶液Liの注入部のように構造が大型にはなら
ずに小型化され且つ複雑にはならずに簡素化され、部品
点数も吸収管部4Bとコイルばね11との2点で足り
る。
Further, since the injection portion 10 is provided on the side of the evaporation pipe portion 4A with respect to the bent portion 4C, the injection portion 1 is provided.
At 0, the concentrated lithium bromide solution Li as an absorbing liquid supplied from the regenerator 31 is directly injected and flows down to the opposite inner surface in the tube. Then, the concentrated lithium bromide solution Li flowing on the inner surface of the tube is spread on the inner surface of the tube and is agitated by the coil springs 11 located below the inner surface of the tube, so that the solution evenly spreads to every corner of the tube and the liquid refrigerant 5 evaporates. The vapor refrigerant A generated from the evaporation pipe portion 4A is efficiently absorbed. Therefore, the structure of the conventional absorber 7 ', such as a lithium bromide concentrated solution Li injection part as shown in FIG. Also, two points, the absorption tube portion 4B and the coil spring 11, are sufficient.

【0029】そして吸収管部4Bの外周にはフィン8′
が設けられているのと、吸収管部4Bの外周には送風フ
ァン9′を設けているので、臭化リチウム濃溶液Li
が、蒸発管部4Aから来る蒸気冷媒Aを吸収管部4Bに
おいて効率的に吸収する時に発生する反応熱は、フィン
8′からの放熱と、送風ファン9′からの送風により冷
却される。
A fin 8'is provided on the outer circumference of the absorption tube portion 4B.
Is provided and a blower fan 9'is provided on the outer circumference of the absorption tube portion 4B, so that the lithium bromide concentrated solution Li is
However, the reaction heat generated when the vapor refrigerant A coming from the evaporation pipe portion 4A is efficiently absorbed in the absorption pipe portion 4B is cooled by the heat radiation from the fins 8'and the air blow from the blower fan 9 '.

【0030】ところで、吸熱管部4Bにおいて蒸気冷媒
Aを吸収した臭化リチウム濃溶液Liは、臭化リチウム
希溶液Li′になって図1および図4に示すような再生
器31に送られる。そして再生器31において臭化リチ
ウム希溶液Li′はバーナ30によって加熱され、濃縮
されることにより、注入部10から吸収管部4B内に再
び吸収液としての臭化リチウム濃溶液Li を注入すると
いう、循環方式を採用すれば、吸収液に液冷媒を吸収す
る都度、廃棄することなく資源の再利用をはかることが
できる。
By the way, the concentrated lithium bromide solution Li which has absorbed the vapor refrigerant A in the endothermic tube portion 4B becomes a diluted lithium bromide solution Li 'and is sent to the regenerator 31 as shown in FIGS. In the regenerator 31, the diluted lithium bromide solution Li 'is heated and concentrated by the burner 30, so that the concentrated lithium bromide solution Li as an absorbing liquid is injected again from the injection part 10 into the absorption tube part 4B. By adopting the circulation system, it is possible to reuse the resource without discarding it each time the absorbing liquid absorbs the liquid refrigerant.

【0031】また蒸気冷媒Aは凝縮器34に送られ、冷
却ファン9′によって冷却された後に蒸発器1に送ら
れ、前述のような滴下機構部6から蒸発器1内に流下す
れば、液冷媒5の再使用が行え、資源の再利用をはかる
ことができる。
Further, the vapor refrigerant A is sent to the condenser 34, cooled by the cooling fan 9 ', and then sent to the evaporator 1, and if it flows down from the dropping mechanism section 6 into the evaporator 1, the liquid refrigerant A is discharged. The refrigerant 5 can be reused and resources can be reused.

【0032】なお上記実施例において室内空気が通る吸
気通路2内に位置して設けた蒸発器1に隣接する熱交換
器13は、冷房・暖房兼用の熱交換器13を使用し、バ
ルブVを切換えることにより、冷房および暖房の両方に
兼用できる空気調和装置として説明したが、熱交換器1
3は冷房機専用として使用することもできる。
In the above embodiment, the heat exchanger 13 adjacent to the evaporator 1 provided in the intake passage 2 through which indoor air passes uses the heat exchanger 13 for both cooling and heating, and the valve V is used. Although it has been described as an air conditioner that can be used for both cooling and heating by switching, the heat exchanger 1
3 can also be used exclusively for the air conditioner.

【0033】また上記実施例においてはコイルばね11
を、吸収管部4Bに対して傾斜して設けた蒸発管部4A
との間の屈曲部4Cより蒸発管部4A側の管内に介装す
ることにより、注入部10から注入する吸収液としての
臭化リチウム濃溶液Liを攪拌可能になしているが、コ
イルばね11を管内に介装しなくても、コイルばね11
に代わる螺旋溝を管内に形成することによっても注入部
10から注入される吸収液は螺旋溝により均一に攪拌さ
れて蒸気冷媒Aを効率良く吸収できることはいうまでも
ない。
In the above embodiment, the coil spring 11 is used.
Of the evaporation pipe portion 4A, which is inclined with respect to the absorption pipe portion 4B.
The lithium bromide concentrated solution Li as the absorbing liquid to be injected from the injection part 10 can be agitated by interposing it in the tube on the side of the evaporation tube part 4A from the bent part 4C between the coil spring 11 and Even if the pipe is not inserted in the pipe, the coil spring 11
It is needless to say that the absorption liquid injected from the injection portion 10 can be uniformly stirred by the spiral groove and the vapor refrigerant A can be efficiently absorbed also by forming the spiral groove instead of the above in the pipe.

【0034】また上記実施例においては蒸発管部4Aを
屈曲部4Cを介して吸収管部4Bと一体に形成している
が、これに限ることなく、別個に形成した蒸発管部4A
と吸収管部4Bとをエルボ等の接続部品を介して接続す
るようにしたものでもよい。また上記説明では蒸気冷媒
を回収するのに吸収液を散布するための機構は、家庭用
の冷房機、冷房・暖房兼用機として説明したがこのほ
か、家庭用の吸収式冷凍機としても使用することができ
る。
In the above embodiment, the evaporation pipe portion 4A is formed integrally with the absorption pipe portion 4B via the bent portion 4C, but the invention is not limited to this, and the evaporation pipe portion 4A is formed separately.
The absorption tube portion 4B may be connected to the absorption tube portion 4B via a connecting component such as an elbow. Further, in the above description, the mechanism for spraying the absorbing liquid to recover the vapor refrigerant has been described as a domestic air conditioner and a combined cooling / heating machine, but it is also used as a domestic absorption type refrigerator. be able to.

【0035】[0035]

【発明の効果】以上のように本発明は、室内空気が通る
通路内に位置して設けた蒸発器の蒸発管部に対して吸収
器の吸収管部を屈曲部を介して傾斜して設けたので、設
置スペースを採らずに小型化が達成されて効率良く、蒸
気冷媒を回収でき、家庭用の小規模製品に適する。しか
も構造が簡素化できるとともに配管も容易になり、部品
点数を少なくできるので、製作および組立が容易になる
とともに製作コストは安価になり、工事費、設備費は廉
価になる。
As described above, according to the present invention, the absorption pipe portion of the absorber is provided to be inclined with respect to the evaporation pipe portion of the evaporator provided in the passage through which the indoor air passes through the bent portion. Therefore, downsizing can be achieved without taking up the installation space, the vapor refrigerant can be recovered efficiently, and it is suitable for small household products. Moreover, since the structure can be simplified, piping can be facilitated, and the number of parts can be reduced, manufacturing and assembling can be facilitated, manufacturing cost can be reduced, and construction cost and facility cost can be reduced.

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

【図1】図1は本発明の一実施例を示す断面図である。FIG. 1 is a sectional view showing an embodiment of the present invention.

【図2】同じく要部の拡大断面図である。FIG. 2 is likewise an enlarged cross-sectional view of a main part.

【図3】同じく説明的に示した拡大断面図である。FIG. 3 is an enlarged cross-sectional view which is also illustratively shown.

【図4】従来のこの種空気調和機の蒸気冷媒吸収装置の
一例を示す断面図である。
FIG. 4 is a cross-sectional view showing an example of a conventional vapor refrigerant absorption device for an air conditioner of this type.

【図5】従来のこの種家庭用もしくはその近辺容量の吸
収式冷凍機用の吸収器の一例を示す断面図である。
FIG. 5 is a cross-sectional view showing an example of a conventional absorber for a home of this type or an absorption refrigerator having a capacity in the vicinity thereof.

【符号の説明】[Explanation of symbols]

1 蒸発器 2 吸気通路 3 排気通路 4A 蒸発管部 4B 吸収管部 4C 屈曲部 5 液冷媒 6 滴下機構部 7 吸収器 10 注入部 11 コイルばね 12 ケース 13 熱交換器 30 バーナ 31 再生器 34 凝縮器 A 蒸気冷媒 Li 臭化リチウム濃溶液 N 室内 N′ 室外 1 Evaporator 2 Intake passage 3 Exhaust passage 4A Evaporation pipe part 4B Absorption pipe part 4C Bent part 5 Liquid refrigerant 6 Dropping mechanism part 7 Absorber 10 Injection part 11 Coil spring 12 Case 13 Heat exchanger 30 Burner 31 Regenerator 34 Condenser A vapor refrigerant Li concentrated lithium bromide solution N indoors N'outdoors

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F25B 37/00 39/02 R F28F 1/24 (72)発明者 岡野 俊也 神奈川県横浜市中区千代崎町四丁目94番 (72)発明者 谷 英樹 大阪市中央区平野町四丁目1番2号 大阪 瓦斯株式会社内 (72)発明者 今井 和哉 大阪市中央区平野町四丁目1番2号 大阪 瓦斯株式会社内 (72)発明者 佐野 易司 静岡県富士市西柏原新田201番地 高木産 業株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Reference number within the agency FI Technical indication location F25B 37/00 39/02 R F28F 1/24 (72) Inventor Toshiya Okano Naka-ku, Yokohama-shi, Kanagawa 4-94, Chiyosaki-cho (72) Hideki Tani, 4-1-2, Hirano-cho, Chuo-ku, Osaka City, Osaka Gas Co., Ltd. (72) Kazuya Imai 4-1-2, Hirano-cho, Chuo-ku, Osaka Gas Co., Ltd. (72) Inventor, Yuji Sano, 201 Shida, Nishi-Kashiwabara, Fuji City, Shizuoka Prefecture Takagi Industrial Co., Ltd.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 蒸発管部内に液冷媒を流下することによ
り蒸発がなされ、室内外に通気可能な通路に位置して設
けた蒸発器と、前記液冷媒を回収可能に設けた吸収器
と、冷媒を含む吸収液を再生可能に設けた再生器とを備
え、前記蒸発管部は、吸収管部に対して屈曲部を介して
傾斜して設けられ、該屈曲部より前記蒸発管部側に再生
器からの吸収液の注入部を設け、該注入部は注入する吸
収液が管内面に流下される位置に設けられたことを特徴
とする空気調和装置。
1. An evaporator provided in a passage through which the liquid refrigerant is evaporated by flowing down the liquid refrigerant in the evaporation pipe portion and which can be ventilated indoors and outdoors; and an absorber provided to collect the liquid refrigerant. And a regenerator that is capable of regenerating an absorbent containing a refrigerant, wherein the evaporation pipe portion is provided inclined with respect to the absorption pipe portion via a bent portion, and the evaporation pipe portion is closer to the evaporation pipe portion side than the bent portion. An air conditioner characterized by being provided with an injection portion for absorbing liquid from the regenerator, and the injection portion being provided at a position where the absorption liquid to be injected flows down to the inner surface of the pipe.
【請求項2】 前記注入部から注入される吸収液が攪拌
可能なコイルばねを前記注入部より下方に位置する吸収
管部側の管内に介装したことを特徴とする請求項1に記
載の空気調和装置。
2. A coil spring capable of agitating the absorbing liquid injected from the injection part is provided in a pipe on the absorption pipe part side located below the injection part. Air conditioner.
【請求項3】 前記注入部から注入される吸収液が攪拌
可能な螺旋溝を前記注入部より下方に位置する吸収管部
側の管内に設けたことを特徴とする請求項1に記載の空
気調和装置。
3. The air according to claim 1, wherein a spiral groove in which the absorption liquid injected from the injection part can be agitated is provided in a pipe on the absorption pipe part side located below the injection part. Harmony device.
【請求項4】 前記蒸発管部は、冷房用の供給通路と暖
房用の供給通路とに凝縮器にて生成される液冷媒を切換
可能に供給することにより室内へ冷気または暖気を送風
可能になす冷房・暖房兼用の熱交換器として設けたこと
を特徴とする請求項1に記載の空気調和装置。
4. The evaporation pipe section is capable of blowing cold air or warm air into a room by switchingably supplying a liquid refrigerant generated by a condenser to a cooling supply passage and a heating supply passage. The air conditioner according to claim 1, wherein the air conditioner is provided as a heat exchanger for both eggplant cooling and heating.
【請求項5】 前記蒸発管部は、前記凝縮器にて生成さ
れる液冷媒が供給されることにより室内へ冷気を送風可
能になす冷房用の熱交換器として設けたことを特徴とす
る請求項1に記載の空気調和装置。
5. The evaporation pipe section is provided as a heat exchanger for cooling, which is capable of blowing cool air into a room by being supplied with a liquid refrigerant generated in the condenser. Item 2. The air conditioner according to Item 1.
JP6002987A 1994-01-17 1994-01-17 Air conditioner Pending JPH07208826A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6002987A JPH07208826A (en) 1994-01-17 1994-01-17 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6002987A JPH07208826A (en) 1994-01-17 1994-01-17 Air conditioner

Publications (1)

Publication Number Publication Date
JPH07208826A true JPH07208826A (en) 1995-08-11

Family

ID=11544735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6002987A Pending JPH07208826A (en) 1994-01-17 1994-01-17 Air conditioner

Country Status (1)

Country Link
JP (1) JPH07208826A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0899521A2 (en) 1997-08-29 1999-03-03 Honda Giken Kogyo Kabushiki Kaisha Absorption refrigerator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6009721A (en) * 1997-04-29 2000-01-04 Honda Giken Kogyo Kabushiki Kaisha Absorption refrigerator
EP0899521A2 (en) 1997-08-29 1999-03-03 Honda Giken Kogyo Kabushiki Kaisha Absorption refrigerator

Similar Documents

Publication Publication Date Title
US6216483B1 (en) Liquid desiccant air conditioner
US20010013226A1 (en) Liquid desiccant air conditioner
CN105744802A (en) Radiant air conditioning system for heating equipment
CN205783400U (en) The radiating subassembly of air-conditioner outdoor unit and air-conditioner outdoor unit
US5916258A (en) GAX aqua absorption type heat pump
US5802866A (en) Air-cooled absorption-type air conditioning apparatus
JPH07208826A (en) Air conditioner
JP3539151B2 (en) Cooling system
JP2001358488A (en) Cooler for facility
JPH01263491A (en) Heat exchanger using heat pipe
JP3145215B2 (en) Evaporation and absorption device in absorption refrigerator
JP2000105087A (en) Cooler
CN213300259U (en) Humidification device and air conditioning system
KR100512041B1 (en) Heat exchanger for air conditioner
KR0115194Y1 (en) Condensing apparatus for absorption type airconditioner
JP2001082824A (en) Absorption refrigerating machine
JP3330845B2 (en) cooling tower
JPH02192547A (en) Absorptive type cooler
JPS61167429A (en) Regenerating method of liquid moisture-absorbent in air-conditioning equipment
KR970009809B1 (en) Double effect absorption cooling/heating apparatus using air cooling absorber
JP2906843B2 (en) Absorption refrigerator
JP2004205155A (en) Heating element cooling system
JP2015503077A (en) Temperature control module
KR19980059862A (en) Absorption HVAC
JP2000055498A (en) Absorption type heat pump

Legal Events

Date Code Title Description
A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20030611