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US3858403A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for drying gases

Assignee: Wilkerson Corp
•
Filing: 1974-01-30
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Granted: 1975-01-07
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Expires: 1994-01-30
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Abstract

Abstract This invention relates to a method and apparatus for drying compressed gas that is to be used at or near the supply pressure in which the temperature sensor of a thermostatically controlled valve responds to the temperature of the incoming wet gas leaving a heat exchanger by cycling on and off a supply of gas to a vortex tube. The cold side of the vortex tube is the prime source of refrigerant for the heat exchanger supplemented by the partially dried gas following removal of the condensate therefrom which is recycled so as to re-enter the exchanger at a point where its temperature is the same or slightly lower than that of the prime source of refrigerant. The invention also contemplates exhausting the hot gases from the vortex tube to the atmosphere outside the main dryer housing while dumping the cold vortex tube fraction inside a housing within the latter as it leaves the heat exchanger. The invention further encompasses using a portion of the incoming wet gas as the supply for the vortex tube.

Inventors

  • 👤 Myron Dunn

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 19:09
CPC Classifications
F; F25; F25B; F25B9/00; F25B9/02; F25B9/04; B; B01; B01D; B01D53/00; B01D53/26

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 239 words
The gas drying apparatus which comprises: a triple pass heat exchanger having the inlet to its first pass connectable to a source of wet gas under pressure, a vortex tube operative to split an incoming stream of gas into a relatively warmer fraction and a relatively cooler fraction connected to deliver the latter to the second pass of the heat exchanger for movement therein in heat exchange relation to the wet gas moving through said first pass, a separator effective to remove the condensate condensed from the wet gas in the heat exchanger connected to receive the partially dried gas issuing from the first pass of the latter, first conduit means connected to receive the partially dried gas from the separator following removal of the condensate therefrom and recycle same into the third pass of the heat exchanger for flow therethrough alongside the gases flowing in said first and second passes so as to maximize heat transfer from the wet gas in said first pass without warming the cold gas in said second pass, second conduit means connected to receive a portion of the gas entering the first pass and deliver same to the vortex tube, and thErmostatically controlled valve means connected in the second conduit means operative upon actuation to shut off the gas supply to the vortex tube whenever the temperature of the gas leaving the first pass of the heat exchanger falls below a preset minimum.
Claim 2
Dependent Claim 239 words
The gas drying apparatus which comprises: a triple pass heat exchanger having the inlet to its first pass connectable to a source of wet gas under pressure, a vortex tube operative to split an incoming stream of gas into a relatively warmer fraction and a relatively cooler fraction connected to deliver the latter to the second pass of the heat exchanger for movement therein in heat exchange relation to the wet gas moving through said first pass, a separator effective to remove the condensate condensed from the wet gas in the heat exchanger connected to receive the partially dried gas issuing from the first pass of the latter, first conduit means connected to receive the partially dried gas from the separator following removal of the condensate therefrom and recycle same into the third pass of the heat exchanger for flow therethrough alongside the gases flowing in said first and second passes so as to maximize heat transfer from the wet gas in said first pass without warming the cold gas in said second pass, second conduit means connected to receive a portion of the gas entering the first pass and deliver same to the vortex tube, and thErmostatically controlled valve means connected in the second conduit means operative upon actuation to shut off the gas supply to the vortex tube whenever the temperature of the gas leaving the first pass of the heat exchanger falls below a preset minimum.
Claim 3
Dependent Claim 43 words
The gas drying apparatus as set forth in claim 1 in which: the gases in the second and third passes of the heat exchanger flow in concurrent flow relation to one another and countercurrent flow relation to the gas in the first pass.
Claim 4
Dependent Claim 72 words
The gas drying apparatus as set forth in claim 1 in which: the first conduit means delivers the partially dried gas to the third pass at a point intermediate the ends of the heat exchanger, said point being selected such that the temperature of said partially dried gas returning to the heat exchanger is at or below the temperature of the relatively warmer gas fraction moving alongside thereof in the second pass.
Claim 5
Dependent Claim 49 words
The gas drying apparatus as set forth in claim 1 in which: the thermostatically controlled valve means includes a temperature sensor; a housing houses the heat exchanger, separator, sensor and both conduit means; and, in which the relatively hotter gas fraction is exhausted to the atmosphere outside said housing.
Claim 6
Dependent Claim 33 words
The gas drying apparatus as set forth in claim 4 in which: the relatively colder gaseous fraction leaving the second pass of the heat exchanger is exhausted to the atmosphere within said housing.
Claim 7
Independent Claim 163 words
The method of drying a wet gas under pressure which comprises the steps of: condensing some of the moisture from the incoming wet gas by passing it in heat exchange relation to the relatively colder fraction of the same gas issuing from the cold side of a vortex tube, stripping the condensate from the incoming gas thus cooled, recycling the stripped gas in heat exchange relation to the incoming wet gas so as to cool and condense additional moisture from the latter, said recycled gas being returned at a point where its temperature is equal to or below that of the relatively warmer fraction from the vortex tube flowing alongside thereof, determining the temperature of the cool gas prior to removing the condensate therefrom, tapping off a portion of the incoming wet gas to supply the vortex tube, and cutting off the flow of incoming wet gas to said vortex tube whenever the temperature of the cool gas falls below the predetermined minimum.
Claim 8
Independent Claim 163 words
The method of drying a wet gas under pressure which comprises the steps of: condensing some of the moisture from the incoming wet gas by passing it in heat exchange relation to the relatively colder fraction of the same gas issuing from the cold side of a vortex tube, stripping the condensate from the incoming gas thus cooled, recycling the stripped gas in heat exchange relation to the incoming wet gas so as to cool and condense additional moisture from the latter, said recycled gas being returned at a point where its temperature is equal to or below that of the relatively warmer fraction from the vortex tube flowing alongside thereof, determining the temperature of the cool gas prior to removing the condensate therefrom, tapping off a portion of the incoming wet gas to supply the vortex tube, and cutting off the flow of incoming wet gas to said vortex tube whenever the temperature of the cool gas falls below the predetermined minimum.
Claim 9
Dependent Claim 40 words
The method as set forth in claim 6 in which: the relatively warmer fraction of gas exiting from the hot side of the vortex tube is exhausted to the atmosphere at a point remote from where the condensation takes place.
Claim 10
Dependent Claim 36 words
The method as set forth in claim 6 in which: the relatively colder fraction of gas is used to cool the environment in which the condensation is carried out following its use for the latter purpose.

References Cited (Backward Citations)

US2522787A Cited
US2741899A Cited
US3229470A Cited
US3460373A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-01-06 1978-07-08 1979-01-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-01-06 1982-07-08 1983-01-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-01-06 1986-07-08 1987-01-07 $7700.00 Window Closed / Lapsed

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