JPS61153353A - Absorption refrigerator - Google Patents
Absorption refrigeratorInfo
- Publication number
- JPS61153353A JPS61153353A JP27374784A JP27374784A JPS61153353A JP S61153353 A JPS61153353 A JP S61153353A JP 27374784 A JP27374784 A JP 27374784A JP 27374784 A JP27374784 A JP 27374784A JP S61153353 A JPS61153353 A JP S61153353A
- Authority
- JP
- Japan
- Prior art keywords
- evaporator
- absorber
- generator
- refrigerant
- 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.)
- Granted
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は発生器、a雑器、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 equipped with a generator, a miscellaneous device, 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0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′a縮雑器3
別缶胴内に収容する構造となっている。An example of the structure of a conventional refrigerator of this kind is shown in FIG. 2. The absorption refrigerator shown in FIG. Reducer 3
The structure is such that it is 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l、吸収器2を
上下配置とし、凝縮器3と発生84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 the absorber 2 are arranged one above the other, and the condenser 3 and the generator 84 are housed together in the round can body. , 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r&2管束は溶液散布方式でチュー
ブ濡れ面を形成し、溶液は上部管列から下部管列へと蒸
発器lからの冷媒蒸気を吸収しながら滴下する為、チュ
ーブ列数が多い場合には下部管束のチューブにまで至っ
た溶液は既に飽和して殆ど吸収能力が保持できず存効度
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, (1) In order to reduce the external width dimension, it is necessary to increase the number of columns of two absorber tube bundles, and the absorber R & two tube bundles form the tube wetted surface by a solution spraying method. However, since the solution drips from the upper tube row to the lower tube row while absorbing refrigerant vapor from the evaporator L, if there are many tube rows, the solution reaching the tubes in the lower tube bundle is already saturated. The lower tube bundle is wasted because it cannot maintain much of its absorption capacity and its effectiveness is low.
一方列数を減少させて、幅方向のチューブ本数を増やそ
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l管束とが左右に配置されて
いるので、吸収器2管東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と茎発器
1との境界部には、T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, the solution spray to the upper east of the absorber 2 tubes is transferred to the evaporator 1.
Therefore, in addition to entrainment of refrigerant liquid droplets from the T-generator 1 side, the boundary between the absorber 2 and the stem generator 1 has the possibility of liquid droplets migrating from the absorber side. It becomes necessary to consider droplet separation in both directions to prevent droplet separation, which complicates the structure of the droplet separator and increases its size.
又、蒸発器l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43−1047
1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 partition wall of the lower part of the evaporator l, the absorption solution may be cooled to below the crystallization temperature and crystals may form on the surface of the partition wall. In this case, the Special Public Interest Publication No. 43-1047
It is necessary to provide a heat insulating layer as shown in 1, which makes the structure complicated.
■ 上部発生器4及び凝縮器3を、吸収器2、蒸発器l
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、気密チェッ
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
ける必要かあ 。■ Upper generator 4 and condenser 3, absorber 2 and evaporator l
If the can body is separate from the can body, it is necessary to provide a connecting pipe 6 between the upper and lower shells. Is it necessary to provide a repair space 7 between the upper and lower shells to check the airtightness and take measures in case of poor airtightness?
す、外形寸法を小型化する場合の障害となる。However, this becomes an obstacle when 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0両端のチュ
ーブプレートの位置決め等多くの段取り時間を要する。In addition, considering the manufacturing process, since the upper and lower shells are manufactured separately, a lot of setup time is required, such as positioning the tube plates at both ends, which requires double the work space.
■ 保温、保冷施工を考えた場合、蒸発器l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 the generator 4 is large, and there are many bends during construction, 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lの上部に高温部であ
る発注器4がある為、熱ロスが大きい。In addition, in the conventional example shown in FIG. 3, (1) heat loss is large because the high temperature section 4 is located above the evaporator 1, which is the lowest temperature section on the absorption cycle;
■ 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l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
造が複雑となっている。■ Because it is necessary to house the vertical multi-stage heat exchanger inside the round can body, the number of rows of evaporators 1 is reduced and the height direction is small, so the evaporative refrigerant passage from evaporator 1 is reduced. are provided on the left and right sides, and have a refrigerant liquid separator on each side, making the structure complicated.
■ 缶胴内部に納まった蒸発器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。(2) The refrigerant passage 9 leading from the evaporator 1 housed inside the can body to the external refrigerant pump is undesirable because it increases the manufacturing difficulty in an absorption refrigerator, which is a vacuum container that must be airtight.
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、構造が暦車で、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 absorber, reduces the number of rows of heat transfer tubes in the absorber, has a small width dimension of the container, has a calendar wheel structure, and has low heat loss. The purpose is to provide refrigerators.
本発明は、上記の問題点を解決するための手段として、
一つの容器を上段部、中段部、下段部に分け、前記上段
部には、発生器と凝縮器とを連通路を介して並べて配備
し、前記中段部には、前記凝縮器のほぼ真下に蒸発器を
、減圧機構を介して配備し、前記発生器のほぼ真下に、
前記蒸発器の片側に設けられた連通路を介して該蒸発器
と連通し、該蒸発器で蒸発した冷媒蒸気を導く蒸発冷媒
通路を配備し、前記下段部には前記蒸発冷媒通路に連通
し、溶液散布部を前記蒸発器の底部よりも下方に備えた
吸収器を備えたことを特徴とする吸収冷凍機を提供する
ものである。The present invention, as a means for solving the above problems,
One container is divided into an upper part, a middle part, and a lower part, and in the upper part, a generator and a condenser are arranged side by side via a communication path, and in the middle part, a generator and a condenser are arranged side by side through a communication path, and in the middle part, a generator and a condenser are arranged side by side through a communication path. An evaporator is provided via a pressure reduction mechanism, substantially directly below the generator,
An evaporative refrigerant passage that communicates with the evaporator through a communication passage provided on one side of the evaporator and guides refrigerant vapor evaporated in the evaporator is provided, and the lower part communicates with the evaporative refrigerant passage. Another object of the present invention is to provide an absorption refrigerator comprising an absorber having a solution spraying section below the bottom of the evaporator.
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、痕発器!及び吸収器2は、容器の中段
部にて蒸発!s1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lは吸収器2の中心より
片側にずらして配置し、蒸発器lにて1発した冷媒蒸気
を導く蒸発冷媒通路lOを前記ずらした側にのみ設け、
且つ反対側蒸発器lの下部に空間11を設けている。In Figure 1, trace generator! And absorber 2 evaporates in the middle part of the container! s1 is placed above the absorber 2 arranged in the lower part of the container, and the evaporator l is placed offset to one side from the center of the absorber 2, and the evaporative refrigerant guides the refrigerant vapor released once in the evaporator l. A passage IO is provided only on the shifted side,
Moreover, 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lOのほぼ上方に発生器4
が、蒸発器1及び蒸発冷媒通路lO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 installed almost above the evaporator 1 via a pressure reducing mechanism 15, and the generator 4 is installed almost above the evaporative refrigerant passage IO.
are arranged using the evaporator 1 and the top plate 12 of the evaporative refrigerant passage lO as partition walls.
なお本実施例では、凝縮器底板である天板12と蒸発器
l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っている。In this embodiment, the side plate 14 that crosses the top plate 12, which is the bottom plate of the condenser, and the bottom plate 13 of the evaporator 1 is recessed inward from the ends of these bottom plates 13.
本構成としたことにより、蒸発器l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. The area can be maintained, and since refrigerant vapor is introduced into the two absorber tube groups from above, it is parallel to the direction in which the absorption solution is distributed, and a uniform absorption effect can be achieved.
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 is transferred to the evaporative refrigerant passage 10.
By locating it upwards, it is possible to prevent the spraying liquid from scattering toward the evaporator 1 side, and since the spray liquid does not come into contact with the wall that houses the refrigerant liquid in the evaporator 1 and is insulated, the absorption liquid There is no need to worry about crystals forming on the partition wall surface.
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l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 the 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 should be used for refrigerators that operate in cold regions or operate for long periods of the year, etc. - Refrigerators that are often operated with low cooling water temperature and relatively low absorption solution concentration. In this case, a refrigerant reservoir 16 may be provided in advance in the space.
吸収冷凍機は前記熱交換器である蒸発器l、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Li
Br1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2〜1
0℃、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すらさかある
為、保冷も不確実で作業コストもかかっていたが、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。The absorption refrigerator includes an evaporator 1 which is the heat exchanger, an absorber 2,
It is an assembly of a condenser 3 and a generator 4, and uses Li as an absorbent.
In refrigerators that use Br1 liquid and water as a refrigerant, the temperature of each heat exchanger is 2 to 1 in the evaporator for general air conditioning use.
0℃, 30-50℃ in the absorber, 30-45℃ in the condenser,
The temperature in the generator is 70 to 100°C, and when considering insulation, it is necessary to keep the evaporator cold and the generator warm. In this case, in particular, if the evaporator is not sufficiently cooled, condensation will occur, causing various problems such as corrosion on the surface of the can body and wetness under the machine, so it is necessary to do this reliably. In the conventional product, the above-mentioned installation process was uneven, making the cold storage unreliable and the work cost high.However, in this embodiment, the top plate 12, which is the bulkhead of the can body, is shown in the shaded area in Fig. 1.
.. The cold insulating material 17 can be attached using the bottom plate 13 and the side plates 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。Note that FIG. 2.3 of the conventional example shows a double-effect absorption refrigerating machine, and FIG. 1 of the embodiment of the present invention shows a single-effect absorption refrigerating machine. 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.
本発明により、吸収器の伝熱管の上下段数を減らして吸
収作用を有効に行わしめ、しかも容器の輻を大とするこ
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。According to the present invention, the number of upper and lower stages of heat transfer tubes in the absorber is reduced to effectively perform the absorption action, and in addition, it is possible to avoid increasing the convergence of the container, prevent heat loss of the heating energy of the generator, and reduce the heat loss from the evaporator. Since the evaporative refrigerant passage only needs to be on one side and the eliminator needs to be on one side, it is possible to provide an absorption refrigerator with a simple structure and a smaller overall size, 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。
I・・蒸発器、2・−吸収器、3−凝縮器、4−・−発
生器、5−液滴分離器、6一連絡配管、7−・・空間、
8・・−冷媒ポンプ、9−・−冷媒通路、l〇−蒸発冷
媒通路、11・・・空間、12・・−天板、13・−・
底板、14−・側板、lS−・減圧機構、16・・・冷
媒溜、17・・。
保冷材。
特許出願人 株式会社 荏原製作所代理人弁理士
高 木 正 行代理人弁理士 依 1
) 孝 次 部第1図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. I...evaporator, 2--absorber, 3-condenser, 4--generator, 5-droplet separator, 6-connecting piping, 7--space,
8...-refrigerant pump, 9--refrigerant passage, l〇-evaporative refrigerant passage, 11... space, 12...-top plate, 13...
Bottom plate, 14-・Side plate, 1S-・Pressure reduction mechanism, 16... Refrigerant reservoir, 17.... Cold insulation material. Patent applicant: Ebara Corporation Representative patent attorney: Masayuki Takagi Representative patent attorney: Yori 1
) Takatsugu Part 1
Claims (1)
真下に、前記蒸発器の片側に設けられた連通路を介して
該蒸発器と連通し、該蒸発器で蒸発した冷媒蒸気を導く
蒸発冷媒通路を配備し、 前記下段部には前記蒸発冷媒通路に連通し、溶液散布部
を前記蒸発器の底部よりも下方に備えた吸収器を備えた ことを特徴とする吸収冷凍機。 2、前記蒸発器の冷媒液溜りの冷媒液が、前記溶液散布
部から散布された溶液がかかる前記吸収器の壁体には接
しないように収容されている特許請求の範囲第1項記載
の吸収冷凍機。[Claims] 1. One container is divided into an upper part, a middle part, and a lower part, in the upper part, a generator and a condenser are arranged side by side via a communication path, and in the middle part, , an evaporator is provided almost directly below the condenser via a pressure reduction mechanism, and is communicated with the evaporator via a communication passage provided on one side of the evaporator almost directly below the generator; An evaporative refrigerant passage is provided for guiding the refrigerant vapor evaporated in the evaporator, and the lower part is provided with an absorber that communicates with the evaporative refrigerant passage and has a solution dispersion part below the bottom of the evaporator. An absorption chiller featuring: 2. The refrigerant liquid in the refrigerant liquid reservoir of the evaporator is accommodated so that the solution sprayed from the solution spraying section does not come into contact with the wall of the absorber. Absorption refrigerator.
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 true JPS61153353A (en) | 1986-07-12 |
JPH0473059B2 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) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5605057A (en) * | 1994-12-01 | 1997-02-25 | Ebara Corporation | Absorption refrigerating machine |
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
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5605057A (en) * | 1994-12-01 | 1997-02-25 | Ebara Corporation | Absorption refrigerating machine |
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 |
JPWO2004087830A1 (en) * | 2003-03-28 | 2006-07-06 | 学校法人八戸工業大学 | Absorption chiller working medium, absorption chiller, and method for producing cooling and heating medium |
Also Published As
Publication number | Publication date |
---|---|
JPH0473059B2 (en) | 1992-11-19 |
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Legal Events
Date | Code | Title | Description |
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LAPS | Cancellation because of no payment of annual fees |