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US3736762A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of producing the gaseous and liquefied nitrogen and an apparatus used therefor

Assignee: Kobe Steel Ltd
•
Filing: 1970-10-20
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Granted: 1973-06-05
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Expires: 1990-10-20
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Abstract

Abstract In a method of producing gaseous and liquefied nitrogen having a pressure higher than atmospheric pressure, by the use of an apparatus comprising a reversible heat exchanger and a single column rectifier, the combination of following steps: the impure gas obtained by heat-exchanging, in a condenser-evaporator, of liquefied air with nitrogen gas, each of which has been separated in the column, is divided into two parts; one of these parts is again divided into two parts; one part of this second division is passed through a control valve and then through the heat exchanger, after which it is united and admixed with the remaining part of the gas resulting from the second division, which has passed through a control valve; this admixture is supplied to an expansion turbine; the expanded impure gas is united and admixed with the remaining part of the gas resulting from the original division, which has passed through a control valve: and this admixture, after having been passed through the air-liquefier and then the heat exchanger, is taken out of the apparatus. Adopting the abovementioned process makes it possible to industrially and advantageously produce gaseous nitrogen and liquefied nitrogen.

Inventors

  • 👤 A Toyama
  • 👤 I Matsumoto
  • 👤 T Izumichi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 13:50
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04248; F25J3/04284; F25J3/04151; F25J3/04242; F25J3/044; F25J2200/00; F25J2200/72; F25J2205/00; F25J2205/24; F25J2205/60; F25J2205/84; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/42; F25J2250/52

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 34 words
A method according to claim 1, wherein prior to dividing one of the original parts of impure gas into the two additional parts of impure gas, said original part is passed through the air-liquefier.
Claim 2
Dependent Claim 32 words
A method according to claim 1, wherein after admixture of the two additional parts of gas, the resultant mixture is passed through a control valve prior to introduction into the expansion turbine.
Claim 3
Dependent Claim 32 words
A method according to claim 2, wherein after admixture of the two additional parts of gas, the resultant mixture is passed through a control valve prior to introduction into the expansion turbine.

References Cited (Backward Citations)

US2627731A Cited
US3203193A Cited
US3217502A Cited
US3312074A Cited
US3319427A Cited
US3340697A Cited
US3375673A Cited
US3546892A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-06-04 1976-12-04 1977-06-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-06-04 1980-12-04 1981-06-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-06-04 1984-12-04 1985-06-05 $7700.00 Window Closed / Lapsed

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