JPS58140585A - Method of cooling denatured alcohol - Google Patents
Method of cooling denatured alcoholInfo
- Publication number
- JPS58140585A JPS58140585A JP2285582A JP2285582A JPS58140585A JP S58140585 A JPS58140585 A JP S58140585A JP 2285582 A JP2285582 A JP 2285582A JP 2285582 A JP2285582 A JP 2285582A JP S58140585 A JPS58140585 A JP S58140585A
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- argon
- refrigerant
- modified
- oxygen
- 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
Links
Landscapes
- Separation By Low-Temperature Treatments (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】
本発明は、変成アルゴンの冷却方法に係り、精製アルゴ
ンを採取する9気分JIII[厘に好適な変成アルゴン
の冷却方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cooling modified argon, and more particularly, to a method for cooling modified argon suitable for collecting purified argon.
従来、精製アルゴン(以下、精製人rと略)を採取する
・空気分離装置より取出された粗アルゴン(以下、粗A
r と略)から酸素を分離し、かつ、ll嵩分離時に約
250℃に昇温した変成アルゴン(以下、変成人rと略
)は、冷凍II&置より供給される冷感により約5℃ま
で冷却されている。Conventionally, purified argon (hereinafter abbreviated as "refiner r") is collected. - Crude argon (hereinafter referred to as crude A) taken out from an air separation device is collected.
The modified argon (hereinafter abbreviated as modified argon), which has been heated to approximately 250°C during bulk separation, is heated to approximately 5°C due to the cooling sensation supplied from Refrigeration II & It is cooled.
このような変成人rの冷却方法では、冷凍装置の設置が
必要であるため、装置価格並びに運転費が増大するとI
n−、た欠点がs+−2だ。This method of cooling the transformed man r requires the installation of a refrigeration system, which increases the equipment price and operating costs.
n-, the drawback is s+-2.
本発明は、上記欠点の除去を目的としたもので、g気分
1lIIIi置より#出される液体酸素で冷厳を冷却し
、該冷厳で、空気分離装置より取出された粗Arかも酸
素を分離し、かつ、該酸素分離時に昇温した変成ムrを
冷却することで、冷凍装置を不用にで亀、装置価格を低
減できると共に運転費を削減で自為変成ムrの冷却方法
を提供するものである。The present invention is aimed at eliminating the above-mentioned drawbacks, and includes cooling a cooling tank with liquid oxygen discharged from a g-room, separating crude Ar and oxygen taken out from an air separation device in the cooling tank, and In addition, by cooling the metamorphic mulch whose temperature has risen during the oxygen separation, it is possible to eliminate the need for a refrigeration device, reduce the cost of the equipment, and provide a method for cooling the spontaneous metamorphic mulch while reducing operating costs. be.
本発明の一*施例を図面により説明する。A first embodiment of the present invention will be explained with reference to the drawings.
図面は1本発明を実施した精製人rを採取する空気分離
装置の系統図で、gAr塔Wより熱交換される。パラジ
ウム触謀楕口では、粗AFに含有された酸素と水素とが
反応するととでllI素が分離され、約ZSO℃に昇温
した変成A【が得られる。The drawing is a system diagram of an air separation device for collecting refiner r according to the present invention, in which heat is exchanged from gAr column W. In the palladium probe, when the oxygen contained in the crude AF reacts with hydrogen, the llI element is separated, and a modified A is obtained at a temperature of approximately ZSO°C.
この変成Arは、導管冨を経て、冷媒槽14に張込まれ
た水等の冷媒中に浸漬されたアルゴン冷却器腸に供給さ
れる。一方、冷媒槽14に張込まれた冷媒は、精留塔旙
に設置された主凝縮器17より導管羽を経て排出され、
冷媒中に浸漬された液酸プロー蒸発器訪に供給畜れ流通
する液体酸素により約1’Cまで冷却され、冷媒を冷却
した液体酸素は気化し導管あを経て大気放出される。ア
ルゴン冷却器巧に供給された約250℃の変成Arはア
ルゴン冷却器上を流通する間に約1℃の冷媒により約5
℃まで冷却され、冷却された変成Atは導管易を経て切
替え使用されるアルゴン脱湿塔肋に供給される。アルゴ
ン脱湿419で除湿された変成人rは、熱交換器Uを介
し導管菖、37を経て精製Ar塔加に供給され、ここで
窒素等信の不純物を除去され精製Atとなって導管あ上
り採取される。この場合、冷媒の温度は、導管あに設け
られた温度検出器恥で冷却された変成Arの温度を検出
し、検出温度をもとに温度制御装置社で導管抛に設けら
れた調節弁52および温水勢の熱媒を冷媒槽14に供給
する導管lに設けられた調節弁錦の弁開度を調節するこ
とにより適正に保持される。なお、冷媒槽14に張込ま
れた冷媒の液位は、液位検出器8゜冷媒排出用の導管菊
に設けられた調節弁間により適正に維持され、また、変
成Arの冷却時に生じたドレンは、ドレン#出用の導管
41.弁開を経てアルゴン冷却器篇より排出される。This modified Ar is supplied to the argon cooler immersed in a refrigerant such as water filled in a refrigerant tank 14 through a conduit. On the other hand, the refrigerant charged in the refrigerant tank 14 is discharged from the main condenser 17 installed in the rectification tower through the conduit vanes.
The liquid oxygen immersed in the refrigerant is supplied to the evaporator and is cooled down to about 1'C by the flowing liquid oxygen.The liquid oxygen that has cooled the refrigerant is vaporized and released into the atmosphere through a conduit. Argon cooler The modified Ar at about 250°C supplied by the argon cooler is heated by about 1°C while flowing over the argon cooler.
℃, and the cooled modified At is supplied to the argon dehumidification column, which is used in a switched manner, through a conduit. The modified adult r that has been dehumidified by argon dehumidification 419 is supplied to the purified Ar column through the heat exchanger U and the conduit tube 37, where impurities such as nitrogen are removed and purified At is converted to the conduit tube. It is collected upstream. In this case, the temperature of the refrigerant is determined by detecting the temperature of the cooled metamorphic Ar with a temperature sensor installed in the conduit, and based on the detected temperature, the temperature controller uses a control valve 52 installed in the conduit. The temperature is maintained properly by adjusting the opening degree of a control valve provided in the conduit l that supplies the hot water heating medium to the refrigerant tank 14. The liquid level of the refrigerant injected into the refrigerant tank 14 is maintained appropriately between the liquid level detector 8° and the control valve provided in the conduit chrysanthemum for refrigerant discharge. The drain is connected to a drain pipe 41. After opening the valve, it is discharged from the argon cooler.
本実施例のような変成Arの冷却方法では、昇温した変
成Arを、精留塔の主凝縮器より排出される液体#Il
素で冷却された冷媒により冷却するので、冷凍装置が不
用となり、また、従来、無駄に捨てられていた液体酸素
が有する寒冷を冷媒を冷却することで有効に回収できる
ので、空気分1111M置全体の寒冷補償を軽減するこ
とができる。In the method of cooling modified Ar as in this embodiment, the heated modified Ar is cooled to liquid #Il discharged from the main condenser of the rectification column.
Since cooling is performed using a naturally cooled refrigerant, there is no need for a refrigeration system, and the cold contained in liquid oxygen, which was conventionally wasted, can be effectively recovered by cooling the refrigerant, so the air content of the entire 1111M plant is reduced. cold compensation can be reduced.
本発明は、以上説明したように、空気分離装置より排出
される液体酸素で冷媒を冷却し、腋冷媒で、空気分離装
置より取出された粗ムrから酸素を分離し、かつ、該酸
素分離時に昇温した変成Arを冷却することで、冷iK
装置を不用にで禽るので、装置価格を低減できると共に
運転費を削減できる効果がある。As explained above, the present invention cools a refrigerant with liquid oxygen discharged from an air separation device, uses an armpit refrigerant to separate oxygen from coarse sludge taken out from the air separation device, and the oxygen separation By cooling the metamorphic Ar that has been heated at the time, the cold iK
Since the equipment is not needed, it is possible to reduce the cost of the equipment and reduce operating costs.
図面は、本発明の一実施例を説明するもので、本発明を
実施した精製人rを採取する空気分離装置の系統図であ
る。
lo・・・・・・@Ar塔、11・・・・・・熱交換器
、U・・・・・・アルゴンブロワ−1l・・・・・・パ
ラジウム触媒槽、14・・・・・・冷−檜、止・・−・
・、アルゴン冷却器、謁・・・・・・精留塔、17・・
・・・・主凝縮器、訪・・・・・・液酸プロー蒸発器、
30からあ・・・・・・導管The drawing explains one embodiment of the present invention, and is a system diagram of an air separation device for collecting refiner r in which the present invention is implemented. lo...@Ar tower, 11...heat exchanger, U...argon blower 1l...palladium catalyst tank, 14... Cold cypress, stop...
・, argon cooler, audience... rectification tower, 17...
...Main condenser, Visit...Liquid acid blower evaporator,
From 30... conduit
Claims (1)
酸素を分魅し、かつ、腋酸素分離時に昇温した変成アル
ゴンの冷却方法において 前記空気分離装置より排出さ
れる液体酸素で冷媒を冷却し、皺冷媒で前記変成アルゴ
ンを冷却することを特徴とした変成アルゴンの冷却方法
。! , In a method for separating oxygen from primary argon taken out from the air separation device II and cooling the modified argon heated during axillary oxygen separation, the refrigerant is cooled with liquid oxygen discharged from the air separation device, and wrinkles are removed. A method for cooling metamorphosed argon, comprising cooling the metamorphosed argon with a refrigerant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2285582A JPS58140585A (en) | 1982-02-17 | 1982-02-17 | Method of cooling denatured alcohol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2285582A JPS58140585A (en) | 1982-02-17 | 1982-02-17 | Method of cooling denatured alcohol |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58140585A true JPS58140585A (en) | 1983-08-20 |
Family
ID=12094324
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2285582A Pending JPS58140585A (en) | 1982-02-17 | 1982-02-17 | Method of cooling denatured alcohol |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58140585A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5612975A (en) * | 1979-07-12 | 1981-02-07 | Kajima Sanso Kk | Argon cooling method |
-
1982
- 1982-02-17 JP JP2285582A patent/JPS58140585A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5612975A (en) * | 1979-07-12 | 1981-02-07 | Kajima Sanso Kk | Argon cooling method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4285702A (en) | Method and apparatus for the recovery of water from atmospheric air | |
CA2137771C (en) | Method and apparatus for refrigerant reclamation | |
US20070289448A1 (en) | Biogas fuel conditioning system | |
US20070012419A1 (en) | Method and device for cryocondensation | |
JPS58140585A (en) | Method of cooling denatured alcohol | |
Assouad et al. | Solar desalination with latent heat recovery | |
WO2007146281A2 (en) | Biogas fuel conditioning system | |
US2481520A (en) | Cooling cycle for internal-combustion engines | |
GB2118713A (en) | Vehicle air conditioning apparatus | |
JP3681187B2 (en) | Air liquefaction separation method and apparatus | |
JPS642239B2 (en) | ||
JPH0529013A (en) | Fuel cell power generation system | |
JP3072563B2 (en) | Method and apparatus for collecting high-purity liquefied nitrogen | |
JP3084716B2 (en) | Absorption chiller / heater and its operation method | |
JPS6291761A (en) | Absorption type water chiller and heater | |
JP3735745B2 (en) | Cooling operation control method for absorption air conditioner | |
JPS5813966A (en) | Controller for absorption type cold and hot water machine | |
JPS5447346A (en) | Air conditioning system | |
JPS5924134A (en) | Calorimeter for air conditioner | |
JPH0245094B2 (en) | ||
JPS60221670A (en) | Raw material gas cooling device | |
JPS5835972Y2 (en) | Refrigeration equipment | |
JPH11344231A (en) | Waste heat energy converting system | |
JPS60169077A (en) | Air separator with oxygen heat exchanger | |
JPS6313764Y2 (en) |