JPS599039B2 - gas cooling device - Google Patents
gas cooling deviceInfo
- Publication number
- JPS599039B2 JPS599039B2 JP4642877A JP4642877A JPS599039B2 JP S599039 B2 JPS599039 B2 JP S599039B2 JP 4642877 A JP4642877 A JP 4642877A JP 4642877 A JP4642877 A JP 4642877A JP S599039 B2 JPS599039 B2 JP S599039B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- repellent liquid
- air
- repellent
- brine
- 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
Description
【発明の詳細な説明】
この発明は、冷凍装置の寒冷と熱交換して冷却された撥
水液を充てん層に散布し、充てん物表面における撥水液
膜と空気との熱交換によって、霜の生成を抑制しつつ低
温の空気等を得る気体冷却装置であり特に業務用冷蔵庫
に適したものである。Detailed Description of the Invention This invention sprays a water-repellent liquid that has been cooled by heat exchange with the cold temperature of a refrigeration device onto a filling layer, and prevents frost by exchanging heat between the water-repellent liquid film on the surface of the filling material and the air. This is a gas cooling device that obtains low-temperature air while suppressing the generation of air, and is particularly suitable for commercial refrigerators.
従来の低温用空気冷却器としては、プレートフィン形の
熱交換器の管内に冷媒を流し、管外面とプレートフィン
面で空気と熱交換させ、空気を冷却する構成が通常であ
る。Conventional low-temperature air coolers usually have a configuration in which a refrigerant is passed through the tubes of a plate-fin type heat exchanger, and the air is cooled by exchanging heat with the air on the tube outer surface and plate fin surface.
この形式の空気冷却器では空気温度を5℃以下に冷却す
る場合、伝熱面はO℃以下になるのが普通である。In this type of air cooler, when the air temperature is cooled to 5°C or less, the heat transfer surface is usually 0°C or less.
この条件下で且つ空気の露点が伝熱面温度より高い場合
には空気中の水分が伝熱面上に凝固して霜層が形成する
。Under these conditions and when the dew point of the air is higher than the temperature of the heat transfer surface, moisture in the air solidifies on the heat transfer surface to form a frost layer.
この霜層は漸次成長し通風抵抗が増大し同時に空気と冷
媒間の熱抵抗を増大させるので、これらの空気冷却器は
除霜機構を備え、一定時間毎に空気冷却器の運転を停止
し除霜運転を行わなければならない。This frost layer gradually grows, increasing ventilation resistance and at the same time increasing the thermal resistance between the air and the refrigerant. Therefore, these air coolers are equipped with a defrosting mechanism that stops the operation of the air cooler at regular intervals to defrost the air. Frost operation must be carried out.
除霜運転を避け空気冷却器を連続的に運転する方法とし
て熱交換器にブラインとして用いられているエチレング
リコールを散布し霜の生成を阻止するブライン散布方式
がある。As a method of continuously operating an air cooler while avoiding defrosting operation, there is a brine spraying method in which ethylene glycol, which is used as brine, is sprayed onto the heat exchanger to prevent frost formation.
この方式は、空気冷却器、冷凍装置、ブライン濃縮装置
より成る。This system consists of an air cooler, a refrigeration system, and a brine concentrator.
空気冷却器の熱交換器に散布されたブラインは、冷凍装
置よりの冷媒によって冷却された熱交換器の伝熱面上で
冷却され、同時に被冷却空気と熱交換して空気を冷却す
る。The brine spread over the heat exchanger of the air cooler is cooled on the heat transfer surface of the heat exchanger cooled by the refrigerant from the refrigeration system, and at the same time exchanges heat with the air to be cooled to cool the air.
ブラインはエチレングリコール等の水溶液であり、吸水
性があるため、この熱交換過程で水分を吸収する。Brine is an aqueous solution of ethylene glycol or the like and has water absorption properties, so it absorbs water during this heat exchange process.
濃縮装置は、この薄められたブラインを濃縮するもので
、通常ヒータによる加熱、及びブラインを噴霧状に散布
して通風空気と接触させることによって濃縮を行なって
いる。A concentrator condenses this diluted brine, and usually performs condensation by heating with a heater and by spraying the brine and bringing it into contact with ventilated air.
このブライン散布方式では、空気冷却器は熱交換器とし
ての特性を満たすためにプレートフィン形か多管式を採
用するのが普通である。In this brine dispersion method, the air cooler usually adopts a plate-fin type or multi-tube type in order to satisfy the characteristics as a heat exchanger.
プレートフィン形の場合、伝熱面をブラインで完全に濡
らすのは容易でなく、散布ブライン量は極めて多量とな
る。In the case of the plate fin type, it is not easy to completely wet the heat transfer surface with brine, and the amount of brine to be sprayed is extremely large.
多管式の場合は必要伝熱面積を確保することが困難で空
気冷却器の寸法が大きくなる欠点があった。In the case of a multi-tube type, it is difficult to secure the necessary heat transfer area and the size of the air cooler becomes large.
又、ブラインは水分吸収により物性値が変化する。In addition, the physical properties of brine change due to moisture absorption.
ブラインの散布量は、空気冷却器の構成材料によっても
変化するが、特にブラインの粘性による変化が大きい。The amount of brine sprayed varies depending on the constituent material of the air cooler, but it varies greatly depending on the viscosity of the brine.
その為、本装置は運転条件によって冷却能力が変化する
。Therefore, the cooling capacity of this device changes depending on the operating conditions.
同様にして濃縮装置の能力も変化し、空気冷却装置とし
ての制御が複雑になる。Similarly, the capacity of the concentrator changes, making its control as an air cooling device complicated.
又、濃縮装置として加熱ヒータが不可欠である。Additionally, a heater is essential as a concentrator.
特に空気中の水分が多くなった時には、このヒータ電力
は装置全体の電力に対し無視出来ぬ量となる。Particularly when there is a lot of moisture in the air, this heater power becomes a non-negligible amount of power for the entire device.
本発明は、冷凍装置の寒冷により冷却された撥水液を充
てん層に散布することによって、空気冷却器を撥水液と
空気の直接熱交換のみを考慮したコンパクトな構造にす
ること、および撥水液を散布することによって消費電力
が少なく安定した性能を持つ空気冷却器を得ようとする
ものである。The present invention provides an air cooler with a compact structure that takes into consideration only direct heat exchange between the water repellent liquid and the air by dispersing the water repellent liquid cooled by the cold of the refrigeration equipment onto the packed layer. The aim is to obtain an air cooler with low power consumption and stable performance by dispersing aqueous liquid.
以下第1図に示す本発明の一実施例を詳しく説明する。An embodiment of the present invention shown in FIG. 1 will be described in detail below.
第1図に於で、11は撥水液散布装置、12は空気と撥
水液間の熱交換を行なう充てん層で、金属板、金鋼、ハ
ニカムなど熱交換に必要な面積を有し空気抵抗が小さい
ものを用いることができる。In Figure 1, 11 is a water-repellent liquid spraying device, and 12 is a filling layer that performs heat exchange between the air and the water-repellent liquid. A material with low resistance can be used.
充てん層では撥水液と空気間の直接接触による熱交換を
行なうので、充てん層の材質の熱伝導性は問題にならず
、撥水液との耐触性、濡れ性を考慮して安価なプラスチ
ック等を用いることもできる。In the filling layer, heat exchange occurs through direct contact between the water repellent liquid and the air, so the thermal conductivity of the material of the filling layer is not an issue, and an inexpensive material is used in consideration of contact resistance and wettability with the water repellent liquid. Plastic etc. can also be used.
13は空気中の撥水液を補集する空隙の大きな金鋼など
で作られたエリミネータである。13 is an eliminator made of gold steel or the like with large voids that collects water-repellent liquid in the air.
14は撥水液槽、16は吸込ダクトである。14 is a water-repellent liquid tank, and 16 is a suction duct.
18は撥水液を循環させるポンプである。18 is a pump that circulates the water repellent liquid.
而して、11,12,13,14,16.18は空気冷
却器10を構成している。Thus, 11, 12, 13, 14, 16, and 18 constitute an air cooler 10.
20は分離装置で、熱回収用熱交換器21、ポンプ22
、空気を送るブロアーよりなる。20 is a separation device, which includes a heat recovery heat exchanger 21 and a pump 22.
, consisting of a blower that sends air.
30は冷凍装置で、圧縮器31、膨脹弁32、熱交換器
33を有する。A refrigeration system 30 includes a compressor 31, an expansion valve 32, and a heat exchanger 33.
撥水液はポンプ18によって撥水液槽14より取り出さ
れ、熱交換器19において冷却され撥水液散布装置11
に送られ散布される。The water repellent liquid is taken out from the water repellent tank 14 by a pump 18, cooled in a heat exchanger 19, and sent to the water repellent liquid spraying device 11.
sent to and distributed.
散布された撥水液は充てん層12の表面を滴下し、充て
ん物表面で空気と熱交換し撥水液槽14にたまる。The sprayed water-repellent liquid drips onto the surface of the filling layer 12, exchanges heat with the air on the surface of the filling material, and accumulates in the water-repellent liquid tank 14.
空気中の水蒸気は、充てん層12での冷却過程で凝縮し
、撥水液槽14へ落下する。Water vapor in the air condenses during the cooling process in the filled layer 12 and falls into the water-repellent liquid tank 14.
撥水液槽14は通常防熱が施されているので、撥水液槽
14内の撥水液の温度上昇は少ない、そのため落下した
水分は氷状のものが得られ、油と水の比重差により氷状
水分ないしは氷状水分の多い撥水液が撥水液槽14の下
部にたまる。Since the water-repellent liquid tank 14 is usually heat-insulated, the temperature rise of the water-repellent liquid in the water-repellent liquid tank 14 is small. Therefore, the water that falls is obtained in the form of ice, and the difference in specific gravity between oil and water is reduced. As a result, ice-like water or a water-repellent liquid containing a large amount of ice-like water accumulates in the lower part of the water-repellent liquid tank 14.
撥水液散布装置11への取出管を、撥水液槽14の上部
より取出すことにより、充てん層12へ散布する撥水液
は、常に、水分を含まない状態になり、撥水液の性質は
常に一定となる。By taking out the outlet pipe to the water-repellent liquid spraying device 11 from the upper part of the water-repellent liquid tank 14, the water-repellent liquid sprayed onto the filling layer 12 always contains no water, and the properties of the water-repellent liquid are maintained. is always constant.
′このようにして安定した性能を持つ空気冷却器が実現
される。'In this way, an air cooler with stable performance is achieved.
同様にして、分離装置20へ導く取出管は撥水液槽14
の下部より取出すことにより効率の良い油水分離が実現
される。Similarly, the extraction pipe leading to the separation device 20 is connected to the water repellent liquid tank 14.
Efficient oil-water separation is achieved by taking out the oil from the bottom of the tank.
分離装置20は強制的に空気を通風して油水を分離する
浮上法が有効である。An effective method for the separation device 20 is a flotation method in which oil and water are separated by forced air ventilation.
撥水液としてはナフテン系の油が本装置に有効な性質を
持っている。As a water repellent liquid, naphthenic oil has properties that are effective for this device.
一般に油は粘度が高く充てん層等固体に散布するには困
難と考えられている。Generally, oil has a high viscosity and is considered difficult to spray onto solids such as packed layers.
特に低温に於では粘度は急激に高くなると考えられてい
るが、ナフテンリッチに精製されたもの(一例として高
圧絶縁油、冷凍機油(IGS)等)は低温においても充
分な流動性を持ち、又水に対する安定性も高いことがわ
かった。It is believed that the viscosity increases rapidly especially at low temperatures, but naphthene-rich refined products (such as high-pressure insulating oil and refrigeration oil (IGS)) have sufficient fluidity even at low temperatures. It was also found that the stability against water is high.
第2図に各種流体の動粘性係数の温度依存性を示す。Figure 2 shows the temperature dependence of the kinematic viscosity coefficients of various fluids.
尚、前記実施例では、油水分離装置は浮上法を用いると
したが、遠心分離法等本方法を含む現用技術が適用出来
る。In the above embodiments, the oil/water separator uses a flotation method, but any current technology including this method, such as a centrifugal separation method, can be applied.
又、空気冷却器において、空気流の方向は撥水液散布方
向と逆方向にしたが、順方向、直角方向としても良い。Further, in the air cooler, the direction of the air flow is opposite to the direction in which the water-repellent liquid is distributed, but the direction of the air flow may be the forward direction or the right angle direction.
以上述べたように本発明は低温用空気冷却器において、
霜の生成を抑制した構造を持つもので除霜運転を必要と
しない。As described above, the present invention provides a low-temperature air cooler,
It has a structure that suppresses frost formation and does not require defrosting operation.
かつ現在実用化されているブライン散布方式に比べて、
充てん層の構成材質、形状に対する制限がほとんどなく
任意の材料を用い極めてコンパクトな構造となること、
また装置の制御が簡単な、かつ消費電力の少ない気体冷
却装置が得られる。And compared to the brine dispersion method currently in use,
There are almost no restrictions on the material and shape of the filling layer, and an extremely compact structure can be achieved using any material.
Furthermore, a gas cooling device that is easy to control and consumes little power can be obtained.
第1図は本発明の一実施例を示す系統図、第2図は流体
の動粘性係数の温度依存性を示す特性図である。
図において、10は空気冷却器、11は撥水液散布装置
、12は充てん層、13はエリミネータ、14は撥水液
槽、15はファン、16は吸込ダクト、17は吐出ダク
ト、18はポンプ、19は熱交換器、20は分離装置、
21は熱交換器、22はポンプ、23はブロアー、30
は冷凍装置、31は圧縮機、32は膨脹弁、33は熱交
換器である。FIG. 1 is a system diagram showing an embodiment of the present invention, and FIG. 2 is a characteristic diagram showing the temperature dependence of the kinematic viscosity coefficient of a fluid. In the figure, 10 is an air cooler, 11 is a water-repellent liquid distribution device, 12 is a packed layer, 13 is an eliminator, 14 is a water-repellent liquid tank, 15 is a fan, 16 is a suction duct, 17 is a discharge duct, and 18 is a pump , 19 is a heat exchanger, 20 is a separation device,
21 is a heat exchanger, 22 is a pump, 23 is a blower, 30
31 is a compressor, 32 is an expansion valve, and 33 is a heat exchanger.
Claims (1)
布装置から散布された撥水液を受けこの撥水液と気体と
の気液接触を行なう充てん層と、上記気液接触後の撥水
液を受ける撥水液槽と、この撥水液槽内の撥水液を上記
撥水液散布装置に供給する撥水液供給路と、冷凍装置の
寒冷により上記撥水液を冷却する熱交換装置と、上記撥
水液槽内の撥水液中の不純物を分離し除去する分離装置
とを備えてなる気体冷却装置。1. A water-repellent liquid spraying device that sprays a water-repellent liquid, a filling layer that receives the water-repellent liquid sprayed from the water-repellent liquid spraying device, and performs gas-liquid contact between the water-repellent liquid and gas, and the above-mentioned gas-liquid contacting layer. A water-repellent liquid tank that receives the water-repellent liquid afterwards, a water-repellent liquid supply path that supplies the water-repellent liquid in the water-repellent liquid tank to the water-repellent liquid spraying device, and a water-repellent liquid supply path that supplies the water-repellent liquid in the water-repellent liquid tank to the water-repellent liquid spraying device; A gas cooling device comprising a heat exchange device for cooling and a separation device for separating and removing impurities in the water repellent liquid in the water repellent liquid tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4642877A JPS599039B2 (en) | 1977-04-21 | 1977-04-21 | gas cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4642877A JPS599039B2 (en) | 1977-04-21 | 1977-04-21 | gas cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53131552A JPS53131552A (en) | 1978-11-16 |
| JPS599039B2 true JPS599039B2 (en) | 1984-02-28 |
Family
ID=12746870
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4642877A Expired JPS599039B2 (en) | 1977-04-21 | 1977-04-21 | gas cooling device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS599039B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4033677B2 (en) * | 2002-01-09 | 2008-01-16 | 忠弘 大見 | Air cooling method |
-
1977
- 1977-04-21 JP JP4642877A patent/JPS599039B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53131552A (en) | 1978-11-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5604295B2 (en) | Structure and method for ambient air vaporizer | |
| CN210356618U (en) | Electronic semiconductor coagulation leading device | |
| US4890463A (en) | Absorption-type refrigeration system with thermal energy recovery, particularly for vehicles provided with an internal combustion engine | |
| CN216592314U (en) | Heat pump unit for preventing defrosting water from being frozen secondarily and heat pump unit | |
| CN115900196A (en) | An air-cooled mode cold and hot fluorine defrosting assembly | |
| JP4486369B2 (en) | Outdoor unit of air conditioner and air conditioner equipped with the same | |
| JPS599039B2 (en) | gas cooling device | |
| CN221463914U (en) | Water curtain spray type device for improving supercooling degree of condenser | |
| CN209857505U (en) | Semiconductor refrigeration gradevin with dehumidification function | |
| CN216557472U (en) | High-efficient indirect evaporative cooling device | |
| CN2608930Y (en) | Direct-contact two-element ice storage cold air conditioner | |
| CN220038648U (en) | Air conditioning device | |
| CN207247374U (en) | Refrigeration host computer and air-conditioning | |
| KR200282298Y1 (en) | Heating-exchange type refrigerating device | |
| CN114981600B (en) | Cooling device and cooling method | |
| CN213273286U (en) | Evaporator ice climbing prevention system | |
| JPH04174229A (en) | Ice heat storage device | |
| CN221924159U (en) | A double-stage cascade heat pump drainage structure for severe cold regions | |
| CN219462558U (en) | Switching defrosting condensing equipment and high concentration VOC exhaust treatment system | |
| CN220602289U (en) | Heat exchange device for cold recovery of air bath type vaporizer | |
| JP3729876B2 (en) | Air conditioner low temperature regenerator | |
| JPH0567867B2 (en) | ||
| CN206572816U (en) | A kind of heat pump antifrost regenerative device of solution | |
| CN208379674U (en) | Condensation evaporation device and air water machine | |
| JPH08136170A (en) | Heat pipe type cooler |