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US3903708A Expired / Lapsed US ⏱️ 0.0 years remaining

Volatile vapor recovery system and method utilizing joule thompson expansion

Assignee: BROWN-MINNEAPOLIS TANK & FABRICATING Co A MN CORP
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Filing: 1973-05-07
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Granted: 1975-09-09
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Expires: 1993-05-07
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Abstract

Abstract A system for recovering volatile combustible liquids from a vapor stream includes a saturating vessel for rendering the vapor stream non-explosive, a plurality of high-pressure ambient aircooled condensing stages, each stage compressing the vapor stream and then cooling it to ambient temperature without the use of refrigeration for forming liquid product and residual vapors, an expansion vessel for receiving the vapors from the last condensing stage and further cooling and condensing them by Joule-Thompson expansion, means for returning recovered liquid product from the condensing stages and the expansion vessel to the saturating vessel, and means for venting the residual vapors from the expansion vessel. Means is also provided for cycling compressor coolant through one of the condensing stages.

Inventors

  • 👤 James Mair

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 15:31
CPC Classifications
B; B67; B67D; B67D7/00; B67D7/04; B67D7/0476

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 190 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a plurality of stages of condensing apparatus, each of said stages including a compressor having an inlet and an outlet and ambient-air-cooled condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, the inlet of the first stage compressor being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, the inlet of said compressor of each of the other stages being connected to the vapor outlet of said condensing means of the immediately preceding stage for receiving the cooled vapor stream therefrom, vent means connected to the vapor outlet of the last stage condensing means for discharging to atmosphere the uncondensed vapor stream therefrom, compressor cooling means for circulating a coolant other than said liquid product through said compressor in each of said stages and through said condensing means in one of said stages, and a liquid product reservoir connected to the liquid product outlets of said condensing means of each of said stages for receiving therefrom the recovered liquid product.
Claim 2
Dependent Claim 190 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a plurality of stages of condensing apparatus, each of said stages including a compressor having an inlet and an outlet and ambient-air-cooled condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, the inlet of the first stage compressor being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, the inlet of said compressor of each of the other stages being connected to the vapor outlet of said condensing means of the immediately preceding stage for receiving the cooled vapor stream therefrom, vent means connected to the vapor outlet of the last stage condensing means for discharging to atmosphere the uncondensed vapor stream therefrom, compressor cooling means for circulating a coolant other than said liquid product through said compressor in each of said stages and through said condensing means in one of said stages, and a liquid product reservoir connected to the liquid product outlets of said condensing means of each of said stages for receiving therefrom the recovered liquid product.
Claim 3
Dependent Claim 54 words
The apparatus set forth in claim 1, wherein the input vapor stream includes combustible hydrocarbons, said condensing apparatus included two stages, said first stage compressor compressing the vapor stream to approximately 65 p.s.i.a. at approximately 232* F., said second stage compressor further compressing the vapor stream to approximately 275 p.s.i.a. at approximately 230* F.
Claim 4
Dependent Claim 153 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a compressor having an inlet and an outlet, said inlet being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, aMbient-air-cooled condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, an expansion vessel having an inlet connected to the vapor outlet of said condensing means and a vapor outlet and a liquid product outlet, said expansion vessel effecting further cooling and condensing of the cooled compressed vapor stream from said condensing means by Joule-Thompson expansion thereof, vent means connected to the vapor outlet of said expansion vessel for discharging to the atmosphere the uncondensed vapor stream therefrom, and a liquid product reservior connected to the liquid product outlets of said condensing means and said expansion vessel for receiving therefrom the recovered liquid product.
Claim 5
Dependent Claim 153 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a compressor having an inlet and an outlet, said inlet being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, aMbient-air-cooled condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, an expansion vessel having an inlet connected to the vapor outlet of said condensing means and a vapor outlet and a liquid product outlet, said expansion vessel effecting further cooling and condensing of the cooled compressed vapor stream from said condensing means by Joule-Thompson expansion thereof, vent means connected to the vapor outlet of said expansion vessel for discharging to the atmosphere the uncondensed vapor stream therefrom, and a liquid product reservior connected to the liquid product outlets of said condensing means and said expansion vessel for receiving therefrom the recovered liquid product.
Claim 6
Dependent Claim 23 words
The apparatus set forth in claim 3, wherein said expansion vessel reduces the pressure of the compressed vapor stream to approximately 5 p.s.i.g.
Claim 7
Dependent Claim 211 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a plurality of stages of condensing apparatus, each of said stages including a compressor having an inlet and an outlet and condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, the inlet of the first stage compressor being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, the inlet of said compressor of each of the other stages being connected to the vapor outlet of said condensing means of the immediately preceding stage for receiving the cooled vapor stream therefrom, an expansion vessel having an inlet connected to the vapor outlet of the last stage condensing means and a vapor outlet and a liquid product outlet, said expansion vessel effecting further cooling and condensing of the cooled compressed vapor stream from the last stage condensing means by Joule-Thompson expansion thereof, vent means connected to the vapor outlet of said expansion vessel for discharging to atmosphere the uncondensed vapor stream therefrom, and a liquid product reservoir connected to the liquid product outlets of said condensing means of each of said stages and said expansion vessel for receiving therefrom the recovered liquid product.
Claim 8
Dependent Claim 211 words
Apparatus for recovering volatile liquids from a vapor stream, said apparatus comprising a plurality of stages of condensing apparatus, each of said stages including a compressor having an inlet and an outlet and condensing means having an inlet connected to the outlet of said compressor and a vapor outlet and a liquid product outlet, the inlet of the first stage compressor being adapted for connection to an associated vapor source for receiving therefrom an input vapor stream, the inlet of said compressor of each of the other stages being connected to the vapor outlet of said condensing means of the immediately preceding stage for receiving the cooled vapor stream therefrom, an expansion vessel having an inlet connected to the vapor outlet of the last stage condensing means and a vapor outlet and a liquid product outlet, said expansion vessel effecting further cooling and condensing of the cooled compressed vapor stream from the last stage condensing means by Joule-Thompson expansion thereof, vent means connected to the vapor outlet of said expansion vessel for discharging to atmosphere the uncondensed vapor stream therefrom, and a liquid product reservoir connected to the liquid product outlets of said condensing means of each of said stages and said expansion vessel for receiving therefrom the recovered liquid product.
Claim 9
Dependent Claim 40 words
The apparatus set forth in claim 5, wherein the last stage compressor effects compression of the vapor stream to approximately 275 p.s.i.a. at approximately 230* F., said expansion vessel effecting expansion of the compressed vapor stream to approximately 5 p.s.i.g.
Claim 10
Independent Claim 87 words
A method for recovering volatile liquids from an input vapor stream, said method comprising steps of compressing the input vapor stream in a plurality of compression stages, condensing the compressed vapor stream by cooling it in a plurality of condensing stages alternating with said compression stages, expanding the vapor stream from the last condensing stage by Joule-Thompson expansion for further cooling and condensing thereof, venting to atmosphere the uncondensed expanded vapors, and collecting the liquid product recovered in each of the condensing stages and the expansion step.
Claim 11
Independent Claim 87 words
A method for recovering volatile liquids from an input vapor stream, said method comprising steps of compressing the input vapor stream in a plurality of compression stages, condensing the compressed vapor stream by cooling it in a plurality of condensing stages alternating with said compression stages, expanding the vapor stream from the last condensing stage by Joule-Thompson expansion for further cooling and condensing thereof, venting to atmosphere the uncondensed expanded vapors, and collecting the liquid product recovered in each of the condensing stages and the expansion step.
Claim 12
Dependent Claim 25 words
The method of claim 7, wherein the Joule-Thompson expansion of the cooled compressed vapor stream effects reduction of the pressure thereof to approximately 5 p.s.i.g.
Claim 13
Dependent Claim 39 words
The method set forth in claim 7, wherein the input vapor stream includes a mixture of combustible hydrocarbons, and further including the step of correcting the concentration of the hydrocarbons of the input vapor stream to a non-explosive level.

References Cited (Backward Citations)

US1918100A Cited
US2849150A Cited
US2976695A Cited
US3079760A Cited
US3091097A Cited
US3188824A Cited
US3613387A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-08 1979-03-10 1979-09-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-08 1983-03-10 1983-09-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-08 1987-03-10 1987-09-09 $7700.00 Window Closed / Lapsed

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