US4853015A
Expired / Lapsed
US
⏱️ 0.0 years remaining
High purity nitrogen and oxygen gas production equipment
Assignee: Air Water Inc
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Filing: 1988-10-14
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Granted: 1989-08-01
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Expires: 2008-10-14
Abstract
Abstract There is provided an apparatus for manufacturing nitrogen gas and oxygen gas of very high purity by cryogenic liquefaction, and without using an expansion turbine. Supercooled and compressed air is sent to a distilling tower where it is mixed with and cooled by the latent heat of vaporization of liquid nitrogen from any external source. Utilizing the difference between their boiling points, nitrogen is taken out as gas while oxygen remains as liquid. The oxygen is concentrated in an oxygen condenser and then further concentrated in an oxygen distilling tower mixed with liquid oxygen from an external source as the refrigerant.
Inventors
- 👤 Akira Yoshino
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 07:46
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04763; F25J3/04769; F25J3/04854; F25J3/0486; F25J3/04151; F25J3/04187; F25J3/04218; F25J3/04248; F25J3/04254; F25J3/04406; F25J3/0443; F25J3/04436; F25J3/04454; F25J3/04812; F25J3/04824; F25J2200/00; F25J2200/34; F25J2200/50; F25J2200/54; F25J2205/00; F25J2205/60; F25J2210/00; F25J2210/42; F25J2210/50; F25J2215/00; F25J2215/42; F25J2215/44; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/42; F25J2250/50; F25J2280/00; F25J2280/02; F25J2290/00; F25J2290/62; Y; Y10; Y10S; Y10S62/00; Y10S62/912; Y10S62/913
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
289 words
An apparatus for manufacturing highly pure nitrogen and oxygen gas consisting essentially of an air-compressing means for compressing outside air, a removing means for removing carbon dioxide gas and water in the air compressed by said air compressing means, a heat-exchanging means for cooling the compressed air from the above removing means to supercold temperature, a liquid nitrogen-storing means for storing liquid nitrogen supplied from outside of the apparatus, a nitrogen-distilling tower in which apart of the compressed air chilled at supercold temperature by the above heat-exchanging means is liquefied to store it inside while only nitrogen is maintained in its gaseous state, liquid nitrogen introducing means for introducing liquid nitrogen from the above storing means for nitrogen gas into the above nitrogen distilling tower as the refrigerant for liquefying the compressed air, an outlet for nitrogen gas provided in the nitrogen-distilling tower in which gaseous nitrogen from the liquid nitrogen refrigerant and gaseous nitrogen produced in the above nitrogen distilling tower are taken out as a nitrogen gas from the above nitrogen distilling tower, an oxygen distilling tower in which nitrogen and oxygen are separated from liquid air utilizing the difference between their boiling points, a liquid air supplying means for supplying liquid air remaining in the nitrogen distilling tower to the oxygen distilling tower, a storing means for storing liquid oxygen supplied from outside of the apparatus, liquid oxygen introducing means for introducing liquid oxygen from the liquid oxygen-storing means into the oxygen distilling tower as the refrigerant, and liquid oxygen gas outlet means for removing both oxygen gas separated from the liquid air utilizing the difference between boiling points of oxygen and nitrogen and oxygen gas from the liquid oxygen refrigerant from the oxygen distilling tower.
Claim 2
Independent Claim
289 words
An apparatus for manufacturing highly pure nitrogen and oxygen gas consisting essentially of an air-compressing means for compressing outside air, a removing means for removing carbon dioxide gas and water in the air compressed by said air compressing means, a heat-exchanging means for cooling the compressed air from the above removing means to supercold temperature, a liquid nitrogen-storing means for storing liquid nitrogen supplied from outside of the apparatus, a nitrogen-distilling tower in which apart of the compressed air chilled at supercold temperature by the above heat-exchanging means is liquefied to store it inside while only nitrogen is maintained in its gaseous state, liquid nitrogen introducing means for introducing liquid nitrogen from the above storing means for nitrogen gas into the above nitrogen distilling tower as the refrigerant for liquefying the compressed air, an outlet for nitrogen gas provided in the nitrogen-distilling tower in which gaseous nitrogen from the liquid nitrogen refrigerant and gaseous nitrogen produced in the above nitrogen distilling tower are taken out as a nitrogen gas from the above nitrogen distilling tower, an oxygen distilling tower in which nitrogen and oxygen are separated from liquid air utilizing the difference between their boiling points, a liquid air supplying means for supplying liquid air remaining in the nitrogen distilling tower to the oxygen distilling tower, a storing means for storing liquid oxygen supplied from outside of the apparatus, liquid oxygen introducing means for introducing liquid oxygen from the liquid oxygen-storing means into the oxygen distilling tower as the refrigerant, and liquid oxygen gas outlet means for removing both oxygen gas separated from the liquid air utilizing the difference between boiling points of oxygen and nitrogen and oxygen gas from the liquid oxygen refrigerant from the oxygen distilling tower.
Claim 3
Dependent Claim
56 words
The apparatus of claim 1 further comprising an oxygen condensing tower for receiving liquid air from the nitrogen distilling tower and separating nitrogen from said liquid air to produce a liquid air having a higher concentration of oxygen and for supplying the liquid air product to the oxygen distilling tower via the liquid air supplying means.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-07-31 | 1993-01-30 | 1993-08-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-07-31 | 1997-01-30 | 1997-08-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-07-31 | 2001-01-30 | 2001-08-01 | $7700.00 | Window Closed / Lapsed |