JP2000304369A - Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device - Google Patents

Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device

Info

Publication number
JP2000304369A
JP2000304369A JP11114283A JP11428399A JP2000304369A JP 2000304369 A JP2000304369 A JP 2000304369A JP 11114283 A JP11114283 A JP 11114283A JP 11428399 A JP11428399 A JP 11428399A JP 2000304369 A JP2000304369 A JP 2000304369A
Authority
JP
Japan
Prior art keywords
liquid
pipe
evaporator
refrigerant
refrigerant vapor
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
JP11114283A
Other languages
Japanese (ja)
Inventor
Keiichi Tanaka
啓一 田中
Hiroyuki Hisamori
弘至 久森
Hironao Tanaka
宏尚 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Zosen Corp
Osaka Gas Co Ltd
Original Assignee
Hitachi Zosen Corp
Osaka 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 Hitachi Zosen Corp, Osaka Gas Co Ltd filed Critical Hitachi Zosen Corp
Priority to JP11114283A priority Critical patent/JP2000304369A/en
Publication of JP2000304369A publication Critical patent/JP2000304369A/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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide the water-eliminating device of a direct-expansion-type evaporator by an absorption-type refrigerating device for eliminating water that remains in a heat transfer pipe in an evaporator. SOLUTION: A gas/liquid separator 31 is provided halfway in a first refrigerant vapor transfer pipe 11 for transferring refrigerant vapor being evaporated in a heat transfer pipe 1a of a direct-expansion-type evaporator 1 to an absorber 2, water contained in the evaporation vapor is separated, water staying in the gas/liquid separator 31 is sucked by an ejector 31 that is driven by absorption liquid being transferred from the absorber 2 to a reproduction part 3, and at the same time the sucked water is guided into the first refrigerant vapor transfer pipe 11 for returning to the side of the absorber 2.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、吸収式冷凍装置に
おける直膨式蒸発器の水分除去装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water removal device for a direct expansion type evaporator in an absorption refrigeration system.

【0002】[0002]

【従来の技術】吸収式冷凍装置、例えば冷凍倉庫におけ
るユニット式クーラーに使用される蒸発器としては、冷
媒液を膨張弁により減圧させて蒸発器内に導き蒸発させ
るようにした直膨式のものが使用されている。図2に示
すように、この直膨式の蒸発器51の容器本体52内に
は、吸収器、再生器、凝縮器などより構成される冷凍駆
動部53から冷媒液移送管54を介して冷媒液を導くと
ともに被冷却流体との間で熱交換を行い被冷却流体を冷
却するための伝熱管55が配置されており、またこの直
膨式の蒸発器51における伝熱管55は、上下に亘って
複数配置された水平部分が円弧部分により互いに接続さ
れた蛇行状に形成されたものであった。
2. Description of the Related Art An evaporator used in an absorption refrigeration unit, for example, a unit cooler in a refrigeration warehouse, is of a direct expansion type in which a refrigerant liquid is decompressed by an expansion valve, guided into an evaporator and evaporated. Is used. As shown in FIG. 2, the refrigerant in a container body 52 of the direct expansion type evaporator 51 is supplied from a refrigerating drive unit 53 including an absorber, a regenerator, a condenser, etc., via a refrigerant liquid transfer pipe 54. A heat transfer tube 55 for guiding the liquid and exchanging heat with the fluid to be cooled to cool the fluid to be cooled is arranged, and the heat transfer tube 55 in the direct expansion type evaporator 51 extends vertically. Thus, a plurality of horizontal portions are formed in a meandering shape connected to each other by arc portions.

【0003】[0003]

【発明が解決しようとする課題】しかし、蒸発器51に
供給される冷媒液、例えばアンモニア液には水分が混じ
っているため、アンモニア液が先に蒸発し、どうしても
水分が伝熱管55の水平部分に残ってしまい、蒸発器5
1における冷却効率が低下するという問題があった。
However, since the refrigerant liquid, for example, the ammonia liquid supplied to the evaporator 51 contains water, the ammonia liquid evaporates first and the water is inevitably removed from the horizontal portion of the heat transfer tube 55. Remains in the evaporator 5
1 has a problem that the cooling efficiency is reduced.

【0004】そこで、本発明は、蒸発器における伝熱管
内に残留する水分を除去し得る吸収式冷凍装置における
直膨式蒸発器の水分除去装置を提供することを目的とす
る。
Accordingly, an object of the present invention is to provide a water removal device for a direct expansion type evaporator in an absorption refrigerating device capable of removing moisture remaining in a heat transfer tube in the evaporator.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明の吸収式冷凍装置における直膨式蒸発器の水
分除去装置は、吸収式冷凍装置における直膨式蒸発器の
伝熱管内で蒸発された冷媒蒸気を吸収器に移送する冷媒
蒸気移送管の途中に気液分離器を設け、吸収器内の吸収
液を液移送用ポンプにより再生部に移送する吸収液移送
管の途中と、上記気液分離器にて分離された冷媒蒸気を
吸収器に移送する上記冷媒蒸気移送管の途中とを、冷媒
液抽出管にて接続するとともに、この冷媒液抽出管の途
中にエジェクタを設け、かつこのエジェクタの吸引部と
気液分離器の液取出部とを、液吸引管により接続したも
のであり、また上記水分除去装置において、蒸発器内に
設けられた伝熱管の最下方の水平部に接続される液吸引
管の一端部よりも気液分離器側の他端部が下方に位置す
るように、液吸引管を傾斜させたものである。
In order to solve the above-mentioned problems, a water removal device for a direct expansion type evaporator in an absorption refrigeration system according to the present invention is provided in a heat transfer tube of the direct expansion type evaporator in an absorption refrigeration system. A gas-liquid separator is provided in the middle of a refrigerant vapor transfer pipe for transferring the refrigerant vapor evaporated in the absorber to the absorber, and the absorption liquid in the absorber is transferred to the regenerating section by a liquid transfer pump. The refrigerant vapor transfer pipe that transfers the refrigerant vapor separated by the gas-liquid separator to the absorber is connected to the refrigerant vapor transfer pipe by a refrigerant liquid extraction pipe, and an ejector is provided in the refrigerant liquid extraction pipe. In addition, the suction part of the ejector and the liquid extraction part of the gas-liquid separator are connected by a liquid suction pipe, and in the water removing device, the lowermost horizontal heat transfer pipe provided in the evaporator is provided. Than one end of the liquid suction pipe connected to the As the other end of the liquid separator side is positioned below, it is obtained by tilting the liquid suction tube.

【0006】上記の構成によると、蒸発器の伝熱管にて
発生した水分を含む冷媒蒸気を吸収器に移送する冷媒蒸
気移送管の途中に、気液分離器を設けるとともに、この
気液分離器内の底部に溜まった水分を、液吸引管を介し
てエジェクタにより、冷媒液抽出管に吸引し、冷媒蒸気
移送管内に導くようにしているので、蒸発器の伝熱管内
に水分が残量するのを防止することができる。
According to the above construction, the gas-liquid separator is provided in the middle of the refrigerant vapor transfer pipe for transferring the refrigerant vapor containing moisture generated in the heat transfer pipe of the evaporator to the absorber. Moisture remaining in the bottom of the evaporator is sucked into the refrigerant liquid extraction pipe by the ejector via the liquid suction pipe and guided into the refrigerant vapor transfer pipe, so that water remains in the heat transfer pipe of the evaporator. Can be prevented.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態の吸収
式冷凍装置における直膨式蒸発器の水分除去装置を、図
1に基づき説明する。なお、本実施の形態における吸収
式冷凍装置としては、例えば冷凍倉庫におけるユニット
式の大型クーラー、食品のフリーザーなどに用いられる
ものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a moisture removal device for a direct expansion type evaporator in an absorption refrigeration system according to an embodiment of the present invention will be described with reference to FIG. The absorption refrigeration apparatus according to the present embodiment is used, for example, as a unit-type large cooler in a freezing warehouse, a food freezer, and the like.

【0008】まず、吸収式冷凍装置の概略構成について
説明する。この吸収式冷凍装置は、冷媒液(例えば、ア
ンモニア液)を導く伝熱管1aを有するとともにこの伝
熱管1a内で冷媒液を蒸発させてその蒸発潜熱により被
冷却流体(例えば、空気、ガスなど)を冷却する蒸発器
1と、この蒸発器1で蒸発された冷媒蒸気(例えば、ア
ンモニア蒸気)を吸収液(例えば、アンモニア水溶液)
に吸収する吸収器2と、加熱再生器3aおよび蒸留塔3
bとから成るとともに上記吸収器2で冷媒蒸気を吸収し
た吸収液を導き加熱再生を行う再生部3と、この再生部
3で再生された冷媒蒸気を凝縮させる凝縮器4と、蒸発
器1の伝熱管1a内の冷媒蒸気を吸収器2に移送する第
1冷媒蒸気移送管11と、途中に液移送用ポンプ(溶液
ポンプともいう)12を有するとともに吸収器2にて冷
媒蒸気を吸収した吸収液を再生部3に移送する吸収液移
送管13と、再生部3の蒸留塔3b側から出た冷媒蒸気
を凝縮器4に移送する第2冷媒蒸気移送管14と、凝縮
器4で凝縮された冷媒液を冷媒液取出管15を介して導
き一時的に蓄える高圧受液槽16と、途中に液移送用ポ
ンプ(還流ポンプでもある)17および膨張弁18を有
して上記高圧受液槽16に蓄えられた冷媒液を蒸発器1
の伝熱管1aに移送する冷媒液移送管19と、この冷媒
液移送管19内の冷媒液すなわち高圧受液槽16から冷
媒液の一部を再生部3の蒸留塔3b側に還流させる還流
管20と、上記第1冷媒蒸気移送管11と冷媒液移送管
19との間に設けられて凝縮器4からの冷媒液の持つ熱
を蒸発器1からの冷媒蒸気に与えて熱効率を向上させる
ための過冷却器21とが具備されている。
First, a schematic configuration of the absorption refrigeration apparatus will be described. This absorption refrigerating apparatus has a heat transfer tube 1a for guiding a refrigerant liquid (for example, an ammonia liquid), evaporates the refrigerant liquid in the heat transfer tube 1a, and uses a latent heat of the evaporation to cool the fluid (for example, air, gas, etc.). Evaporator 1 for cooling water and refrigerant vapor (e.g., ammonia vapor) evaporated by evaporator 1 for absorbing liquid (e.g., aqueous ammonia solution)
, Heat regenerator 3a and distillation column 3
b, a regenerating unit 3 for guiding and heating and regenerating the absorbing liquid having absorbed the refrigerant vapor in the absorber 2, a condenser 4 for condensing the refrigerant vapor regenerated in the regenerating unit 3, and an evaporator 1. A first refrigerant vapor transfer pipe 11 for transferring refrigerant vapor in the heat transfer tube 1a to the absorber 2, and a liquid transfer pump (also referred to as a solution pump) 12 on the way, and absorption of the refrigerant vapor absorbed by the absorber 2. An absorbent transfer pipe 13 for transferring the liquid to the regenerating section 3; a second refrigerant vapor transfer pipe 14 for transferring the refrigerant vapor from the distillation column 3b of the regenerating section 3 to the condenser 4; A high-pressure liquid receiving tank 16 for guiding and temporarily storing the refrigerant liquid through a refrigerant liquid outlet pipe 15 and a liquid transfer pump (also a reflux pump) 17 and an expansion valve 18 in the middle of the high-pressure liquid receiving tank. The refrigerant liquid stored in the evaporator 1
And a reflux pipe for returning a part of the refrigerant liquid from the high-pressure liquid receiving tank 16 to the distillation column 3b of the regenerating unit 3. 20, provided between the first refrigerant vapor transfer pipe 11 and the refrigerant liquid transfer pipe 19, in order to improve the thermal efficiency by giving the heat of the refrigerant liquid from the condenser 4 to the refrigerant vapor from the evaporator 1. Subcooler 21 is provided.

【0009】そして、上記吸収式冷凍装置には、蒸発器
1における伝熱管1a内に残留する水分を除去するため
の水分除去装置22が具備されている。すなわち、この
水分除去装置22は、過冷却器21より上流側位置の第
1冷媒蒸気移送管11の途中に設けられた気液分離器3
1と、一端部が液移送用ポンプ12より下流側位置の吸
収液移送管13の途中に接続されるとともに他端部が気
液分離器31と過冷却器21との間の第1冷媒蒸気移送
管11の途中に接続された冷媒液抽出管32と、この冷
媒液抽出管32の途中に設けられたエジェクタ33と、
上記気液分離器31の液取出口(液取出部)と上記エジ
ェクタ33の吸引口(吸引部)とを接続する液吸引管3
4と、上記冷媒液抽出管32のエジェクタ33より上流
側位置に設けられた第1開閉弁35と、上記液吸引管3
4の途中に設けられた第2開閉弁36と、これら両開閉
弁35,36を制御する制御器37とから構成されてい
る。なお、この制御器37は、例えばタイマーを有して
所定時間おきに両開閉弁35,36を開閉させる機能を
有している。
The absorption refrigeration system is provided with a water removal device 22 for removing water remaining in the heat transfer tube 1a of the evaporator 1. That is, the water removing device 22 is provided with the gas-liquid separator 3 provided in the middle of the first refrigerant vapor transfer pipe 11 at a position upstream of the subcooler 21.
And one end of the first refrigerant vapor connected between the gas-liquid separator 31 and the supercooler 21 at one end connected to the absorption liquid transfer pipe 13 at a position downstream of the liquid transfer pump 12. A refrigerant liquid extraction pipe 32 connected in the middle of the transfer pipe 11, an ejector 33 provided in the refrigerant liquid extraction pipe 32,
A liquid suction pipe 3 that connects a liquid outlet (liquid outlet) of the gas-liquid separator 31 and a suction port (suction unit) of the ejector 33.
4, a first on-off valve 35 provided at a position upstream of the ejector 33 of the refrigerant liquid extraction pipe 32, and the liquid suction pipe 3
4 comprises a second on-off valve 36 provided on the way and a controller 37 for controlling both on-off valves 35, 36. The controller 37 has, for example, a function of having a timer to open and close the on-off valves 35 and 36 at predetermined time intervals.

【0010】また、蒸発器1と気液分離器31との間に
おける第1蒸発器側冷媒蒸気移送管11aの先端部は、
気液分離器31内の上方部に開口されるとともに、上下
に亘って蛇行するように設けられた伝熱管1aの最下部
の水平部分の出口側に接続されたこの第1蒸発器側冷媒
蒸気移送管11aの基端部よりも下方となるように傾斜
されている。なお、気液分離器31から吸収器2に到る
第1吸収器側冷媒蒸気移送管11bについては、気液分
離器31の上部に接続されている。
[0010] Further, the tip of the first vaporizer side refrigerant vapor transfer pipe 11a between the evaporator 1 and the gas-liquid separator 31 is:
This first evaporator-side refrigerant vapor is opened to the upper part in the gas-liquid separator 31 and connected to the outlet side of the lowermost horizontal part of the heat transfer tube 1a provided to meander vertically. It is inclined so as to be lower than the base end of the transfer pipe 11a. The first absorber-side refrigerant vapor transfer pipe 11b extending from the gas-liquid separator 31 to the absorber 2 is connected to the upper part of the gas-liquid separator 31.

【0011】したがって、蒸発器1の伝熱管1a内にて
発生した水分を含む(水分リッチ)冷媒蒸気は気液分離
器31内に入り、ここで水分が溜められる。一方、冷媒
蒸気は、その上部から第1吸収器側冷媒蒸気移送管11
bを経て吸収器2に移送される。さらに、上記冷媒液抽
出管32による冷媒液の導入個所より下流側の第1冷媒
蒸気移送管11は、水分が自然に吸収器2まで流れるよ
うに、吸収器2側が下がるように傾斜されている。
Accordingly, the (vapor-rich) refrigerant vapor containing water generated in the heat transfer tube 1a of the evaporator 1 enters the gas-liquid separator 31, where the water is stored. On the other hand, the refrigerant vapor flows from the upper part thereof to the first absorber-side refrigerant vapor transfer pipe 11.
b and is transferred to the absorber 2. Further, the first refrigerant vapor transfer pipe 11 downstream of the refrigerant liquid introduction point by the refrigerant liquid extraction pipe 32 is inclined so that the absorber 2 side is lowered so that moisture naturally flows to the absorber 2. .

【0012】上記構成において、通常の運転時には、第
1および第2開閉弁35,36を閉じて冷媒液抽出管3
2に冷媒液が流れないようにされて、吸収冷凍サイクル
が作動される。すなわち、この運転時においては、蒸発
器1の伝熱管1a内で発生した水分リッチな冷媒蒸気は
気液分離器31内に入り、ここで水分が底部に溜められ
るとともに、冷媒蒸気は第1吸収器側冷媒蒸気移送管1
1bを経て、吸収器2に移送される。
In the above configuration, during normal operation, the first and second on-off valves 35 and 36 are closed and the refrigerant liquid extraction pipe 3 is closed.
The refrigerant refrigeration cycle is operated while preventing the refrigerant liquid from flowing to the second refrigeration cycle. That is, in this operation, the moisture-rich refrigerant vapor generated in the heat transfer tube 1a of the evaporator 1 enters the gas-liquid separator 31, where the water is stored at the bottom and the refrigerant vapor is removed by the first absorption. Refrigerant vapor transfer pipe 1
Via 1b, it is transferred to the absorber 2.

【0013】ところで、気液分離器31の底部に溜まっ
た水分は、制御器37に設けられているタイマーによ
り、所定時間おきに、第1および第2開閉弁35,36
が開かれて、エジェクタ33の吸引作用により吸収器に
移送される。すなわち、吸収液移送管13内を流れる冷
媒液が、液移送用ポンプ12の駆動力により、冷媒液抽
出管32に供給されてエジェクタ33が駆動され、気液
分離器31の底部に溜まっている水分が、液吸引管34
より冷媒液抽出管32側に吸引された後、第1冷媒蒸気
移送管11内に、正確に言えば、第1吸収器側冷媒蒸気
移送管11b内に導かれ、最終的に、吸収器2に戻され
る。
By the way, the water accumulated at the bottom of the gas-liquid separator 31 is discharged from the first and second on-off valves 35 and 36 at predetermined time intervals by a timer provided in the controller 37.
Is opened and transferred to the absorber by the suction action of the ejector 33. That is, the refrigerant liquid flowing in the absorption liquid transfer pipe 13 is supplied to the refrigerant liquid extraction pipe 32 by the driving force of the liquid transfer pump 12 to drive the ejector 33 and accumulate at the bottom of the gas-liquid separator 31. The water is absorbed in the liquid suction pipe 34
After being drawn into the refrigerant liquid extraction pipe 32 side, it is guided into the first refrigerant vapor transfer pipe 11, more precisely, into the first absorber-side refrigerant vapor transfer pipe 11 b, and finally, into the absorber 2. Is returned to.

【0014】このように、蒸発器1の伝熱管1aにて発
生した水分を含む冷媒蒸気を吸収器2に移送する第1冷
媒蒸気移送管11の途中に、気液分離器31を設けると
ともに、この気液分離器31内の底部に溜まった水分
を、液吸引管34を介してエジェクタ33により、冷媒
液抽出管32側に排出し、そして第1冷媒蒸気移送管1
1内に導くようにしているので、蒸発器1の伝熱管1a
内に水分が残るのを防止することができ、したがって蒸
発器1での冷却効率の低下を防止することができる。
As described above, the gas-liquid separator 31 is provided in the middle of the first refrigerant vapor transfer pipe 11 for transmitting the refrigerant vapor containing moisture generated in the heat transfer pipe 1a of the evaporator 1 to the absorber 2. The water collected at the bottom in the gas-liquid separator 31 is discharged to the refrigerant liquid extraction pipe 32 side by the ejector 33 via the liquid suction pipe 34, and the first refrigerant vapor transfer pipe 1
1, the heat transfer tube 1a of the evaporator 1
It is possible to prevent moisture from remaining in the inside, and thus to prevent the cooling efficiency in the evaporator 1 from decreasing.

【0015】ところで、上記実施の形態においては、制
御器37に設けられたタイマーにより、第1および第2
開閉弁35,36を、所定時間おきに開くように説明し
たが、図1の仮想線にて示すように、例えば気液分離器
31に液面計41を設けるとともにこの液面計41から
の検出信号を制御器37に入力するようになし、水分が
所定量溜まったときに、制御器37を介して、第1およ
び第2開閉弁35,36が、自動的に(場合によっては
手動でもよい)開かれる。
In the above embodiment, the first and second timers are provided by a timer provided in the controller 37.
Although the on-off valves 35 and 36 have been described to be opened at predetermined time intervals, as shown by the phantom line in FIG. The detection signal is input to the controller 37, and when a predetermined amount of water has accumulated, the first and second on-off valves 35 and 36 are automatically (in some cases manually operated) via the controller 37. Good) open.

【0016】[0016]

【発明の効果】以上のように本発明の構成によると、蒸
発器の伝熱管にて発生した水分を含む冷媒蒸気を吸収器
に移送する冷媒蒸気移送管の途中に、気液分離器を設け
るとともに、この気液分離器内の底部に溜まった水分
を、液吸引管を介してエジェクタにより、冷媒液抽出管
側に排出するとともに、冷媒蒸気移送管内に導くように
しているので、蒸発器における伝熱管内に水分が残るの
を防止することができ、したがって蒸発器における冷却
効率の低下を防止することができる。
As described above, according to the structure of the present invention, the gas-liquid separator is provided in the middle of the refrigerant vapor transfer pipe for transferring the refrigerant vapor containing moisture generated in the heat transfer pipe of the evaporator to the absorber. At the same time, the water collected at the bottom of the gas-liquid separator is discharged to the refrigerant liquid extraction pipe side by the ejector via the liquid suction pipe, and is guided to the refrigerant vapor transfer pipe. It is possible to prevent moisture from remaining in the heat transfer tube, and thus prevent a decrease in cooling efficiency in the evaporator.

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

【図1】本発明の実施の形態における吸収式冷凍装置の
概略全体構成を示す図である。
FIG. 1 is a diagram showing a schematic overall configuration of an absorption refrigeration apparatus according to an embodiment of the present invention.

【図2】従来例の吸収式冷凍装置における蒸発器の概略
構成を示す断面図である。
FIG. 2 is a sectional view showing a schematic configuration of an evaporator in a conventional absorption refrigeration apparatus.

【符号の説明】[Explanation of symbols]

1 蒸発器 1a 伝熱管 2 吸収器 3 再生部 4 凝縮器 11 第1冷媒蒸気移送管 19 冷媒液移送管 22 水分除去装置 31 気液分離器 32 冷媒液抽出管 33 エジェクタ 34 液取出管 35 第1開閉弁 36 第2開閉弁 37 制御器 DESCRIPTION OF SYMBOLS 1 Evaporator 1a Heat transfer tube 2 Absorber 3 Regeneration part 4 Condenser 11 First refrigerant vapor transfer tube 19 Refrigerant liquid transfer tube 22 Water removal device 31 Gas-liquid separator 32 Refrigerant liquid extraction tube 33 Ejector 34 Liquid extraction tube 35 First On-off valve 36 Second on-off valve 37 Controller

───────────────────────────────────────────────────── フロントページの続き (72)発明者 久森 弘至 大阪府大阪市住之江区南港北1丁目7番89 号 日立造船株式会社内 (72)発明者 田中 宏尚 大阪府大阪市住之江区南港北1丁目7番89 号 日立造船株式会社内 Fターム(参考) 3L093 AA02 BB01 BB37 DD08 HH02 JJ04 KK05 LL05 MM02  ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Hiroshi Hisamori 1-7-89 Minami Kohoku, Suminoe-ku, Osaka-shi, Osaka Inside Hitachi Zosen Corporation (72) Inventor Hironao Tanaka 1 Minami-Kohoku, Suminoe-ku, Osaka-shi, Osaka No.7-89 F-term in Hitachi Zosen Corporation (Reference) 3L093 AA02 BB01 BB37 DD08 HH02 JJ04 KK05 LL05 MM02

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】吸収式冷凍装置における直膨式蒸発器の伝
熱管内で蒸発された冷媒蒸気を吸収器に移送する冷媒蒸
気移送管の途中に気液分離器を設け、吸収器内の吸収液
を液移送用ポンプにより再生部に移送する吸収液移送管
の途中と、上記気液分離器にて分離された冷媒蒸気を吸
収器に移送する上記冷媒蒸気移送管の途中とを、冷媒液
抽出管にて接続するとともに、この冷媒液抽出管の途中
にエジェクタを設け、かつこのエジェクタの吸引部と気
液分離器の液取出部とを、液吸引管により接続したこと
を特徴とする吸収式冷凍装置における直膨式蒸発器の水
分除去装置。
1. A gas-liquid separator is provided in a refrigerant vapor transfer pipe for transferring refrigerant vapor evaporated in a heat transfer pipe of a direct expansion type evaporator to an absorber in an absorption refrigeration apparatus. A part of the refrigerant liquid transfer pipe that transfers the liquid to the regenerating unit by the liquid transfer pump and a part of the refrigerant vapor transfer pipe that transfers the refrigerant vapor separated by the gas-liquid separator to the absorber are connected to the refrigerant liquid. An absorption pipe connected with an extraction pipe, an ejector is provided in the middle of the refrigerant liquid extraction pipe, and a suction section of the ejector and a liquid extraction section of the gas-liquid separator are connected by a liquid suction pipe. Moisture removal device for direct expansion type evaporator in refrigeration system.
【請求項2】蒸発器内に設けられた伝熱管の最下方の水
平部に接続される液吸引管の一端部よりも気液分離器側
の他端部が下方に位置するように、液吸引管を傾斜して
設けたことを特徴とする請求項1記載の吸収式冷凍装置
における直膨式蒸発器の水分除去装置。
2. The liquid so that the other end on the gas-liquid separator side is located lower than one end of a liquid suction pipe connected to the lowermost horizontal portion of the heat transfer tube provided in the evaporator. The water removal device for a direct expansion type evaporator in an absorption refrigeration system according to claim 1, wherein the suction pipe is provided at an angle.
JP11114283A 1999-04-22 1999-04-22 Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device Pending JP2000304369A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11114283A JP2000304369A (en) 1999-04-22 1999-04-22 Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11114283A JP2000304369A (en) 1999-04-22 1999-04-22 Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device

Publications (1)

Publication Number Publication Date
JP2000304369A true JP2000304369A (en) 2000-11-02

Family

ID=14633970

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11114283A Pending JP2000304369A (en) 1999-04-22 1999-04-22 Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device

Country Status (1)

Country Link
JP (1) JP2000304369A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7337630B2 (en) 2005-11-10 2008-03-04 Johnson Controls Technology Company Compact evaporator for chiller application
KR100836273B1 (en) 2007-04-06 2008-06-10 한국기계연구원 Evaporating apparatus combining with expansion using the liquid medium injection type
WO2009053908A1 (en) * 2007-10-23 2009-04-30 Agecoserv S.R.L. A low-temperature absorption refrigerator
JP2019507313A (en) * 2016-01-28 2019-03-14 クール4シー エーピーエスCool4Sea Aps Absorption refrigeration and air conditioning equipment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7337630B2 (en) 2005-11-10 2008-03-04 Johnson Controls Technology Company Compact evaporator for chiller application
US7587911B2 (en) 2005-11-10 2009-09-15 York International Corporation Compact evaporator for chiller application
KR100836273B1 (en) 2007-04-06 2008-06-10 한국기계연구원 Evaporating apparatus combining with expansion using the liquid medium injection type
WO2009053908A1 (en) * 2007-10-23 2009-04-30 Agecoserv S.R.L. A low-temperature absorption refrigerator
JP2019507313A (en) * 2016-01-28 2019-03-14 クール4シー エーピーエスCool4Sea Aps Absorption refrigeration and air conditioning equipment
JP7029807B2 (en) 2016-01-28 2022-03-04 クール4シー エーピーエス Absorption refrigeration and air conditioning equipment

Similar Documents

Publication Publication Date Title
JP2000105030A (en) Two-stage cascade refrigerating device
JP3887227B2 (en) Refrigerant storage device
JPH0886530A (en) Absorption type water cooling and heating machine
JPH06201213A (en) Absorption type air conditioner
JP2000304369A (en) Device for eliminating water of direct-expansion-type evaporator in absorption-type refrigerating device
JP2002048435A (en) Absorption type refrigerating machine
JP3424385B2 (en) Adsorption refrigeration equipment and adsorption air conditioning equipment
JP2000320918A (en) Ammonia absorption freezer
JPH06207751A (en) Heat pump fitted with oil separator
JP3660493B2 (en) Absorption refrigeration system controller
JP2573030B2 (en) Non-condensable gas extraction device for absorption refrigerator
JPH10306959A (en) Absorption refrigerating machine and refrigerator provided with the machine
JP3920979B2 (en) Absorption air conditioner control device
JP3920997B2 (en) Absorption air conditioner control device
JP2503752B2 (en) Adsorption refrigerator
JPH11281187A (en) Absorption refrigerating machine
JPS63204080A (en) Absorption refrigerator
JPH0719645A (en) Absorption refrigeranting machine
JPH058458Y2 (en)
JP2000002472A (en) Absorptive freezer
JPS6152902B2 (en)
JPH0238054U (en)
JPH0730974B2 (en) Extraction device for absorption refrigerator
JP2000304371A (en) Defroster of direct-inflation-type evaporator in absorption-type refrigeration device
JP2002147886A (en) Absorption refrigerating machine