JPS6118370Y2 - - Google Patents

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Publication number
JPS6118370Y2
JPS6118370Y2 JP16958981U JP16958981U JPS6118370Y2 JP S6118370 Y2 JPS6118370 Y2 JP S6118370Y2 JP 16958981 U JP16958981 U JP 16958981U JP 16958981 U JP16958981 U JP 16958981U JP S6118370 Y2 JPS6118370 Y2 JP S6118370Y2
Authority
JP
Japan
Prior art keywords
stage
low
chamber
condenser
generator
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
Application number
JP16958981U
Other languages
Japanese (ja)
Other versions
JPS5874058U (en
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 filed Critical
Priority to JP16958981U priority Critical patent/JPS5874058U/en
Publication of JPS5874058U publication Critical patent/JPS5874058U/en
Application granted granted Critical
Publication of JPS6118370Y2 publication Critical patent/JPS6118370Y2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【考案の詳細な説明】 本考案は吸収式冷凍機、詳しくは高段発生器と
低段発生器及び高段凝縮器と低段凝縮器とを備え
た吸収式冷凍機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerator, and more particularly to an absorption refrigerator equipped with a high-stage generator, a low-stage generator, a high-stage condenser, and a low-stage condenser.

従来以上の如く構成する吸収式冷凍機は、例え
ば特公昭53−35663号公報に示されている。この
従来のものは第4図に示すように、発生器及び凝
縮器をそれぞれ高段と低段の2個に分割して、分
割した各単一の発生器a1,a2と凝縮器b1,b2とを
それぞれ1対として独立した室内A,Bに設ける
と共に、これら各室A,Bに設ける発生器a1,a2
を互に直列状に連通させて高段発生器a1から低段
発生器a2に至る溶液の流れを可能にしていた。ま
た、前記各凝縮器b1,b2に配設する冷却水配管c
を連続さて、冷却水を前記低段発生器a2に対応す
る低段凝縮器b2から高段発生器a1に対応する高段
凝縮器b1へ流通させると共に、これら低段凝縮器
b2と高段凝縮器b1とにそれぞれ冷媒液管d2,d1
並列的に接続していたのである。
An absorption refrigerating machine constructed as described above is shown in, for example, Japanese Patent Publication No. 35663/1983. As shown in Fig. 4, in this conventional system, the generator and condenser are each divided into two parts, a high stage and a low stage, and each divided single generator a 1 , a 2 and condenser b 1 and b 2 are provided as a pair in independent rooms A and B, and generators a 1 and a 2 are provided in each of these rooms A and B.
were connected to each other in series to enable flow of solution from the high stage generator a1 to the low stage generator a2 . In addition, cooling water pipes c installed in each of the condensers b 1 and b 2
Then, cooling water is passed from the low stage condenser b 2 corresponding to the low stage generator a 2 to the high stage condenser b 1 corresponding to the high stage generator a 1 , and these low stage condensers
Refrigerant liquid pipes d 2 and d 1 were connected in parallel to b 2 and high-stage condenser b 1 , respectively.

所が以上の如く前記高段凝縮器b1と低段凝縮器
b2とに別々に冷媒液管d1,d2を接続して、これら
各冷媒液管d1,d2を合流させた後、高段及び低段
蒸発器e1,e2に接続する場合には、低段凝縮器b2
で過冷却状態となつた液冷媒と、高段凝縮器b1
液冷媒との平均的状態となつた液冷媒が前記各蒸
発器e1,e2に導びかれることになつていたのであ
り、一度過冷却状態となつた前記低段凝縮器b2
りの液冷媒の冷凍能力を無駄にしていたのであ
る。
As mentioned above, the high stage condenser b1 and the low stage condenser
Connect refrigerant liquid pipes d 1 and d 2 to b 2 separately, and after merging these refrigerant liquid pipes d 1 and d 2 , connect to high stage and low stage evaporators e 1 and e 2 . In case, low stage condenser b 2
The liquid refrigerant, which has reached an average state between the liquid refrigerant that has become supercooled and the liquid refrigerant in the high-stage condenser b 1 , was to be led to each of the evaporators e 1 and e 2 . Therefore, the refrigerating capacity of the liquid refrigerant from the low-stage condenser b2 , which had once reached a supercooled state, was wasted.

しかして本考案は以上の如き従来の吸収式冷凍
機における問題点に鑑み考案したので、目的とす
るところは、凝縮器よりの液冷媒を全体として過
冷却状態にならしめ、もつて冷凍効率を上昇させ
得る吸収式冷凍機を提供する点にあり、仕切壁を
もち、該仕切壁を挾んで水平方向側に高段室と低
段室とを形成した胴体の前記各室に、前記各凝縮
器を配置し、前記高段室に前記高段発生器を、ま
た、前記低段室に前記低段発生器をそれぞれ接続
すると共に、前記仕切壁の下端近くに流通孔を設
けて、前記高段室から低段室への凝縮液の流れを
可能にする一方、前記流通孔の低段室側に、前記
流通孔より高さの高い堰を設け、前記低段室に冷
媒液管を接続したことを特徴とするものである。
However, the present invention was devised in view of the above-mentioned problems with conventional absorption refrigerators, and its purpose is to bring the liquid refrigerant from the condenser into a supercooled state as a whole, thereby increasing refrigeration efficiency. The object of the present invention is to provide an absorption refrigerating machine that can be lifted up, and has a partition wall, and a high chamber and a low chamber are formed horizontally across the partition wall. the high-stage generator is connected to the high-stage chamber, and the low-stage generator is connected to the low-stage chamber, and a flow hole is provided near the lower end of the partition wall, While allowing the condensate to flow from the tray chamber to the lower chamber, a weir higher in height than the distribution hole is provided on the lower chamber side of the distribution hole, and a refrigerant liquid pipe is connected to the lower chamber. It is characterized by the fact that

以下本考案の実施例を図面に基づいて説明す
る。
Embodiments of the present invention will be described below based on the drawings.

1は箱形の胴体で、該胴体1の天板11に仕切
壁2を垂設し、該仕切壁2を挾んで水平方向両側
を高段室3と低段室4と成す一方、前記高段室3
には高段凝縮器31を、前記低段室4には低段凝
縮器41をそれぞれ配設する。また、第1図に示
したものは、これら凝縮器31,41の下方に、
高段発生器32と低段発生器42とを設け、前記
高段発生器32を前記低段発生器42の上方に位
置せしめると共に、前記高段発生器32に貯溜す
る溶液が一定深さ以上になると、第3図に示すご
とくの液封機構5を介して前記低段発生器42側
に流入するごとく成している。そして前記高段発
生器32を前記高段室3に、前記低段発生器42
を前記低段室4にそれぞれ開口させているのであ
る。
Reference numeral 1 denotes a box-shaped body, and a partition wall 2 is vertically disposed on a top plate 11 of the body 1, and a high chamber 3 and a low chamber 4 are formed on both sides in the horizontal direction by sandwiching the partition wall 2. Step room 3
A high-stage condenser 31 is disposed in the chamber 4, and a low-stage condenser 41 is disposed in the low-stage chamber 4, respectively. Furthermore, in the case shown in FIG. 1, below these condensers 31 and 41,
A high-stage generator 32 and a low-stage generator 42 are provided, the high-stage generator 32 is positioned above the low-stage generator 42, and the solution stored in the high-stage generator 32 has a depth of at least a certain depth. Then, the liquid flows into the low-stage generator 42 through a liquid seal mechanism 5 as shown in FIG. Then, the high stage generator 32 is placed in the high stage chamber 3, and the low stage generator 42 is placed in the high stage chamber 3.
are opened to the lower chamber 4, respectively.

また、前記高段発生器32と低段発生器42と
に配設する温水管Hは連続させており、前記低段
発生器42から高段発生器32へ温水が流通する
ごとく成す一方、前記高段凝縮器31と低段凝縮
器41とに配設する冷却水配管cも連続させてお
り、前記低段凝縮器41から高段凝縮器31へ冷
却水が流通するごとく成しているのである。
Further, the hot water pipes H disposed in the high stage generator 32 and the low stage generator 42 are continuous, so that hot water flows from the low stage generator 42 to the high stage generator 32, while The cooling water piping c disposed between the high-stage condenser 31 and the low-stage condenser 41 is also continuous, so that the cooling water flows from the low-stage condenser 41 to the high-stage condenser 31. be.

しかして本考案においては、第2図に示すごと
く前記仕切壁2の下端近くに流通孔21を設け
て、前記高段室3から低段室4への凝縮器の流れ
を可能にすると共に、前記流通孔21の低段室4
側に、前記流通孔21を形成位置よりも高さの高
い堰6を設ける一方、冷媒液管7を前記低段室4
に接続するのである。なお、高段室3及び低段室
4の底壁22は高段室3側から仕切室4側に下向
きに傾斜しており、凝縮液の排出を良好としてい
る。
Therefore, in the present invention, as shown in FIG. 2, a flow hole 21 is provided near the lower end of the partition wall 2 to enable flow of the condenser from the high chamber 3 to the low chamber 4, and Low chamber 4 of the communication hole 21
A weir 6 with a height higher than the position where the communication hole 21 is formed is provided on the side, and the refrigerant liquid pipe 7 is connected to the low chamber 4.
It connects to. The bottom walls 22 of the high chamber 3 and the low chamber 4 are inclined downward from the high chamber 3 side to the partition chamber 4 side, which facilitates the discharge of condensed liquid.

また、蒸発器81,82及び吸収器91,92
を配置する断面円形の胴体10を壁体10aによ
り上下に分割し、上部に低段蒸発器82と低段吸
収器92とを並列状に配置すると共に、下部に高
段蒸発器81と高段吸収器91とを並列状に配置
しており、前記冷媒液管7を、前記高段蒸発器8
1に開口している。そして、前記胴体10におけ
る壁体10aの蒸発器側と吸収器側とには、それ
ぞれ高段側に開口する流通管10b,10bを設
け、該流通管10b,10bの下端部に受体10
c,10cを取付けて、液封機構を形成してお
り、これら各液封機構を介して、前記各蒸発器8
2,81及び各吸収器92,91を連通している
のである。
In addition, evaporators 81, 82 and absorbers 91, 92
The body 10, which has a circular cross section and is arranged with The absorber 91 is arranged in parallel, and the refrigerant liquid pipe 7 is connected to the high stage evaporator 8.
It opens at 1. Further, on the evaporator side and the absorber side of the wall 10a of the body 10, there are provided flow pipes 10b, 10b which open to the higher stage side, respectively, and a receiver 10 is provided at the lower end of the flow pipes 10b, 10b.
c and 10c are attached to form a liquid seal mechanism, and each of the evaporators 8
2, 81 and each absorber 92, 91 are connected to each other.

尚、第1図において、83は冷媒ポンプ、93
は溶液ポンプ、94は熱交換器であり、Eは冷水
配管、Fは冷却水配管である。
In addition, in FIG. 1, 83 is a refrigerant pump, and 93 is a refrigerant pump.
is a solution pump, 94 is a heat exchanger, E is a cold water pipe, and F is a cooling water pipe.

しかして、前記発生器32,42で濃溶液とな
つた溶液は、濃溶液管D及び前記熱交換器94を
介して前記低段吸収器92側に流入し、前記液封
機構から前記高段吸収器91を経て、前記溶液ポ
ンプ93及び熱交換器94を介して前記高段発生
器32に返還される一方、前記発生器32,42
において発生した冷媒ガスは、前記凝縮器31,
41において凝縮し、前記冷媒液管7を介して前
記高段蒸発器81側に流入して蒸発すると共に、
未蒸発の冷媒液は前記冷媒ポンプ83を介して前
記低段蒸発器82側より散布され、前記液封機構
を構成すると前記連通管10b及び受体10cを
介して流下し、再び前記高段蒸発器81に供給さ
れるのであり、また、蒸発したガス冷媒は、前記
各吸収器91,92で前記濃溶液に吸収されるの
である。
The solution that has become a concentrated solution in the generators 32 and 42 flows into the low stage absorber 92 side via the concentrated solution pipe D and the heat exchanger 94, and flows from the liquid sealing mechanism to the high stage absorber 92 side. After passing through the absorber 91, it is returned to the high stage generator 32 via the solution pump 93 and heat exchanger 94, while the generators 32, 42
The refrigerant gas generated in the condenser 31,
41, and flows into the high stage evaporator 81 side via the refrigerant liquid pipe 7 and evaporates,
The unevaporated refrigerant liquid is dispersed from the low-stage evaporator 82 side via the refrigerant pump 83, and when the liquid seal mechanism is configured, it flows down through the communication pipe 10b and the receiver 10c, and returns to the high-stage evaporator. The evaporated gas refrigerant is absorbed into the concentrated solution in each of the absorbers 91 and 92.

以上の如く構成した実施例のものでは、前記高
段凝縮器31においては、高い温度・圧力で冷媒
が凝縮する一方、前記低段凝縮器41においては
低い温度・圧力で冷媒が凝縮するのであるが、前
記高段凝縮器31において凝縮した冷媒も、前記
流通孔21及び堰6を経て、前記低段室4側に流
入し、前記冷却水配管cを流れる低温の冷却水よ
り冷却され、前記低段凝縮器41において凝縮す
る冷媒と同等の過冷却状態となつて前記冷媒液管
7へと流出するのである。よつて前記凝縮器3
1,41においてそれぞれ凝縮した冷媒を、全体
として過冷却冷媒と成して前記蒸発器81,82
に供給することができ、冷凍能力を高めることが
できるものである。
In the embodiment configured as described above, the refrigerant is condensed at high temperature and pressure in the high stage condenser 31, while the refrigerant is condensed at low temperature and pressure in the low stage condenser 41. However, the refrigerant condensed in the high-stage condenser 31 also flows into the low-stage chamber 4 side through the circulation hole 21 and the weir 6, and is cooled by the low-temperature cooling water flowing through the cooling water pipe c. The refrigerant is in a supercooled state equivalent to that of the refrigerant condensed in the low-stage condenser 41, and flows out into the refrigerant liquid pipe 7. Therefore, the condenser 3
The refrigerant condensed in 1 and 41 respectively is made into a supercooled refrigerant as a whole and is transferred to the evaporators 81 and 82.
It is possible to increase the refrigeration capacity.

以上の説明により明らかなごとく、本考案の吸
収式冷凍機は仕切壁2をもち、該仕切壁2を挾ん
で水平方向両側に高段室3と低段室4とを形成し
た胴体1の前記各室3,4に、前記各凝縮器3
1,41を配置し、前記高段室3に前記高段発生
器32を、また、前記低段室4に前記低段発生器
42をそれぞれ接続すると共に、前記仕切壁2の
下端近くに流通孔21を設けて、前記高段室3か
ら低段室4への凝縮器の流れを可能にする一方、
前記流通孔21の低段室4側に、前記流通孔21
より高さの高い堰6を設け、前記低段室4に冷媒
液管7を接続したことを特徴とするものであるの
で、前記凝縮器31,41よりの液冷媒を全体と
して過冷却な状態とすることができ、よつて冷凍
能力を高めることができるものである。
As is clear from the above explanation, the absorption refrigerating machine of the present invention has a partition wall 2, and a high chamber 3 and a low chamber 4 are formed on both sides in the horizontal direction with the partition wall 2 in between. In each chamber 3, 4, each condenser 3
1 and 41, the high-stage generator 32 is connected to the high-stage chamber 3, and the low-stage generator 42 is connected to the low-stage chamber 4. holes 21 are provided to allow condenser flow from said high stage chamber 3 to said low stage chamber 4;
The communication hole 21 is located on the lower chamber 4 side of the communication hole 21.
Since a weir 6 with a higher height is provided and a refrigerant liquid pipe 7 is connected to the low stage chamber 4, the liquid refrigerant from the condensers 31 and 41 is kept in a supercooled state as a whole. This makes it possible to increase the refrigeration capacity.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案の実施例を示す配管系統図、第
2図及び第3図は要部の部分拡大断面図、第4図
は従来例を示す配管系統図である。 1……胴体、2……仕切壁、21……流通孔、
3……高段室、31……高段凝縮器、32……高
段発生器、4……低段室、41……低段凝縮器、
42……低段発生器、6……堰、7……冷媒液管
FIG. 1 is a piping system diagram showing an embodiment of the present invention, FIGS. 2 and 3 are partially enlarged sectional views of main parts, and FIG. 4 is a piping system diagram showing a conventional example. 1... body, 2... partition wall, 21... distribution hole,
3...high stage chamber, 31...high stage condenser, 32...high stage generator, 4...low stage chamber, 41...low stage condenser,
42...Low stage generator, 6...Weir, 7...Refrigerant liquid pipe

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 高段発生器32と低段発生器42及び高段凝縮
器31と低段凝縮器41とを備えた吸収式冷凍機
において、仕切壁2をもち、該仕切壁2を挾んで
水平方向両側に高段室3と低段室4とを形成した
胴体1の前記各室3,4に、前記各凝縮器31,
41を配置し、前記高段室3に前記高段発生器3
2を、また、前記低段室4に前記低段発生器42
をそれぞれ接続すると共に、前記仕切壁2の下端
近くに流通孔21を設けて、前記高段室3から低
段室4への凝縮器の流れを可能にする一方、前記
流通孔21の低段室4側に、前記流通孔21より
高さの高い堰6を設け、前記低段室4に冷媒液管
7を接続したことを特徴とする吸収式冷凍機。
In an absorption refrigerator equipped with a high-stage generator 32, a low-stage generator 42, a high-stage condenser 31, and a low-stage condenser 41, it has a partition wall 2, and has partition walls 2 on both sides in the horizontal direction. Each condenser 31,
41, and the high stage generator 3 is placed in the high stage chamber 3.
2, and the low stage generator 42 is also installed in the low stage chamber 4.
are connected to each other, and a flow hole 21 is provided near the lower end of the partition wall 2 to enable flow of the condenser from the high stage chamber 3 to the low stage chamber 4. An absorption refrigerator characterized in that a weir 6 higher in height than the flow hole 21 is provided on the side of the chamber 4, and a refrigerant liquid pipe 7 is connected to the lower chamber 4.
JP16958981U 1981-11-13 1981-11-13 absorption refrigerator Granted JPS5874058U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16958981U JPS5874058U (en) 1981-11-13 1981-11-13 absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16958981U JPS5874058U (en) 1981-11-13 1981-11-13 absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS5874058U JPS5874058U (en) 1983-05-19
JPS6118370Y2 true JPS6118370Y2 (en) 1986-06-04

Family

ID=29961575

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16958981U Granted JPS5874058U (en) 1981-11-13 1981-11-13 absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS5874058U (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100511940B1 (en) * 2003-12-06 2005-09-05 엘에스전선 주식회사 Apparatus for preserving differential pressure in two stage abosrption chiller
KR101951183B1 (en) * 2018-05-25 2019-02-22 박재완 Absorption water cooler and heater

Also Published As

Publication number Publication date
JPS5874058U (en) 1983-05-19

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