JPH0163992U - - Google Patents

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Publication number
JPH0163992U
JPH0163992U JP1987156775U JP15677587U JPH0163992U JP H0163992 U JPH0163992 U JP H0163992U JP 1987156775 U JP1987156775 U JP 1987156775U JP 15677587 U JP15677587 U JP 15677587U JP H0163992 U JPH0163992 U JP H0163992U
Authority
JP
Japan
Prior art keywords
rectification column
pressure rectification
low
air separation
cold box
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.)
Granted
Application number
JP1987156775U
Other languages
Japanese (ja)
Other versions
JPH0533912Y2 (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 JP1987156775U priority Critical patent/JPH0533912Y2/ja
Publication of JPH0163992U publication Critical patent/JPH0163992U/ja
Application granted granted Critical
Publication of JPH0533912Y2 publication Critical patent/JPH0533912Y2/ja
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation By Low-Temperature Treatments (AREA)

Description

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

第1図、第2図は本考案装置の一具体例を示す
フローシートであり、図中: 1……原料空気圧縮機、2……水洗浄塔、3,
4……切替式空気熱交換器(3は高温熱交換器、
4は低温熱交換器)、5……高圧精留塔、6……
主蒸化器、7……吸着器(2塔切替式……液化空
気過器)、8……液化空気過冷却器、9……液
化窒素過冷却器、10……低圧精留塔、11……
アルゴン精留塔、12……二重殻真空断熱液化窒
素貯槽、13……液化酸素ポンプ、14……吸着
器(2塔切替式……液化酸素過器)、18……
二重殻真空断熱導管、20……凝縮器、24a,
24b,24c,24d……切替バルブ、25a
,25b……フラペツトボツクス、50……液化
ユニツト、C・B……コールドボツクス、26〜
49,51,56,57……導管、54……パー
ライト断熱大型貯槽、55……液化窒素ポンプ。
Figures 1 and 2 are flow sheets showing a specific example of the device of the present invention, in which: 1... raw air compressor, 2... water washing tower, 3,
4...Switchable air heat exchanger (3 is a high temperature heat exchanger,
4 is a low temperature heat exchanger), 5...high pressure rectification column, 6...
Main evaporator, 7... Adsorber (two-column switching type... liquefied air filter), 8... Liquefied air supercooler, 9... Liquefied nitrogen supercooler, 10... Low pressure rectification column, 11 ……
Argon rectification column, 12... Double-shell vacuum insulated liquefied nitrogen storage tank, 13... Liquefied oxygen pump, 14... Adsorption device (two-column switching type... liquefied oxygen over device), 18...
Double shell vacuum insulated conduit, 20... Condenser, 24a,
24b, 24c, 24d...Switching valve, 25a
, 25b...Frappet box, 50...Liquification unit, C/B...Cold box, 26~
49, 51, 56, 57... conduit, 54... large perlite insulated storage tank, 55... liquefied nitrogen pump.

Claims (1)

【実用新案登録請求の範囲】 (1) 圧縮された空気を原料として高圧精留塔5
と低圧精留塔10とを備えた複式精留塔により酸
素ガスと窒素ガスを製造する、コールドボツクス
に封入された空気分離装置において、前記コール
ドボツクス外方に設置した断熱型液化窒素貯槽1
2を、断熱パイプ18を介して高圧精留塔5の頂
部に連通し、該断熱パイプ18はコールドボツク
スC・B内に膨張弁18aを具備し、前記低圧精
留塔底部液だめ52に液面検知具53を設けたこ
とを特徴とする、低圧精留塔底部液面を制御する
ことにより寒冷量を調節する空気分離装置。 (2) 前記高圧精留塔5頂部から取り出した窒素
ガスを分岐して液化する装置をコールド・ボツク
ス内に配設した実用新案登録請求の範囲第1項記
載の低圧精留塔底部液面を制御することにより寒
冷量を調節する空気分離装置。
[Claims for Utility Model Registration] (1) A high-pressure rectification column 5 using compressed air as a raw material.
In an air separation device enclosed in a cold box, which produces oxygen gas and nitrogen gas by a double rectification column equipped with a low-pressure rectification column 10, an adiabatic liquefied nitrogen storage tank 1 installed outside the cold box.
2 is connected to the top of the high-pressure rectification column 5 via an insulated pipe 18, and the insulated pipe 18 is equipped with expansion valves 18a in cold boxes C and B, and the liquid is supplied to the bottom liquid reservoir 52 of the low-pressure rectification column. An air separation device that adjusts the amount of refrigeration by controlling the liquid level at the bottom of a low-pressure rectification column, characterized in that it is equipped with a surface detector 53. (2) The liquid level at the bottom of the low-pressure rectification column according to claim 1, which is a utility model registration, wherein a device for branching and liquefying the nitrogen gas taken out from the top of the high-pressure rectification column 5 is disposed in a cold box. Air separation equipment that adjusts the amount of refrigeration by controlling it.
JP1987156775U 1987-10-15 1987-10-15 Expired - Lifetime JPH0533912Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987156775U JPH0533912Y2 (en) 1987-10-15 1987-10-15

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987156775U JPH0533912Y2 (en) 1987-10-15 1987-10-15

Publications (2)

Publication Number Publication Date
JPH0163992U true JPH0163992U (en) 1989-04-25
JPH0533912Y2 JPH0533912Y2 (en) 1993-08-27

Family

ID=31435618

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987156775U Expired - Lifetime JPH0533912Y2 (en) 1987-10-15 1987-10-15

Country Status (1)

Country Link
JP (1) JPH0533912Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61190277A (en) * 1985-02-16 1986-08-23 大同酸素株式会社 High-purity nitrogen and oxygen gas production unit

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61190277A (en) * 1985-02-16 1986-08-23 大同酸素株式会社 High-purity nitrogen and oxygen gas production unit

Also Published As

Publication number Publication date
JPH0533912Y2 (en) 1993-08-27

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