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JP2826631B2 - Heat exchange device for direct expansion refrigeration system - Google Patents

Heat exchange device for direct expansion refrigeration system

Info

Publication number
JP2826631B2
JP2826631B2 JP6137719A JP13771994A JP2826631B2 JP 2826631 B2 JP2826631 B2 JP 2826631B2 JP 6137719 A JP6137719 A JP 6137719A JP 13771994 A JP13771994 A JP 13771994A JP 2826631 B2 JP2826631 B2 JP 2826631B2
Authority
JP
Japan
Prior art keywords
refrigerant
heat exchanger
heat exchange
liquid
temperature
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 - Lifetime
Application number
JP6137719A
Other languages
Japanese (ja)
Other versions
JPH07310957A (en
Inventor
忠源 楊
進鴻 羅
▲ゆー▼▲くん▼ 洪
茂勇 翁
燿祖 胡
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.)
KOGYO GIJUTSU KENKYUIN
Original Assignee
KOGYO GIJUTSU KENKYUIN
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 KOGYO GIJUTSU KENKYUIN filed Critical KOGYO GIJUTSU KENKYUIN
Priority to JP6137719A priority Critical patent/JP2826631B2/en
Publication of JPH07310957A publication Critical patent/JPH07310957A/en
Application granted granted Critical
Publication of JP2826631B2 publication Critical patent/JP2826631B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/05Compression system with heat exchange between particular parts of the system

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

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、一種の直接膨張式冷凍
系統に関し、冷水機などの流体冷却装置に応用される直
接膨張式の冷凍システムであって、並びにその他の類似
の冷却動作を発生するものに活用されるものに関する。
BACKGROUND OF THE INVENTION The present invention relates to a type of direct expansion refrigeration.
The system is directly applied to fluid cooling devices such as water coolers.
Contact expansion refrigeration systems, as well as other similar
The present invention relates to a device that is used to generate a cooling operation.

【0002】[0002]

【従来の技術】流体を冷却する装置に応用されるシステ
ムには、満液式(Liquid over−feedi
ng)と直接膨張式の2種があり、その中、満液式のシ
ステムは比較的複雑である、このため冷却効率が特別に
要求される製品を除いては、直接膨張式が採られてい
る。直接膨張式システムは、満液式のものより簡単では
あるが、冷却効率が低く、このため、簡単でしかも高い
冷却効率を有す冷水機やそれに類似の製品に使用できる
冷凍システムが求められていた。
2. Description of the Related Art A system applied to a device for cooling a fluid is disclosed.
The system is filled with liquid (Liquid over-feedi
ng) and a direct expansion type.
The stem is relatively complex, which results in extra cooling efficiency
Except for required products, direct inflatable
You. A direct inflatable system is easier than a full one
However, the cooling efficiency is low and therefore simple and high
Can be used for water coolers with cooling efficiency and similar products
There was a need for a refrigeration system.

【0003】図1に示されるのは、一種の伝統的且つ典
型的な冷水機の冷凍システムであり、これは一つの感温
式膨張弁(5)と、一つの該膨張弁(5)に連接する蒸
発器 (1)、蒸発器(1)の冷媒出口(13)に連接す
る一つの圧縮機(3)、及び圧縮機(3)と膨張弁
(5)に連接する熱交換器(4)を包括する。そのうち
膨張弁(5)の温度センサー(51)例えば感温球は蒸
発器(1)の出口(13)付近に設けられ、検出する蒸
発器(1)の過熱温度により、膨張弁(5)を経て冷媒
の流量を制御する。膨張弁(5)は、冷媒管(47)中
の液態冷媒を蒸発器(1)内へと導入し、液態冷媒は蒸
発過程で冷水(このシステムが冷水機に応用される場
合)の熱を吸収して冷水の温度を下降させる。これによ
り、蒸発器(1)を通過した水は冷却されて温度が下が
る。相対的に、液態冷媒は、冷媒管(12)は水の熱を
吸収し、蒸発器(1)の出口に至る時、液態冷媒は既に
完全に蒸発且つ過熱している。温度センサー(51)の
作用により、上述したように蒸発器(1)の出口(1
3)の温度を検出し、さらに液態冷媒が膨張弁(5)を
通過する流量を調整する。これは主に、蒸発器(1)出
口の冷媒が完全に蒸発且つ過熱されていないと、液態冷
媒が吸入管から引き入れられ、これが圧縮機(3)に送
られると圧縮機(3)内部を損壊するためである。
FIG . 1 shows a kind of traditional and classical
This is a chiller system for a typical water cooler,
-Type expansion valve (5) and a steam valve connected to one expansion valve (5).
The generator (1) is connected to the refrigerant outlet (13) of the evaporator (1).
One compressor (3), and a compressor (3) and an expansion valve
A heat exchanger (4) connected to (5) is included. Among them
The temperature sensor (51) of the expansion valve (5), for example,
A steam detector is provided near the outlet (13) of the generator (1) to detect steam.
Due to the superheated temperature of the generator (1), the refrigerant passes through the expansion valve (5)
To control the flow rate. The expansion valve (5) is in the refrigerant pipe (47).
Liquid refrigerant is introduced into the evaporator (1), and the liquid refrigerant is vaporized.
Chilled water during the power generation process (when this system is applied to chilled water
B) to reduce the temperature of the cold water. This
The water that has passed through the evaporator (1) is cooled and the temperature decreases.
You. In comparison, the liquid refrigerant is such that the refrigerant pipe (12) heats water.
When absorbing and reaching the outlet of the evaporator (1), the liquid refrigerant is already
It is completely evaporated and overheated. Temperature sensor (51)
By the action, as described above, the outlet (1) of the evaporator (1)
The temperature of 3) is detected, and the liquid refrigerant further operates the expansion valve (5).
Adjust the flow through. This is mainly due to the evaporator (1)
If the refrigerant in the mouth is not completely evaporated and heated,
The medium is drawn from the suction pipe and sent to the compressor (3).
This is to cause damage to the inside of the compressor (3) when it is damaged.

【0004】周知のように、気態の熱伝導係数は液態と
気態の両態混合体より低く、また気態の冷媒の熱伝導係
数は飽和冷媒の熱伝導係数より低い。そのため、もし蒸
発器が完全には冷媒を気態かつ過熱しなければ、熱交換
率を上げることができるはずである。これが、伝統的な
直膨式冷凍システムにあって長い間克服しなければなら
ない問題であった。
[0004] As is well known, the thermal conductivity coefficient of the gaseous state is different from that of the liquid state.
Lower than the gaseous mixture, and the heat conduction of the gaseous refrigerant
The number is lower than the heat transfer coefficient of the saturated refrigerant. Therefore, if steam
If the generator is not completely gaseous and does not overheat the refrigerant, heat exchange
You should be able to increase the rate. This is the traditional
The direct expansion refrigeration system has to be overcome for a long time
There was no problem.

【0005】[0005]

【発明が解決しようとする問題】本発明は、一種の液態
/気態分離器を直接蒸発器中の冷煤の出口に連接し、蒸
発器の冷媒を完全に気化させずに熱交換率を高める流体
冷凍システムを提供することを課題とする。
SUMMARY OF THE INVENTION The present invention provides a kind of liquid state.
/ Connect the gas separator directly to the outlet of the cold soot in the evaporator,
Fluid that increases the heat exchange rate without completely vaporizing the refrigerant of the generator
It is an object to provide a refrigeration system.

【0006】本発明は次に、特殊な熱交換装置(hea
t exchange device)を設けて圧縮機
が放出する高圧気態冷媒(refrigerant v
apor)を熱交換装置の上半部で冷却して液態とし、
別に該熱交換装置の下半部で液態/気態分離器(vap
or/liquid separator)から送られ
る含油液態度冷媒(oil−rich liquid
refrigerant)を該熱交換装置の管内で蒸発
させ、前述の冷却した液態の冷媒を熱交換装置のハウジ
ング内で二次冷却(subcool)する、流体冷凍シ
ステムを提供することを課題とする。
[0006] The present invention is next based on a special heat exchange device (hea).
t exchange device)
High-pressure gaseous refrigerant (refrigerant v)
apor) is cooled in the upper half of the heat exchanger to a liquid state,
Separately, a liquid / gas separator (vap) is provided in the lower half of the heat exchanger.
or / liquid separator)
Oil-rich liquid refrigerant (oil-rich liquid)
evaporate in the tubes of the heat exchanger
And the cooled liquid refrigerant described above is housed in a heat exchanger.
Fluid refrigeration system for subcooling
The task is to provide a stem.

【0007】本発明はさらに、一つの温度センサー(t
emperature sensor)を冷凍システム
中の膨張弁(expansion valve)に設
け、これにより熱交換装置の二次熱交換を経た含油液態
度冷媒の温度を検出することを課題とする。
The present invention further provides a single temperature sensor (t
emperature sensor) refrigeration system
The expansion valve (expansion valve)
Oil-impregnated liquid after passing through the secondary heat exchange of the heat exchanger.
It is an object to detect the temperature of a refrigerant.

【0008】[0008]

【課題を解決するための手段】本発明は、流体冷却装置
或いはその他の冷却設備に応用され、 一つの感温式の膨
張弁で、一つの蒸発器から送られた冷媒を、液態/気態
両態の状態に保持し、 蒸発器の出口の飽和液態/気態混
合冷媒を分離し、飽和気態冷媒と含油液態冷媒となし、
飽和気態冷媒を一つの圧縮機の吸気管に送り、並びに含
油液態冷媒を一つの熱交換装置に送り、 熱交換装置を経
た含油液態冷媒を蒸発し、過熱蒸気とし、並びに圧縮機
の吸気管へと送り、 圧縮機により圧縮された高圧気態冷
媒を熱交換装置を経て二次冷却された液態冷媒とし、そ
の後、上記感温式の膨張弁へと送る。
SUMMARY OF THE INVENTION The present invention provides a fluid cooling device.
Or it is applied to other cooling equipment, Rise of one temperature-sensitive
With the expansion valve, the refrigerant sent from one evaporator is converted into liquid / air state
Maintain both states, and mix saturated liquid / gas at the evaporator outlet.
The combined refrigerant is separated, and no saturated gaseous refrigerant and no oil-containing liquid refrigerant,
Send the saturated gaseous refrigerant to the intake pipe of one compressor,
The oil-liquid refrigerant is sent to one heat exchange device and passed through the heat exchange device.
Evaporates oil-containing liquid refrigerant into superheated steam, and
Feeding into the intake pipe, a high pressure Kitaihiya compressed by the compressor
The medium is a liquid refrigerant that has been secondarily cooled through a heat exchanger, and
After that, it is sent to the above-mentioned temperature-sensitive expansion valve.

【0009】本発明は、一つの蒸発器で、一つの冷媒入
口と一つの冷媒出口を有し、冷媒に該蒸発器中で液態/
気態両態共存の状態で熱交換を進行させるものと、 一つ
の液態/気態分離器で、一つの気態出口と一つの液態出
口と、一つの入口を有し、そのうち入口は上述の蒸発器
の出口と連接するものと、 一つの圧縮機で、一つの入口
と一つの出口を有し、そのうち入口はそれぞれ上 述の液
態/気態分離器の気態出口と、熱交換装置の低圧気態冷
媒出口に連接するものと、を有し、前述の熱交換装置
は、 一つの低圧液態冷媒入口で、前述の液態/気態分離
器の液態出口に連接するものと、 一つの低圧気態冷媒入
口で、前述の圧縮機の入口に連接するものと、 一つの高
圧二次冷却液態冷媒出口で、前述の膨張弁の入口に連接
するものと、を有し、前述の熱交換装置の低圧液態冷媒
入口は、熱交換装置の低圧気態冷媒出口に連接し、二次
熱交換器を形勢し、該熱交換装置を経た高圧気態冷媒入
口の流体は、二次熱交換器と熱交換を進行し、その後熱
交換装置の高圧二次冷却液態冷媒出口から前述の膨張弁
に送る。
According to the present invention, one evaporator is used to supply one refrigerant.
It has a port and one refrigerant outlet, and the refrigerant has a liquid /
As to advance the heat exchanger in gaseous both states coexisting, one
Liquid / gas separator with one gas outlet and one liquid outlet
It has a mouth and one inlet, of which the inlet is the evaporator described above
And one compressor, one inlet
Has one outlet and of which the inlet liquid respectively on predicate
Air outlet of the air / air separator and low pressure air cooling of the heat exchanger
A heat exchanger connected to the medium outlet,
Is the low-pressure liquid refrigerant inlet, and the liquid / gas separation described above
And one low-pressure gaseous refrigerant
At the mouth, one connected to the inlet of the aforementioned compressor and one
The outlet of the secondary cooling liquid refrigerant is connected to the inlet of the expansion valve described above.
And the low-pressure liquid refrigerant of the heat exchanger described above.
The inlet is connected to the low-pressure gaseous refrigerant outlet of the heat exchanger,
A heat exchanger is formed, and a high-pressure gaseous refrigerant that has passed through the heat exchanger is introduced.
The fluid in the mouth undergoes heat exchange with the secondary heat exchanger and then heat
From the high-pressure secondary cooling liquid refrigerant outlet of the exchange unit to the expansion valve
Send to

【0010】上記熱交換装置は二次熱交換器の上に位置
する一つの一次熱交換器を包括し、該一次熱交換器中に
は多数の迂回する冷却水管を有し、且つ上述の二次熱交
換器には多数の冷媒管を有して液態/気態分離器の液態
冷媒の通過に供される。
[0010] The above heat exchanger is located above the secondary heat exchanger.
One primary heat exchanger to be included in the primary heat exchanger
Has a number of bypass cooling water pipes and the secondary heat exchange described above.
The exchanger has a number of refrigerant pipes and the liquid state of the liquid / gas state separator.
Provided for the passage of refrigerant.

【0011】上記膨張弁の温度センサーは、二次交換器
の出口に設け、該出口の温度を検出して上述の膨張弁に
フィードバックして冷媒の流量を調整させる。
The temperature sensor for the expansion valve is a secondary exchanger.
Is provided at the outlet, and the temperature of the outlet is detected to connect the above-described expansion valve.
Feedback is made to adjust the flow rate of the refrigerant.

【0012】本発明の上記蒸発器は一つの容器中に設け
られる。
The evaporator of the present invention is provided in one container.
Can be

【0013】[0013]

【作用】本発明は、蒸発器の冷媒管を経て、その管路
(conduit)に先ず液態/気態分離器を通過させ
た後、圧縮機に連接し、これにより蒸発器内の冷媒が液
態/気態両相の共存状態の下で熱交換を進行する。そし
て一つの特別設計の熱交換器の一端を、蒸発器の前に連
接する膨張弁に連接し、且つもう一端は圧縮機の出口管
に連接する。該熱交換器中には、伝統的な熱交換装置中
の冷却水管構造を設ける外、一つの二次熱交換器と液態
/気態分離器の含油液態冷媒管を連接し、これにより低
圧含油液態冷媒を気化し、こうして圧縮機から送られる
高圧気態冷媒 をず熱交換装置中の冷却水管と熱交換して
冷却して高圧液態冷媒とし、さらに熱交換器底部の二次
熱交換を経て冷えた液態冷媒とする。
According to the present invention, the refrigerant pipe of the evaporator passes through the pipe.
(Conduit) first through a liquid / gas separator
After that, it is connected to the compressor, which causes the refrigerant in the evaporator to
Heat exchange proceeds under the coexistence state of both gaseous and gaseous phases. Soshi
Connect one end of one specially designed heat exchanger before the evaporator.
The other end is connected to the expansion valve and the other end is the outlet pipe of the compressor.
Connect with In the heat exchanger, the traditional heat exchanger
In addition to providing a cooling water pipe structure, one secondary heat exchanger and liquid state
/ Connect the oil-containing liquid refrigerant pipe of the gaseous separator,
Vaporizes the oil-impregnated liquid refrigerant and is thus sent from the compressor
Exchanging heat with the cooling water pipe in the heat exchanger without high-pressure gas refrigerant
Cooled to a high-pressure liquid refrigerant, and further cooled to the secondary
A liquid refrigerant cooled through heat exchange.

【0014】[0014]

【実施例】本発明は、冷水器やその他の冷却を応用した
類似物に応用することができる。図2に示されるよう
に、容器(11)の入口管(111)と出口管(11
2)は、どのように容器中の蒸発器(1)と熱交換を進
行する物質、例えば水、空気等を受け取るかを示すため
に表示し、該物質は、入口管(111)から蒸発器
(1)内に進入し、冷媒管(12)中の冷媒と熱交換を
進行し、その後出口管(112)から排出される。この
ため、容器(11)は冷水器、或いは気態容器、或いは
その他の適当な流体を保存或いは通過させるための熱交
換容器とする。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is applied to water coolers and other cooling systems.
It can be applied to analogs. As shown in FIG.
In addition, the inlet pipe (111) and the outlet pipe (11) of the container (11)
2) How to promote heat exchange with the evaporator (1) in the vessel
To indicate whether it receives materials to be carried out, such as water, air, etc.
And the substance is supplied from the inlet pipe (111) to the evaporator.
(1) and exchange heat with the refrigerant in the refrigerant pipe (12).
And then discharged from the outlet pipe (112). this
Therefore, the container (11) is a water cooler, an air container, or
Heat exchange to preserve or pass other suitable fluids
Replacement container.

【0015】本発明のシステムと伝統的な直接膨張式蒸
発器システムの類似する所は、同様に、一つの蒸発器を
有し、その内部に冷媒管(12)と、冷媒管(12)と
熱交換を進行できる物質の通道或いは容器を有すること
である。熱交換を進行する物質は、前に述べた通り、入
口管(111)から進入した後、出口管(112)から
排出される。感温式膨張弁(5)の出口端を蒸発器
(1)の冷媒管の入口端を連接する。熱交換装置(4)
を膨張弁(5)の入口端に連接し、一つの圧縮機(3)
を熱交換装置(4)と蒸発器(1)の間に配置し、且つ
それぞれ管路で熱交換装置(4)と蒸発器(1)に連接
する。
The system of the present invention and a traditional direct expansion steam
A similar part of the generator system is likewise using one evaporator
And a refrigerant pipe (12) and a refrigerant pipe (12) therein.
Have a passage or container for a substance that can proceed with heat exchange
It is. Substances that proceed with heat exchange should be
After entering from the mouth pipe (111), from the exit pipe (112)
Is discharged. Evaporator at the outlet end of the temperature-sensitive expansion valve (5)
The inlet end of the refrigerant pipe of (1) is connected. Heat exchange device (4)
Is connected to the inlet end of the expansion valve (5), and one compressor (3)
Is disposed between the heat exchange device (4) and the evaporator (1), and
Connected to the heat exchange device (4) and evaporator (1) via respective pipelines
I do.

【0016】本発明のシステムはさらに一つの液態/気
態分離器(2)を有し、これは蒸発器(1)の冷媒管
(12)の出口管路(13)と圧縮機(3)の間に連接
する。該液態/気態分離器(2)は一つの気態冷媒出口
管(21)(Segment)と一つの含油液態冷媒出
口管(22)を有する。そのうち気態冷媒出口管(2
1)は圧縮機(3)の吸気管(31)と溶接し、含油液
態冷媒出口管(22)は熱交換装置(4)中の二次熱交
換器(43)の入口管(45)に連接する。このように
して、含油液態冷媒を直接圧縮機(3)の吸気管(3
1)中に送ることなく、また蒸発器(1)中の冷媒管
(12)内の冷媒を必ずしも過熱する必要なく、 只液態
/気態の両態を呈するだけで熱伝導率を高めることがで
きる。
The system of the present invention further comprises one liquid / gas
State separator (2), which is a refrigerant pipe of the evaporator (1).
Connection between outlet line (13) of (12) and compressor (3)
I do. The liquid / gas separator (2) has one gaseous refrigerant outlet
Pipe (21) (Segment) and one oil-containing liquid refrigerant outlet
It has a mouth tube (22). The gaseous refrigerant outlet pipe (2
1) is welded to the intake pipe (31) of the compressor (3),
The refrigerant outlet pipe (22) is connected to the secondary heat exchanger in the heat exchanger (4).
It is connected to the inlet pipe (45) of the exchanger (43). in this way
Then, the oil-containing liquid refrigerant is directly transferred to the intake pipe (3) of the compressor (3).
1) Refrigerant pipe without passing into and in the evaporator (1)
(12) always without the need to superheat the refrigerant in, Tadaekitai
/ It is possible to increase thermal conductivity just by showing both air
Wear.

【0017】[0017] 図2と図3に示されるように、本発明のシAs shown in FIG. 2 and FIG.
ステム中の特殊な熱交換装置(4)は、一つの一次熱交A special heat exchange device (4) in the stem provides one primary heat exchange
換器(41)と該一次熱交換器(41)の底部に位置すExchanger (41) and the bottom of the primary heat exchanger (41).
る二次熱交換器(43)を有し、そのうち一次熱交換器Secondary heat exchanger (43), of which the primary heat exchanger
(41)は伝統的な熱交換器と同様に多数の迂回する冷(41) has a number of bypass cooling systems similar to traditional heat exchangers
却水管(42)を有し(図2中では只1本をもって代表It has a drainage pipe (42).
とする)、これにより圧縮機(3)の出口管(32)か), So that the outlet pipe (32) of the compressor (3)
ら送りだされる高圧気態冷媒を、一次熱交換器(41)The high-pressure gaseous refrigerant sent out from the primary heat exchanger (41)
中に進入させて冷却水管(42)と熱交換を進行させ、And heat exchange proceeds with the cooling water pipe (42).
液態/気態両態共存の冷媒とし、その後、さらに二次熱Refrigerant that coexists in both liquid and gaseous state
交換器(43)中に進入させ第2次熱交換を進行する。The second heat exchange proceeds by entering the heat exchanger (43).
二次熱交換器(43)中には多数の冷媒管(44)(図In the secondary heat exchanger (43), a number of refrigerant pipes (44) (FIG.
2中では只1本をもって代表とする)が設けられ、液態2 only one is represented), and the liquid state
/気態分離器(2)から送られる含油液態冷媒を、入口/ The oil-containing liquid refrigerant sent from the gas separator (2)
管(45)から各冷媒管(44)中へと送り入れ、二次The pipes (45) are fed into each refrigerant pipe (44),
熱交換器(43)中で液態/気態両態共存の冷媒と熱交Heat exchange with refrigerant in both liquid and gaseous state in heat exchanger (43)
換を進行し、これにより冷媒管(44)中の液態冷媒をThe liquid refrigerant in the refrigerant pipe (44).
気化した後、出口管(46)より圧縮機(3)の吸気管After vaporization, the suction pipe of the compressor (3) is passed through the outlet pipe (46).
(31)に送り入れ、同時に液態/気態両態共存の冷媒Refrigerant that is sent to (31) and simultaneously coexists in both liquid and gaseous state
を再度冷却して液態とし、その後、管路(47)を経てIs cooled again to a liquid state, and then is passed through a pipe (47).
膨張弁(5)へと送る。Send to expansion valve (5).

【0018】[0018] 本発明のシステム中の膨張弁(5)は、そThe expansion valve (5) in the system of the present invention
の温度センサー(51)、例えば感温球或いはその他等Temperature sensor (51), for example, thermo bulb or others
しい効果を有するもの、を使用して熱交換装置(4)のUsing a heat exchanger (4)
二次熱交換器(43)の出口管(46)の温度を検出Detects the temperature of the outlet pipe (46) of the secondary heat exchanger (43)
し、もって該温度の変化により膨張弁(5)の冷媒流量Then, the change in the temperature causes the refrigerant flow rate of the expansion valve (5) to change.
を調節する。一般的には、温度が高くなるほど冷媒の流Adjust Generally, the higher the temperature, the more the refrigerant flows.
量は大きくなる、反対の場合もまたしかりである。The amount is larger, and vice versa.

【0019】[0019]

【発明の効果】本発明の冷凍系統中では蒸発器内の冷媒
は過熱して完全に蒸発させる必要がなく、液態/気態両
態共存の状態の下で熱交換を進行でき、もって熱交換率
を高めることができる。本発明は液態冷媒が蒸発器を経
た後に直接圧縮機中に進入するのを防止し、且つ液態/
気態分離器中の液態冷媒を熱交換装置での熱交換を経て
気態とした後、さらに圧縮機中へと送り、このような液
態冷媒気化の過程は、同時に圧縮機の送りだす高圧気態
冷媒に速やかに放熱させて液態とする。本発明の膨張弁
に送る液態冷媒は、二次の熱交換を経るため、伝統的な
冷楳温度より低い温度となる。この結果、蒸発器の熱交
換率を高めるのに有効である。
The refrigerant in the evaporator in the refrigeration system of the present invention
Does not need to be overheated and completely evaporated;
Can proceed under the condition of coexistence
Can be increased. In the present invention, the liquid refrigerant passes through an evaporator.
To prevent direct entry into the compressor after
The liquid refrigerant in the gaseous separator undergoes heat exchange in a heat exchanger.
After being in a gaseous state, it is sent further into the compressor,
The refrigerant vaporization process is based on the high-pressure
The refrigerant is immediately radiated to be in a liquid state. Expansion valve of the present invention
Liquid refrigerant is sent to the traditional heat exchanger through secondary heat exchange.
The temperature will be lower than the cold temperature. As a result, heat exchange of the evaporator
It is effective to increase the conversion rate.

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

【図1】従来の直接膨張式蒸発器のシステム図である。FIG. 1 is a system diagram of a conventional direct expansion type evaporator.

【図2】本発明の直接膨張式蒸発器のシステム図であ
る。
FIG. 2 is a system diagram of the direct expansion type evaporator of the present invention.

【図3】FIG. 3 本発明の上記図2の3−3線における断面図でFIG. 3 is a cross-sectional view taken along line 3-3 of FIG. 2 of the present invention.
ある。is there.

【符号の説明】 (1)蒸発器 (2)液態/気態分離器 (3)圧縮機 (4)熱交換装置 (5)膨張弁 (11)容器
(12)冷媒管(13)出口管路 (21)気態冷媒出口管(22)含油液態冷媒出口管 (31)吸気管 (3
2)出口管 (41)一次熱交換器 (42)冷却水管 (43)二
次熱交換器 (44)冷媒管 (45)入口管 (46)出口管
(47)管路 (51)温度センサー (111)入口管 (112)
出口管
[Description of Signs ] (1) Evaporator (2) Liquid / gas state separator (3) Compressor (4) Heat exchange device (5) Expansion valve (11) Container
(12) Refrigerant tube (13) Outlet line (21) Air- state refrigerant outlet tube ( 22) Oil- containing liquid-state refrigerant outlet tube (31) Intake tube (3)
2) Outlet pipe (41) Primary heat exchanger (42) Cooling water pipe (43) Secondary heat exchanger (44) Refrigerant pipe (45) Inlet pipe (46) Outlet pipe
(47) Pipe (51) Temperature sensor (111) Inlet pipe (112)
Outlet pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 胡 燿祖 台湾新竹縣竹東鎮中興路四段195號64館 (56)参考文献 特開 平1−277175(JP,A) 実開 平2−41059(JP,U) (58)調査した分野(Int.Cl.6,DB名) F25B 1/00 331 F25B 39/04────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hu Yongzhu, No. 195, No. 195, Fourth Section, Nakagyo Road, Bhudong Township, Hsinchu County, Taiwan (56) References JP-A 1-277175 (JP, A) 41059 (JP, U) (58) Field surveyed (Int. Cl. 6 , DB name) F25B 1/00 331 F25B 39/04

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一種の直接膨張式冷凍システムの熱交換
装置とされて、中空の本体を有し、その内部に一次熱交
換器41と、該一次熱交換器41の下に位置する二次熱
交換器43が設けられ、該一次熱交換器41に複数の冷
却管が設けられ、該二次熱交換器43に液体/気体分離
器の液態冷媒を通過させる複数の冷媒管が設けられ、該
本体の上方に圧縮機3より供給される高温高圧気態冷媒
が引き込まれ、該一次熱交換器41が先に高温高圧気態
冷媒を冷却して高温液態冷媒となし、該二次熱交換器4
3が高温液態冷媒中に浸されて該二次熱交換器43を通
過する液態冷媒が潜熱を吸収して気化した後に圧縮機3
に回送され、且つ熱交換装置本体内の高温液態冷媒が潜
熱を放出して温度が下がった後に膨張弁5に送られるよ
うにしてあり、以上の構成からなる直接膨張式冷凍シス
テムの熱交換装置。
1. A heat exchange device for a direct expansion refrigeration system having a hollow main body, a primary heat exchanger 41 therein, and a secondary heat exchanger located below the primary heat exchanger 41. The heat exchanger 43 is provided, the primary heat exchanger 41 is provided with a plurality of cooling pipes, and the secondary heat exchanger 43 is provided with a plurality of refrigerant pipes for passing the liquid refrigerant of the liquid / gas separator, The high-temperature and high-pressure gaseous refrigerant supplied from the compressor 3 is drawn into the upper part of the main body, and the primary heat exchanger 41 first cools the high-temperature and high-pressure gaseous refrigerant into a high-temperature liquid refrigerant, and the secondary heat exchange. Vessel 4
After the liquid refrigerant 3 is immersed in the high-temperature liquid refrigerant and the liquid refrigerant passing through the secondary heat exchanger 43 absorbs latent heat and evaporates, the compressor 3
And the high-temperature liquid refrigerant in the heat exchange device main body emits latent heat to be sent to the expansion valve 5 after the temperature has dropped, and the heat exchange device of the direct expansion refrigeration system having the above configuration .
【請求項2】 前記冷却管が迂回する冷却水管とされた
ことを特徴とする、請求項1に記載の直接膨張式冷凍シ
ステムの熱交換装置。
2. The heat exchange device for a direct expansion refrigeration system according to claim 1, wherein the cooling pipe is a bypass cooling water pipe.
【請求項3】 前記二次熱交換器43の出口に温度変化
を検出する装置が設けられたことを特徴とする、請求項
1に記載の直接膨張式冷凍システムの熱交換装置。
3. The heat exchange device for a direct expansion refrigeration system according to claim 1, wherein a device for detecting a temperature change is provided at an outlet of the secondary heat exchanger 43.
JP6137719A 1994-05-17 1994-05-17 Heat exchange device for direct expansion refrigeration system Expired - Lifetime JP2826631B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6137719A JP2826631B2 (en) 1994-05-17 1994-05-17 Heat exchange device for direct expansion refrigeration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6137719A JP2826631B2 (en) 1994-05-17 1994-05-17 Heat exchange device for direct expansion refrigeration system

Publications (2)

Publication Number Publication Date
JPH07310957A JPH07310957A (en) 1995-11-28
JP2826631B2 true JP2826631B2 (en) 1998-11-18

Family

ID=15205233

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6137719A Expired - Lifetime JP2826631B2 (en) 1994-05-17 1994-05-17 Heat exchange device for direct expansion refrigeration system

Country Status (1)

Country Link
JP (1) JP2826631B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10220909A (en) 1996-12-03 1998-08-21 Komatsu Ltd Fluid temperature control device
CN102062491A (en) * 2010-12-16 2011-05-18 张家港市江南利玛特设备制造有限公司 Triple type condensation device for ship air conditioner
CN107388628A (en) * 2017-09-12 2017-11-24 广东纽恩泰新能源科技发展有限公司 A kind of heat pump circulating system suitable for low temperature environment

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5846070U (en) * 1981-09-22 1983-03-28 株式会社熊谷製作所 Refrigeration equipment
JPH01277175A (en) * 1988-04-27 1989-11-07 Nippon Denso Co Ltd Refrigerating cycle
JPH0241059U (en) * 1988-09-12 1990-03-20

Also Published As

Publication number Publication date
JPH07310957A (en) 1995-11-28

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