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US4948393A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of separating oil, water, sand, and gas from produced fluids

Assignee: Chevron USA Inc
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Filing: 1989-07-07
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Granted: 1990-08-14
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Expires: 2009-07-07
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Abstract

Abstract The invention deals with separating production fluids into separate components of oil, water, sand and gas in first and second stage separators. Preheating of the production fluid prior to entry into the first stage separator is partially accomplished by direct mixing with hot processed water taken from the effluent of the first stage separator and the second stage separator. Recirculated processed water may also be used to improve sand removal from the first and second stage separators.

Inventors

  • 👤 John E. Hodson
  • 👤 Michael D. Chalmers

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 02:18
CPC Classifications
B; B01; B01D; B01D19/00; B01D19/0068; B01D17/00; B01D17/02; B01D17/0208; B01D17/0217; B01D17/04; B01D17/042; B01D17/047; B01D19/0005

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 368 words
A method of separating fluids produced from a production well into separate components of oil, gas, water, and sand comprising flowing production fluid containing oil, water, gas, and sand from a production location toward a first stage separator, prior to flowing said production fluid to said first stage separator mixing said production fluid with heated produced water obtained from the effluent of said first stage separator and having a temperature of between about 120° C. to 160° C. in sufficient amount to heat said production fluid to between about 50° C. to 80° C., flowing said heated production fluid into said first stage separator to permit a first stage separation of the production fluid into a primarily gas component, a primarily oil-gas-water-sand component and a primarily produced water-sand component, continuing to separate substantial portion of produced water from the produced water-sand component in said first stage separator and passing a portion of said produced water to a first heater to heat said produced water to between about 120° C. to 160° C., continuing to mix said heated produced water with said production fluids prior to passing said production fluid to said first stage separator, removing gas from said first stage separator, and removing sand from said first stage separator, removing the oil-gas-water-sand component from said first stage separator, reheating said oil-gas-water-sand component to a temperature of between about 80° C. to 110° C., flowing said reheated oil-gas-water-sand component to a second stage separator, separating said oil-gas-water-sand into a gas component, a produced water component, a sand component and an oil component, removing gas from said second stage separator, removing sand from said second stage separator, removing oil from said second stage separator, removing produced water from said second stage separator, passing said removed oil in heat exchange contact with said oil-gas-water-sand component prior to flowing said oil-gas-water-sand component into said second stage separator and circulating a portion of the produced water effluent from said second stage separator and combining said portion of produced water with the produced water from said first stage separator prior to heating the produced water to between about 120° C. to about 160° C. for mixing with produced fluids coming from said production well.
Claim 2
Independent Claim 368 words
A method of separating fluids produced from a production well into separate components of oil, gas, water, and sand comprising flowing production fluid containing oil, water, gas, and sand from a production location toward a first stage separator, prior to flowing said production fluid to said first stage separator mixing said production fluid with heated produced water obtained from the effluent of said first stage separator and having a temperature of between about 120° C. to 160° C. in sufficient amount to heat said production fluid to between about 50° C. to 80° C., flowing said heated production fluid into said first stage separator to permit a first stage separation of the production fluid into a primarily gas component, a primarily oil-gas-water-sand component and a primarily produced water-sand component, continuing to separate substantial portion of produced water from the produced water-sand component in said first stage separator and passing a portion of said produced water to a first heater to heat said produced water to between about 120° C. to 160° C., continuing to mix said heated produced water with said production fluids prior to passing said production fluid to said first stage separator, removing gas from said first stage separator, and removing sand from said first stage separator, removing the oil-gas-water-sand component from said first stage separator, reheating said oil-gas-water-sand component to a temperature of between about 80° C. to 110° C., flowing said reheated oil-gas-water-sand component to a second stage separator, separating said oil-gas-water-sand into a gas component, a produced water component, a sand component and an oil component, removing gas from said second stage separator, removing sand from said second stage separator, removing oil from said second stage separator, removing produced water from said second stage separator, passing said removed oil in heat exchange contact with said oil-gas-water-sand component prior to flowing said oil-gas-water-sand component into said second stage separator and circulating a portion of the produced water effluent from said second stage separator and combining said portion of produced water with the produced water from said first stage separator prior to heating the produced water to between about 120° C. to about 160° C. for mixing with produced fluids coming from said production well.
Claim 3
Dependent Claim 39 words
The method of claim 1 further characterized in that a portion of the produced water removed from said first stage separator is recirculated back into said first stage separator to assist in removing sand from said first stage separator.

References Cited (Backward Citations)

US2457959A Cited
US2765045A Cited
US3469373A Cited
US3759324A Cited
US4778443A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-08-13 1994-02-12 1994-08-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-08-13 1998-02-12 1998-08-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-08-13 2002-02-12 2002-08-14 $7700.00 Window Closed / Lapsed

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