JPH0473059B2 - - Google Patents
Info
- Publication number
- JPH0473059B2 JPH0473059B2 JP27374784A JP27374784A JPH0473059B2 JP H0473059 B2 JPH0473059 B2 JP H0473059B2 JP 27374784 A JP27374784 A JP 27374784A JP 27374784 A JP27374784 A JP 27374784A JP H0473059 B2 JPH0473059 B2 JP H0473059B2
- Authority
- JP
- Japan
- Prior art keywords
- evaporator
- absorber
- generator
- refrigerant passage
- condenser
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 38
- 239000006096 absorbing agent Substances 0.000 claims description 29
- 238000010521 absorption reaction Methods 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 15
- 239000006185 dispersion Substances 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 5
- 230000009467 reduction Effects 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 238000005192 partition Methods 0.000 description 6
- 238000009413 insulation Methods 0.000 description 5
- 238000010276 construction Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は発生器、凝縮器、蒸発器、吸収器及び
吸収液系路、冷媒系路を備えた吸収冷凍機の構造
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to the structure of an absorption refrigerator that includes a generator, a condenser, an evaporator, an absorber, an absorption liquid line, and a refrigerant line.
従来のこの種の冷凍機の構造の一例を第2図に
示す。図示の如き吸収冷凍機は、吸収器2及び蒸
発器1が左右に配置されている構造で、かつ発生
器4及び凝縮器3を別缶胴内に収容する構造とな
つている。
An example of the structure of a conventional refrigerator of this type is shown in FIG. The absorption refrigerator shown in the figure has a structure in which an absorber 2 and an evaporator 1 are arranged on the left and right sides, and a generator 4 and a condenser 3 are housed in a separate can body.
また、上記の第2図に示す如き従来例の、後述
する問題点を改良するものとして、第3図に示す
如き従来例が見られる。 Further, a conventional example as shown in FIG. 3 can be seen as an improvement on the problems described later in the conventional example shown in FIG. 2 described above.
即ち、第3図のものにおいては、蒸発器1、吸
収器2を上下配置とし、凝縮器3と発生器4を丸
缶胴内に併せ収容した構造であり、上から凝縮器
3、発生器4、蒸発器1、吸収器2の順に並べら
れている。 That is, in the one shown in Fig. 3, the evaporator 1 and absorber 2 are arranged one above the other, and the condenser 3 and generator 4 are housed together in the round can body. 4, evaporator 1, and absorber 2 are arranged in this order.
しかしながら、上記の如き従来のものにおいて
は次の如き問題点がある。
However, the conventional devices as described above have the following problems.
即ち、第2図の如き従来例においては、
外形幅寸法を小さくしようとすれば、吸収器
2管束縦列数を多くせざるを得ない。吸収器2
管束は溶液散布方式でチユーブ漏れ面を形成
し、溶液は上部管列から下部管列へと蒸発器1
からの冷媒蒸気を吸収しながら滴下する為、チ
ユーブ列数が多い場合には下部管束のチユーブ
にまで至つた溶液は既に飽和して殆ど吸収能力
が保持できず有効度が薄い為、下部管束に無駄
が生じる。 That is, in the conventional example shown in FIG. 2, if the outer width dimension is to be reduced, the number of columns of two absorber tube bundles must be increased. Absorber 2
The tube bundle forms a tube leakage surface using a solution dispersion method, and the solution flows from the upper tube row to the lower tube row in the evaporator 1.
Since the solution drips while absorbing the refrigerant vapor from the lower tube bundle, if there are many tube rows, the solution that reaches the tubes in the lower tube bundle is already saturated and cannot retain much absorption capacity, making it less effective. There will be waste.
一方列数を減少させて、幅方向のチユーブ本
数を増やそうとすると缶胴の幅寸法が大きくな
る。 On the other hand, if an attempt is made to increase the number of tubes in the width direction by decreasing the number of rows, the width dimension of the can body increases.
吸収器2管束と蒸発器1管束とが左右に配置
されているので、吸収器2管束上への溶液散布
飛沫が蒸発器1側へ入り込む可能性があり、こ
の為、吸収器2と蒸発器1との境界部には、蒸
発器1側からの冷媒液飛沫同伴に加えて、吸収
器側からの溶液飛沫移行を防止するための液滴
分離を両方向に対して配慮する必要が生じ、液
滴分離器の構造が複雑となり、寸法が大きくな
る。 Since the absorber 2 tube bundle and the evaporator 1 tube bundle are arranged on the left and right, there is a possibility that solution spray droplets on the absorber 2 tube bundle will enter the evaporator 1 side. In addition to the entrainment of refrigerant liquid droplets from the evaporator 1 side, it is necessary to consider droplet separation in both directions to prevent solution droplets from transferring from the absorber side. The structure of the droplet separator becomes complex and its dimensions increase.
又、蒸発器1下部液溜隔壁部へ溶液散布液が
接触すると、吸収溶液が結晶温度以下に冷却さ
れ、隔壁表面上に結晶を生じる恐れがある。こ
の場合特公昭43−10471に示される如き断熱層
を設ける必要があり、構造が複雑となる。 Further, when the solution spraying liquid comes into contact with the lower liquid reservoir partition wall of the evaporator 1, the absorption solution may be cooled below the crystallization temperature and crystals may form on the partition wall surface. In this case, it is necessary to provide a heat insulating layer as shown in Japanese Patent Publication No. 43-10471, and the structure becomes complicated.
上部発生器4及び凝縮器3を、吸収器2、蒸
発器1と別缶胴にした場合は、上部胴と下部胴
の連絡配管6を設ける必要がある。上部胴と下
部胴の間に、気密チエツク及び万一の気密不良
の対策の為の補修用の空間7を設ける必要があ
り、外形寸法を小型化する場合の障害となる。 If the upper generator 4 and condenser 3 are provided in separate can bodies from the absorber 2 and evaporator 1, it is necessary to provide a connecting pipe 6 between the upper and lower shells. It is necessary to provide a space 7 between the upper shell and the lower shell for airtightness check and repair in case of airtightness failure, which becomes an obstacle in reducing the external dimensions.
又、製造工程を考えると、上部胴及び下部胴
を別個に製作するため、作業スペースが倍必要
となる。両端のチユーブプレートの位置決め等
多くの段取り時間を要する。 Furthermore, considering the manufacturing process, since the upper and lower shells are manufactured separately, twice the work space is required. It takes a lot of setup time, such as positioning the tube plates at both ends.
保温、保冷施工を考えた場合、蒸発器1及び
発生器4周囲の外部接触面積が広く、又施工も
曲がりが多く生じ施工費が高くなる。 When considering heat insulation and cold insulation construction, the external contact area around the evaporator 1 and generator 4 is large, and the construction also involves many bends, which increases the construction cost.
の如き問題点がある。There are problems such as.
また、第3図に示す如き従来例においては、
吸収サイクル上の最低温部である蒸発器1の
上部に高温部である発生器4がある為、熱ロス
が大きい。 In addition, in the conventional example shown in FIG. 3, the generator 4, which is a high temperature part, is located above the evaporator 1, which is the lowest temperature part in the absorption cycle, so that heat loss is large.
縦型の多段の配置の熱交換器を丸缶胴内に収
容せしめる必要から、蒸発器1の列数を少なく
し、高さ方向を小さくしている為、蒸発器1か
らの蒸発冷媒通路は左右に設けられ、左右各々
冷媒液分離器を備えることから構造が複雑とな
つている。 Since it is necessary to house the vertical multi-stage heat exchanger in the round can body, the number of rows of evaporators 1 is reduced and the height direction is made small, so the evaporative refrigerant passage from the evaporator 1 is The structure is complicated because it is provided on the left and right sides, and each side has a refrigerant liquid separator.
缶胴内部に納まつた蒸発器1から外部の冷媒
ポンプへ通ずる冷媒通路9は、気密が絶対必要
な真空容器である吸収冷凍機においては、製作
上の困難度を増し好ましくない。 The refrigerant passage 9 leading from the evaporator 1 housed inside the can body to the external refrigerant pump is undesirable in an absorption refrigerator, which is a vacuum container that must be airtight, since it increases the difficulty in manufacturing.
の如き問題点を有する。It has the following problems.
本発明は、従来のものの上記の問題点を解決
し、吸収器の伝熱管の列数を少なくしながら、容
器の幅方向の寸法が小であり、構造が簡単で、熱
損失も少ない吸収冷凍機を提供することを目的と
する。 The present invention solves the above-mentioned problems of the conventional ones, reduces the number of rows of heat transfer tubes in the absorber, has a small width dimension of the container, has a simple structure, and has low heat loss. The purpose is to provide a machine.
本発明は、一つの容器の上段部には、発生器4
と凝縮器3とを連通路を介して並列配備し、中段
部には、前記凝縮器3のほぼ真下に蒸発器を、減
圧機構15のある天板12を介して配備し、かつ
前記発生器4のほぼ真下に、前記蒸発器1の片側
に設けられ、該蒸発器1と連通した蒸発冷媒通路
10を配備して発生器4を蒸発器1から離すと共
に、該蒸発冷媒通路10と蒸発器1との真下の下
段部には蒸発器から離れた片側で前記蒸発冷媒通
路10に連通し、かつ前記蒸発器1の底部よりも
下方に溶液散布部を備えた吸収器2を備えたもの
である。
The present invention has a generator 4 in the upper part of one container.
and a condenser 3 are arranged in parallel via a communication path, and an evaporator is arranged in the middle section almost directly below the condenser 3 via a top plate 12 with a pressure reduction mechanism 15, and the generator 4, an evaporative refrigerant passage 10 is provided on one side of the evaporator 1 and communicated with the evaporator 1 to separate the generator 4 from the evaporator 1, and to connect the evaporative refrigerant passage 10 and the evaporator. 1, an absorber 2 is provided at the lower stage directly below the evaporator 1, the absorber 2 is connected to the evaporative refrigerant passage 10 on one side away from the evaporator, and has a solution dispersion section below the bottom of the evaporator 1. be.
本発明の実施例を図面を用いて説明する。 Embodiments of the present invention will be described using the drawings.
第1図において、蒸発器1及び吸収器2は、容
器の中段部にて蒸発器1を容器の下段部に配備し
た吸収器2の上方に配置すると共に、蒸発器1は
吸収器2の中心より片側にずらして配置し、蒸発
器1にて蒸発した冷媒蒸気を導く蒸発冷媒通路1
0を前記ずらした側にのみ設け、且つ反対側蒸発
器1の下部に空間11を設けている。 In FIG. 1, the evaporator 1 and the absorber 2 are arranged in the middle part of the container, and the evaporator 1 is arranged above the absorber 2, which is arranged in the lower part of the container. An evaporative refrigerant passage 1 which is arranged to be shifted to one side and guides the refrigerant vapor evaporated in the evaporator 1.
0 is provided only on the shifted side, and a space 11 is provided below the evaporator 1 on the opposite side.
又、凝縮器3及び発生器4は容器の上段部に並
べて横配置とし、蒸発器1のほぼ上部に減圧機構
15を介して凝縮器3が、前記蒸発冷媒通路10
のほぼ上方に発生器4が、蒸発器1及び蒸発冷媒
通路10の天板12を隔壁として配置されてい
る。 Further, the condenser 3 and the generator 4 are horizontally arranged side by side in the upper part of the container, and the condenser 3 is connected to the evaporative refrigerant passage 10 almost above the evaporator 1 via a pressure reducing mechanism 15.
The generator 4 is arranged substantially above the evaporator 1 and the top plate 12 of the evaporative refrigerant passage 10 as a partition wall.
なお本実施例では、凝縮器底板である天板12
と蒸発器1の底板13を渡る側板14が、これら
底板13の端部より内側に凹む構造となつてい
る。 Note that in this embodiment, the top plate 12 which is the bottom plate of the condenser
A side plate 14 extending across the bottom plate 13 of the evaporator 1 is recessed inward from the ends of the bottom plate 13.
本構成としたことにより、蒸発器1の管束は縦
長にでき、吸収器2の管束は列数を減らし幅方向
を大きくすることができる為、蒸発冷媒通路10
は蒸発器1の片側で十分通路面積が保持できると
共に、吸収器2管群には上部から冷媒蒸気が導入
されるので、吸収溶液の散布方向と平行となり、
均一な吸収作用を発揮することができる。 With this configuration, the tube bundle of the evaporator 1 can be made vertically long, and the tube bundle of the absorber 2 can be made wider in the width direction by reducing the number of rows.
Since a sufficient passage area can be maintained on one side of the evaporator 1, and the refrigerant vapor is introduced into the absorber 2 tube group from above, it is parallel to the direction of dispersion of the absorption solution.
It can exhibit a uniform absorption effect.
又、吸収器2における溶液散布液は、蒸発冷媒
通路10を上方にしたことにより蒸発器1側への
飛散を防ぐことができると共に、散布液が、蒸発
器1の冷媒液を収容する壁体と接触することがな
く、絶縁されている為、吸収液の隔壁面上での結
晶の心配もない。 Further, the solution sprayed liquid in the absorber 2 can be prevented from scattering toward the evaporator 1 side by placing the evaporative refrigerant passage 10 upward, and the sprayed liquid can be prevented from scattering toward the evaporator 1 by the wall body containing the refrigerant liquid. Since there is no contact with the liquid and it is insulated, there is no need to worry about crystals forming on the partition surface of the absorption liquid.
凝縮器3、発生器4の配置は上述の如く、高温
部である発生器4を、天板12を通して、蒸発冷
媒通路10と隣接させ、蒸発器1とは離したこと
により、熱損失は、無視できる量とすることがで
きる。 As mentioned above, the arrangement of the condenser 3 and generator 4 is such that the generator 4, which is a high-temperature part, is placed adjacent to the evaporative refrigerant passage 10 through the top plate 12 and separated from the evaporator 1, thereby reducing heat loss. The amount can be ignored.
蒸発器1の下部空間は、吸収器2との熱絶縁を
図ると共に、寒冷地や、年間での運転が長い等、
冷却水温度が低く、吸収溶液濃度が比較的薄い運
転が多い冷凍機の場合には、該空間に予め冷媒溜
16を設けることもできる。 The space below the evaporator 1 is designed to provide thermal insulation from the absorber 2, and is designed to be used in cold regions or where operation is long during the year.
In the case of a refrigerator that is often operated with a low cooling water temperature and a relatively low absorption solution concentration, a refrigerant reservoir 16 may be provided in advance in this space.
吸収冷凍機は前記熱交換器である蒸発器1、吸
収器2、凝縮器3、発生器4の集合体であり、吸
収剤としてLiBr溶液を、冷媒として水を使用し
ている冷凍機においては各熱交換器温度は一般空
調用途で、蒸発器で2〜10℃、吸収器で30〜50
℃、凝縮器で30〜45℃、発生器で70〜100℃であ
り、断熱を考えると、蒸発器で保冷、発生器で保
温が必要となる。この場合特に蒸発器は保冷が不
十分であると、結露を生じ、缶胴表面の腐蝕や、
機械下の濡れ等、種々の不具合がある為、確実に
施す必要がある。従来品は前述の施工しずらさが
ある為、保冷も不確実で作業コストもかかつてい
たが、本実施例では、第1図の斜線部に缶胴の隔
壁である天板12、底板13、側板14を利用し
て、保冷材17を取りつけることができ、施工個
所も少なく、又、施工も容易という効果がある。 An absorption refrigerator is an assembly of the heat exchangers evaporator 1, absorber 2, condenser 3, and generator 4, and in a refrigerator that uses LiBr solution as an absorbent and water as a refrigerant, The temperature of each heat exchanger is 2 to 10℃ for the evaporator and 30 to 50℃ for the absorber for general air conditioning applications.
℃, 30 to 45℃ in the condenser, and 70 to 100℃ in the generator. Considering insulation, it is necessary to keep the evaporator cold and the generator warm. In this case, if the evaporator is not kept cool enough, condensation may occur, causing corrosion on the surface of the can body.
Since there are various problems such as wetness under the machine, it is necessary to apply it reliably. The conventional product has the above-mentioned construction difficulty, so cold insulation is uncertain and work costs are high.However, in this embodiment, the top plate 12, bottom plate 13, which is the bulkhead of the can body, are shown in the shaded area in Fig. 1. The cold insulation material 17 can be attached using the side plate 14, and there are fewer installation locations and the installation is also easy.
本構造は第1図の如く、前述の各熱交換器(蒸
発器、吸収器、凝縮器、発生器)の管板を共有化
し、各熱交換器の缶胴を隔壁に利用して、組立て
る構成とすれば、製作も容易であり、且つ作業ス
ペースも一ケ所で済むという製作上の効果も生じ
ている。 As shown in Figure 1, this structure is assembled by sharing the tube plate of each heat exchanger (evaporator, absorber, condenser, generator) and using the can body of each heat exchanger as a partition wall. This configuration has the advantage of being easy to manufacture and requiring only one work space.
尚、従来例の第2,3図は二重効用吸収冷凍機
で本発明の実施例の第1図は単効用吸収冷凍機で
示したが、本発明は、前記各熱交換器で構成され
る吸収冷凍機の構造に関するものであり、吸収サ
イクルは単効用でも二重効用でも適用できる。 2 and 3 of the conventional example show a double-effect absorption refrigerator, and FIG. 1 of the embodiment of the present invention shows a single-effect absorption refrigerator. This paper relates to the structure of an absorption refrigerating machine, and the absorption cycle can be applied to either single-effect or double-effect.
本発明は一つの容器の上段部には、発生器と凝
縮器とを連通路を介して並列配備し、中段部に
は、前記凝縮器のほぼ真下に蒸発器を、減圧機構
のある天板を介して配備し、かつ前記発生器のほ
ぼ真下に、前記蒸発器の片側に設けられ、該蒸発
器と連通した蒸発冷媒通路を配備して発生器を蒸
発器から離すと共に、該蒸発冷媒通路と蒸発器と
の真下の下段部には蒸発器から離れた片側で前記
蒸発冷媒通路に連通し、かつ前記蒸発器の底部よ
りも下方に溶液散布部を備えた吸収器を備えたこ
とにより、蒸気冷媒通路は、蒸発器の片側で十分
通路面積が保有でき吸収器管群へは上方から冷媒
蒸気が導入されるので、吸収溶液の散布方向と平
行となり、吸収器内での均一な吸収作用を発揮す
ることができるし、蒸発器から離れた片側に寄つ
た吸収器における溶液散布液は、蒸発冷媒通路を
上方にしたことにより蒸発器側への飛散を防ぐこ
とができると共に、散布液が、蒸発器の冷媒液を
収容する壁体と接触することがなく、絶縁されて
いることで、吸収液の隔壁面上での結晶の心配も
ないし、しかも高温部である発生器を、天板を通
して、蒸発冷媒通路と隣接させ、蒸発器とは離し
たことにより、熱損失は、無視できる量とするこ
とができるほか、吸収器の伝熱管群の上下段数を
も減らして吸収作用を有効に行わしめ、しかも容
器の幅を大とすることを避け、発生器の加熱エネ
ルギの熱損失を防ぎ、蒸発器からの蒸発冷媒通路
が片側のみで済み、エリミネータも片側でよいの
で構造が簡単となり、全体の寸法が小型化となる
吸収冷凍機を提供することができ、実用上極めて
大なる効果を奏する。
In the present invention, a generator and a condenser are arranged in parallel through a communication path in the upper part of one container, and an evaporator is arranged in the middle part almost directly below the condenser, and a top plate with a pressure reduction mechanism is installed in the middle part. and substantially directly below the generator, an evaporative refrigerant passage provided on one side of the evaporator and communicating with the evaporator to separate the generator from the evaporator; and an absorber connected to the evaporative refrigerant passage on one side remote from the evaporator and having a solution dispersion section below the bottom of the evaporator is provided in the lower part directly below the evaporator. The vapor refrigerant passage has a sufficient passage area on one side of the evaporator, and the refrigerant vapor is introduced from above into the absorber tube group, so it is parallel to the direction of dispersion of the absorption solution, ensuring a uniform absorption action within the absorber. In addition, by placing the evaporative refrigerant passage upward, it is possible to prevent the solution spraying liquid in the absorber that is located on one side away from the evaporator from scattering toward the evaporator side. Since it does not come into contact with the wall that houses the refrigerant liquid in the evaporator and is insulated, there is no need to worry about crystals of the absorbent liquid on the partition wall surface.Furthermore, the generator, which is a high-temperature part, can be placed on the top plate. By arranging the evaporative refrigerant passage through the evaporative refrigerant passage and separating it from the evaporator, heat loss can be made negligible, and the number of upper and lower stages of the absorber's heat transfer tube group can be reduced to make the absorption effect more effective. In addition, it avoids increasing the width of the container, prevents heat loss of the heating energy of the generator, and simplifies the structure because the evaporative refrigerant passage from the evaporator only needs to be on one side, and the eliminator only needs to be on one side. It is possible to provide an absorption refrigerator whose overall size is reduced, which is extremely effective in practice.
第1図は本発明の実施例のフロー図、第2図及
び第3図は従来例のフロー図である。
1……蒸発器、2……吸収器、3……凝縮器、
4……発生器、5……液滴分離器、6……連絡配
管、7……空間、8……冷媒ポンプ、9……冷媒
通路、10……蒸発冷媒通路、11……空間、1
2……天板、13……底板、14……側板、15
……減圧機構、16……冷媒溜、17……保冷
材。
FIG. 1 is a flow diagram of an embodiment of the present invention, and FIGS. 2 and 3 are flow diagrams of a conventional example. 1...evaporator, 2...absorber, 3...condenser,
4... Generator, 5... Droplet separator, 6... Connecting pipe, 7... Space, 8... Refrigerant pump, 9... Refrigerant passage, 10... Evaporative refrigerant passage, 11... Space, 1
2...Top plate, 13...Bottom plate, 14...Side plate, 15
...pressure reduction mechanism, 16 ... refrigerant reservoir, 17 ... cold insulation material.
Claims (1)
3とを連通路を介して並列配備し、中段部には、
前記凝縮器3のほぼ真下に蒸発器を、減圧機構1
5のある天板12を介して配備し、かつ前記発生
器4のほぼ真下に、前記蒸発器1の片側に設けら
れ、該蒸発器1と連通した蒸発冷媒通路10を配
備して発生器4を蒸発器1から離すと共に、該蒸
発冷媒通路10と蒸発器1との真下の下段部には
蒸発器から離れた片側で前記蒸発冷媒通路10に
連通し、かつ前記蒸発器1の底部よりも下方に溶
液散布部を備えた吸収器2を備えたことを特徴と
する吸収冷凍機。 2 前記蒸発器1が、蒸発器底部より離れた下方
位置に冷媒液を収容される冷媒液溜り16を備え
ている特許請求の範囲第1項記載の吸収冷凍機。[Claims] 1. In the upper part of one container, a generator 4 and a condenser 3 are arranged in parallel via a communication path, and in the middle part,
An evaporator is installed almost directly below the condenser 3, and a pressure reduction mechanism 1 is installed.
5, and an evaporative refrigerant passage 10 provided on one side of the evaporator 1 and communicating with the evaporator 1 is provided almost directly below the generator 4. is separated from the evaporator 1, and a lower part directly below the evaporative refrigerant passage 10 and the evaporator 1 is connected to the evaporative refrigerant passage 10 on one side away from the evaporator, and is lower than the bottom of the evaporator 1. An absorption refrigerating machine characterized by comprising an absorber 2 with a solution dispersion section below. 2. The absorption refrigerator according to claim 1, wherein the evaporator 1 is provided with a refrigerant liquid reservoir 16 in which the refrigerant liquid is stored at a lower position away from the bottom of the evaporator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27374784A JPS61153353A (en) | 1984-12-27 | 1984-12-27 | Absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27374784A JPS61153353A (en) | 1984-12-27 | 1984-12-27 | Absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61153353A JPS61153353A (en) | 1986-07-12 |
| JPH0473059B2 true JPH0473059B2 (en) | 1992-11-19 |
Family
ID=17532006
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27374784A Granted JPS61153353A (en) | 1984-12-27 | 1984-12-27 | Absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61153353A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3193578B2 (en) * | 1994-12-01 | 2001-07-30 | 株式会社荏原製作所 | Absorption refrigerator |
| WO2004087830A1 (en) * | 2003-03-28 | 2004-10-14 | Hachinohe Institute Of Technology | Operating medium for absorption refrigerator, absorption refrigerator and process for producing cold heat heating medium |
-
1984
- 1984-12-27 JP JP27374784A patent/JPS61153353A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61153353A (en) | 1986-07-12 |
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| LAPS | Cancellation because of no payment of annual fees |