Patent US4617037A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4617037A Expired / Lapsed US ⏱️ 0.0 years remaining

Nitrogen production method

Assignee: Taiyo Nippon Sanso Corp
•
Filing: 1985-10-31
•
Granted: 1986-10-14
•
Expires: 2005-10-31
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A nitrogen production method wherein air is compressed, is removed of water and carbon dioxide contained therein, and is simultaneously cooled to a temperature close to the liquefying point, and the resultant cleaned and cooled air is fed into a rectifying column for rectification so that high purity nitrogen is withdrawn from the rectifying column overhead; and wherein the oxygen-enriched liquid air withdrawn from the rectifying column bottom is expanded and fed into a condensation step wherein it becomes a source of reflux producing cold in the above-mentioned rectifying column, and then a cold is produced by adiabatically expanding the vaporized gas, after which heat exchange with raw air is performed. In this method, there is provided a closed circulating system wherein a circulating gas which is compressed is cooled by heat exchange with a return gas of the circulating gas, and the resultant cooled gas is fed into a reboiler at the bottom of the above-mentioned rectifying column wherein it vaporizes a liquid in the bottom of the rectifying column, and after the compressed circulating gas itself is liquefied through the above described step and expanded, it is fed into the above-mentioned condenser wherein it is vaporized by heat exchange with the high purify nitrogen from the above-mentioned rectifying column, and further the resultant vaporized gas is restored to normal temperature by heat exchange with the above-mentioned compressed circulating gas and is then subjected to recompression for continued circulation.

Inventors

  • 👤 Hidetake Okada
  • 👤 Satoshi Urata

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 19:49
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04248; F25J3/04284; F25J3/04278; F25J3/04333; F25J3/04351; F25J3/04375; F25J3/04381; F25J3/044; F25J3/04642; F25J3/04763; F25J3/04866; F25J3/04951; F25J3/04957; F25J2200/00; F25J2200/50; F25J2200/72; F25J2200/74; F25J2200/76; F25J2205/00; F25J2205/24; F25J2215/00; F25J2215/30; F25J2215/32; F25J2230/00; F25J2230/24; F25J2250/00; F25J2250/20; F25J2270/00; F25J2270/12; F25J2270/40; F25J2270/58

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 254 words
A method for producing nitrogen wherein air is compressed, is removed of water and carbon contained therein, cooled to a temperature close to the liquefying point, is then fed into a rectifying column for rectification and from the overhead of said rectifying column high purity nitrogen is withdrawn; and wherein oxygen-enriched liquid air, fed from the bottom of said rectifying column, is expanded and fed into a condensation step whereafter said expanded oxygen-enriched liquid air is used as a source of reflux producing cold for said rectifying column and adiabatic expansion is effected on the evaporated gas to produce cold, so that heat exchange with raw air is conducted, said method for producing nitrogen being provided with a closed cycle comprising the step of: compressing a circulating gas; cooling a compressed circulating gas by heat exchange with a circulating gas fed back into said compressing step; vaporizing a bottom liquid in said rectifying column by supplying said cooled circulating gas into a reboiler at the bottom of said rectifying column to thereby liquefy the cooled circulating gas; expanding said liquefied circulating gas; thereafter feeding an expanded circulating gas into said condensation step to vaporize the same by heat exchange with said high purity nitrogen withdrawn from the rectifying column overhead; thereafter feeding said vaporized circulating gas into said cooling step before the same is fed back into said compressing step, to heat the same by heat exchange with said compressed circulating gas; and returning said heated circulating gas into said compressing step for circulation.
Claim 2
Independent Claim 254 words
A method for producing nitrogen wherein air is compressed, is removed of water and carbon contained therein, cooled to a temperature close to the liquefying point, is then fed into a rectifying column for rectification and from the overhead of said rectifying column high purity nitrogen is withdrawn; and wherein oxygen-enriched liquid air, fed from the bottom of said rectifying column, is expanded and fed into a condensation step whereafter said expanded oxygen-enriched liquid air is used as a source of reflux producing cold for said rectifying column and adiabatic expansion is effected on the evaporated gas to produce cold, so that heat exchange with raw air is conducted, said method for producing nitrogen being provided with a closed cycle comprising the step of: compressing a circulating gas; cooling a compressed circulating gas by heat exchange with a circulating gas fed back into said compressing step; vaporizing a bottom liquid in said rectifying column by supplying said cooled circulating gas into a reboiler at the bottom of said rectifying column to thereby liquefy the cooled circulating gas; expanding said liquefied circulating gas; thereafter feeding an expanded circulating gas into said condensation step to vaporize the same by heat exchange with said high purity nitrogen withdrawn from the rectifying column overhead; thereafter feeding said vaporized circulating gas into said cooling step before the same is fed back into said compressing step, to heat the same by heat exchange with said compressed circulating gas; and returning said heated circulating gas into said compressing step for circulation.
Claim 3
Dependent Claim 39 words
A nitrogen producing method according to claim 1, wherein said circulating gas is composed of a single or a mixed gas, each having its boiling point at an intermediate point between the respective boiling points of nitrogen and oxygen.
Claim 4
Dependent Claim 25 words
A nitrogen producing method according to claim 2, wherein said circulating gas is a gas containing at least two components of nitrogen, argon and oxygen.
Claim 5
Dependent Claim 14 words
A nitrogen producing method according to claim 3, wherein said circulating gas is air.
Claim 6
Dependent Claim 16 words
A nitrogen producing method according to claim 2, wherein said circulating gas is an argon gas.
Claim 7
Dependent Claim 32 words
A nitrogen producing method according to claim 1, wherein recompression of the circulating gas heated by said heat exchange is partially performed by recovered power which is generated by said adiabatic expansion.

References Cited (Backward Citations)

US3126267A Cited
US3914949A Cited
US3818714A Cited
US4088464A Cited
US4099945A Cited
US4566887A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-10-13 1990-04-14 1990-10-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-10-13 1994-04-14 1994-10-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-10-13 1998-04-14 1998-10-14 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag