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US4966684A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the removal of mercury from natural gas condensate

Assignee: Mobil Oil AS
•
Filing: 1989-04-27
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Granted: 1990-10-30
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Expires: 2009-04-27
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Abstract

Abstract A process for the removal of mercury from natural gas condensate wherein the natural gas condensate is passed over a catalyst, while also passing a stream of methane containing hydrogen sulfide over the catalyst.

Inventors

  • 👤 Costandi A. Audeh

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 15:23
CPC Classifications
C; C10; C10L; C10L3/00; C10L3/06; C10L3/10

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 40 words
A process for the removal of mercury from natural gas condensate comprising the steps of: passing said natural gas condensate over a catalyst in a reactor vessel and simultaneously passing a mixture of methane and hydrogen sulfide over said catalyst.
Claim 2
Dependent Claim 40 words
A process for the removal of mercury from natural gas condensate comprising the steps of: passing said natural gas condensate over a catalyst in a reactor vessel and simultaneously passing a mixture of methane and hydrogen sulfide over said catalyst.
Claim 3
Dependent Claim 29 words
A process according to claim 1 wherein said catalyst is presulfided by passing hydrogen sulfide over said catalyst prior to passing said condensate and said mixture over said catalyst.
Claim 4
Dependent Claim 19 words
A process according to claim 1 wherein said reactor vessel is maintained at a pressure of about 5-40 atmospheres.
Claim 5
Dependent Claim 19 words
A process according to claim 1 wherein said reactor vessel is maintained at a pressure of about 10-15 atmospheres.
Claim 6
Dependent Claim 19 words
A process according to claim 1 wherein said reactor vessel is maintained at a temperature of about 100-300° C.
Claim 7
Dependent Claim 19 words
A process according to claim 1 wherein said reactor vessel is maintained at a temperature of about 200-250° C.
Claim 8
Dependent Claim 29 words
A process according to claim 1 wherein the volume of said condensate passing over said catalyst every hour divided by the volume of said catalyst is below about 20.
Claim 9
Dependent Claim 18 words
A process according to claim 1 wherein said mixture comprises between about 20 ppm-50% by volume hydrogen sulfide.
Claim 10
Dependent Claim 17 words
A process according to claim 1 wherein said mixture comprises between about 0.2-0.5% by volume hydrogen sulfide.
Claim 11
Dependent Claim 66 words
A process for the removal of mercury from natural gas condensate comprising the steps of: passing said natural gas condensate over a cobalt/molybdenum catalyst in a reactor vessel which is maintained at a pressure of about 5-40 atmospheres and a temperature of about 100°-300° C., and simultaneously passing a mixture of methane and hydrogen sulfide comprising about 20 ppm-50% by volume hydrogen sulfide over said catalyst.
Claim 12
Dependent Claim 66 words
A process for the removal of mercury from natural gas condensate comprising the steps of: passing said natural gas condensate over a cobalt/molybdenum catalyst in a reactor vessel which is maintained at a pressure of about 5-40 atmospheres and a temperature of about 100°-300° C., and simultaneously passing a mixture of methane and hydrogen sulfide comprising about 20 ppm-50% by volume hydrogen sulfide over said catalyst.
Claim 13
Dependent Claim 29 words
A process according to claim 10 wherein said catalyst is presulfided by passing hydrogen sulfide over said catalyst prior to passing said condensate and said mixture over said catalyst.
Claim 14
Dependent Claim 19 words
A process according to claim 10 wherein said reactor vessel is maintained at a pressure of about 10-15 atmospheres.
Claim 15
Dependent Claim 19 words
A process according to claim 10 wherein said reactor vessel is maintained at a temperature of about 200-250° C.
Claim 16
Dependent Claim 29 words
A process according to claim 10 wherein the volume of said condensate passing over said catalyst every hour divided by the volume of said catalyst is below about 20.
Claim 17
Dependent Claim 17 words
A process according to claim 10 wherein said mixture comprises between about 0.2-0.5% by volume hydrogen sulfide.

References Cited (Backward Citations)

US2905636A Cited
US4044098A Cited
US4430206A Cited
US4764219A Cited
US4915818A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-10-29 1994-04-30 1994-10-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-10-29 1998-04-30 1998-10-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-10-29 2002-04-30 2002-10-30 $7700.00 Window Closed / Lapsed

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