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US4380907A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of boiling liquefied gas

Assignee: Cryoplants Ltd
•
Filing: 1981-07-09
•
Granted: 1983-04-26
•
Expires: 2001-07-09
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Abstract

Abstract A method of boiling a liquefied gas in a heat exchanger 10 includes the step of introducing a seed gas via a pipeline 18 to spray nozzles 34 situated under passages 22 of the heat exchanger 10 for reboiling the liquefied gas, e.g. oxygen. The passages 22 alternate with passages 24 for condensing nitrogen vapor. The seed gas bubbles are trapped by cavities formed in the heat exchange surfaces where boiling of the oxygen takes place. Each cavity is of such a size and shape that the trapped bubbles grow until they break away from the cavity leaving residues of vapor therein sufficient to allow further gas to accummulate by evaporation until again bubbles break away.

Inventors

  • 👤 Robert S. Barnes
  • 👤 Raymond Harper

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 04:30
CPC Classifications
F; F28; F28F; F28F27/00; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04406; F25J3/04412; F25J5/00; F25J5/002; F28F13/00; F28F13/18; F28F13/185; F28F13/187; F25J2245/00; F25J2245/50; F25J2250/00; F25J2250/02; F25J2290/00; F25J2290/32; F25J2290/44

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 129 words
A method of boiling a liquefied gas in a heat exchanger having cavities formed in heat exchange surfaces comprising the steps of: (a) passing another fluid into said heat exchanger in indirect heat exchange relation with said liquefied gas to thereby supply thermal energy to said liquefied gas; (b) introducing bubbles of a seeding gas into the liquefied gas in the heat exchanger; (c) trapping at least some of said bubbles of seeding gas in said cavities; and (d) retaining said trapped bubbles in said cavities until said bubbles increase to a size such that said bubbles break away from said cavities while leaving a sufficient residue of vapors of the liquefied gas in the cavities to enable further bubbles to form therein by boiling of said liquefied gas.
Claim 2
Independent Claim 129 words
A method of boiling a liquefied gas in a heat exchanger having cavities formed in heat exchange surfaces comprising the steps of: (a) passing another fluid into said heat exchanger in indirect heat exchange relation with said liquefied gas to thereby supply thermal energy to said liquefied gas; (b) introducing bubbles of a seeding gas into the liquefied gas in the heat exchanger; (c) trapping at least some of said bubbles of seeding gas in said cavities; and (d) retaining said trapped bubbles in said cavities until said bubbles increase to a size such that said bubbles break away from said cavities while leaving a sufficient residue of vapors of the liquefied gas in the cavities to enable further bubbles to form therein by boiling of said liquefied gas.
Claim 3
Dependent Claim 48 words
The method defined in claim 1 additionally comprising the steps of monitoring the temperature difference between the temperatures of said boiling liquefied gas and said heat exchange surfaces, and interrupting the introduction of said bubbles of seeding gas while said monitored temperature difference is below a predetermined value.
Claim 4
Dependent Claim 31 words
The method defined in claim 1 wherein said fluid is a vapor and additionally comprising the step of condensing said vapor in said heat exchanger while said liquefied gas is boiled.
Claim 5
Dependent Claim 57 words
The method defined in claim 3 additionally comprising the steps of monitoring (1) the pressure of vapor of said liquefied gas in said heat exchanger and (2) the pressure of said vapor which is condensed in said heat exchanger, and interrupting the introduction of said seeding gas upon the difference between said pressures exceeding a predetermined value.
Claim 6
Dependent Claim 36 words
The method defined in claim 1 wherein said step of introducing bubbles of said seeding gas comprises injecting bubbles into said liquefied gas prior to passing said liquefied gas and said bubbles into said heat exchanger.

References Cited (Backward Citations)

US3012408A Cited
US3400545A Cited
US3378063A Cited
US4018264A Cited
US4159739A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-04-25 1986-10-25 1987-04-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-04-25 1990-10-25 1991-04-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-04-25 1994-10-25 1995-04-26 $7700.00 Window Closed / Lapsed

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