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US4597779A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for inhibiting hydrates while producing moist CO2 from subterranean reservoirs

Assignee: Shell USA Inc
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Filing: 1985-02-27
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Granted: 1986-07-01
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Expires: 2005-02-27
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Abstract

Abstract In producing CO 2 from subterranean reservoirs at conditions apt to cause two-phase flow in pipes conveying the fluid, the formation of hydrates is prevented by adding a polyhydric alcohol hydrate inhibitor in proportions capable of maintaining an effective concentration within the aqueous liquid-phase in spite of partitioning of the inhibitor into a CO 2 -rich liquid-phase of many times greater volume.

Inventors

  • 👤 Zaida Diaz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:19
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/26; B01D53/263

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 236 words
In a CO 2 -producing process in which moist CO 2 is produced at high pressure from a subterranean well, is mixed with a hydrate inhibitor and is piped to a facility for drying CO 2 and subsequently supplying it for use at high pressure, an improvement for avoiding the need for producing and piiping the CO 2 at pressures and temperatures maintaining a single phase state comprising: conducting said producing and piping of moist CO 2 at pressure and temperature conditions of at least about 500 psia but less than critical conditions and the ambient temperature near the wellhead apt to convert the fluid being piped to a fluid containing both an aqueous liquid-phase and a CO 2 -rich liquid-phase having a volume which is many times greater than that of the aqueous liquid-phase; mixing the so produced moist CO 2 with sufficient hydrate inhibitor to cause the concentration remaining in said aqueous phase to be sufficient to prevent hydrate formation in spite of the amount of inhibitor which will be partitioned into said CO 2 -phase; and using as said hydrate inhibitor a polyhydric alcohol hydrate inhibitor having a solubility in CO 2 at the conditions in the pipe which is low relative to the solubility of methanol in that CO 2 , so that, while simplifying the producing and piping operations, both the contamination of CO 2 and loss of inhibitor are minimized.
Claim 2
Dependent Claim 236 words
In a CO 2 -producing process in which moist CO 2 is produced at high pressure from a subterranean well, is mixed with a hydrate inhibitor and is piped to a facility for drying CO 2 and subsequently supplying it for use at high pressure, an improvement for avoiding the need for producing and piiping the CO 2 at pressures and temperatures maintaining a single phase state comprising: conducting said producing and piping of moist CO 2 at pressure and temperature conditions of at least about 500 psia but less than critical conditions and the ambient temperature near the wellhead apt to convert the fluid being piped to a fluid containing both an aqueous liquid-phase and a CO 2 -rich liquid-phase having a volume which is many times greater than that of the aqueous liquid-phase; mixing the so produced moist CO 2 with sufficient hydrate inhibitor to cause the concentration remaining in said aqueous phase to be sufficient to prevent hydrate formation in spite of the amount of inhibitor which will be partitioned into said CO 2 -phase; and using as said hydrate inhibitor a polyhydric alcohol hydrate inhibitor having a solubility in CO 2 at the conditions in the pipe which is low relative to the solubility of methanol in that CO 2 , so that, while simplifying the producing and piping operations, both the contamination of CO 2 and loss of inhibitor are minimized.
Claim 3
Dependent Claim 24 words
The process of claim 1 in which a significant fraction of the CO 2 being piped is present as a CO 2 -rich liquid-phase.
Claim 4
Dependent Claim 21 words
The process of claim 1 in which the pressure of the CO 2 being piped is greater than about 500 psi.
Claim 5
Dependent Claim 26 words
The process of claim 1 in which a significant proportion of water is removed from the produced CO 2 -containing fluid before the inhibitor is added.
Claim 6
Dependent Claim 21 words
The process of claim 1 in which the inhibitor is a compound of the group ethylene glycol, diethylene glycol and glycerol.
Claim 7
Dependent Claim 50 words
The process of claim 5 in which the inhibitor is a compound of the group diethylene glycol and glycerol and the drying agent utilized for dehydrating the CO 2 in the dehydration facility contains reconstituted portions of the same compound used as the hydrate inhibitor for the CO 2 .
Claim 8
Dependent Claim 12 words
The process of claim 6 in which the hydrate inhibitor is glycerol.

References Cited (Backward Citations)

US3495380A Cited
US3676981A Cited
JPS4918268A Cited
US4235289A Cited
US4478612A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-06-30 1989-12-30 1990-07-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-06-30 1993-12-30 1994-07-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-06-30 1997-12-30 1998-07-01 $7700.00 Window Closed / Lapsed

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