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US3707849A Expired / Lapsed US ⏱️ 0.0 years remaining

Fractionation of air by using refrigeration from open cycle evaporation of external cryogenic liquid

Assignee: Linde GmbH
•
Filing: 1970-03-03
•
Granted: 1973-01-02
•
Expires: 1990-03-03
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Abstract

Abstract A system for the low temperature fractionation of air is provided wherein gaseous nitrogen is withdrawn from the rectification column and passed in indirect heat exchange relationship with a vaporizing external refrigerant such as methane or natural gas. The resultant liquified nitrogen is recycled to the column and acts as reflux liquid therein. To provide make-up refrigeration for liquid products that are removed from the system without passing through the main heat exchanger, a portion of the withdrawn nitrogen is heated in the main heat exchanger, thereby cooling the incoming air. The warmed nitrogen is then pre-cooled and subsequently liquefied by the external refrigerant. The nitrogen recycle steps are conducted at approximately the same pressure of nitrogen thereby eliminating the need for compressor and expansion valves on said recycle line.

Inventors

  • 👤 R Becker

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 10:05
CPC Classifications
F; F17; F17C; F17C9/00; F17C9/02; F17C9/04; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04187; F25J3/04218; F25J3/04224; F25J3/04248; F25J3/04254; F25J3/0426; F25J3/04266; F25J3/04333; F25J3/04351; F25J3/04406; F25J3/04412; F17C2221/00; F17C2221/01; F17C2221/014; F17C2221/03; F17C2221/031; F17C2227/00; F17C2227/03; F17C2227/0367; F17C2227/0388; F17C2227/0393; F17C2265/00; F17C2265/01; F17C2265/015; Y; Y10; Y10S; Y10S62/00; Y10S62/912

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 248 words
In a process for the low-temperature separation of air in an air fractionating column, wherein refrigeration is supplied by the evaporation of methane used as an external refrigerant, and wherein the transfer of the cold from the refrigerant to the air is conducted by way of an intermediate auxiliary gas, the improvement comprising the steps of: withdrawing nitrogen gas from said air fractionating column, dividing the withdrawn nitrogen into two partial streams, warming one of said partial streams of nitrogen to ambient temperature in indirect heat exchange with unfractionated air, precooling resultant warmed partial stream in heat exchange with said refrigerant, the latter being at a pressure of about 1 atmosphere absolute, passing both said precooled partial streams of nitrogen and the other of said two partial streams of nitrogen as said auxiliary gas, in indirect heat exchange relationship with said methane refrigerant, the latter evaporating at a pressure of 0.12 - 0.3 atmospheres absolute, thereby condensing said nitrogen, returning resultant liquid nitrogen to the air fractionating column, and employing said liquid nitrogen as reflux liquid, with the provision that the steps of withdrawing said nitrogen from the air fractionating column, condensing said nitrogen, returning said liquid nitrogen tO the column and of employing said liquid nitrogen as reflux are conducted at approximately the same pressure within the range of 4 - 8 atmospheres absolute, with the further provision that said methane be maintained out of heat exchange contact with said air through a common heat exchange wall.
Claim 2
Dependent Claim 248 words
In a process for the low-temperature separation of air in an air fractionating column, wherein refrigeration is supplied by the evaporation of methane used as an external refrigerant, and wherein the transfer of the cold from the refrigerant to the air is conducted by way of an intermediate auxiliary gas, the improvement comprising the steps of: withdrawing nitrogen gas from said air fractionating column, dividing the withdrawn nitrogen into two partial streams, warming one of said partial streams of nitrogen to ambient temperature in indirect heat exchange with unfractionated air, precooling resultant warmed partial stream in heat exchange with said refrigerant, the latter being at a pressure of about 1 atmosphere absolute, passing both said precooled partial streams of nitrogen and the other of said two partial streams of nitrogen as said auxiliary gas, in indirect heat exchange relationship with said methane refrigerant, the latter evaporating at a pressure of 0.12 - 0.3 atmospheres absolute, thereby condensing said nitrogen, returning resultant liquid nitrogen to the air fractionating column, and employing said liquid nitrogen as reflux liquid, with the provision that the steps of withdrawing said nitrogen from the air fractionating column, condensing said nitrogen, returning said liquid nitrogen tO the column and of employing said liquid nitrogen as reflux are conducted at approximately the same pressure within the range of 4 - 8 atmospheres absolute, with the further provision that said methane be maintained out of heat exchange contact with said air through a common heat exchange wall.
Claim 3
Dependent Claim 34 words
A process as defined by claim 1, wherein said air fractionating column is a double column and the nitrogen gas is withdrawn from the high-pressure column and is returned as liquid to the same.

References Cited (Backward Citations)

US2685181A Cited
US3058314A Cited
US3107992A Cited
US3183677A Cited
US3216206A Cited
US3339370A Cited
US3492828A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-01-02 1976-07-03 1977-01-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-01-02 1980-07-03 1981-01-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-01-02 1984-07-03 1985-01-02 $7700.00 Window Closed / Lapsed

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