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US4469032A Expired / Lapsed US ⏱️ 0.0 years remaining

Zone combustion of high sulfur coal to reduce SOx emission

Assignee: Mobil Oil AS
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Filing: 1982-09-16
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Granted: 1984-09-04
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Expires: 2002-09-16
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Abstract

Abstract In the combustion of high sulfur coal, SOx emission is reduced by pyrolizing the coal in a reducing atmosphere to form char and convert the sulfur compounds to combustible gases including H2S. The H2S is reacted with the coal and the char to produce ash containing sulfur which is easily removed from the combustion process. A three zone furnace includes a zone in which the coal is pyrolized in a reducing atmosphere to convert the sulfur compounds to combustible gas which reacts with the coal and char.

Inventors

  • 👤 Tsoung Y. Yan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 18:45
CPC Classifications
F; F23; F23B; F23B90/00; F23B90/04; F23B90/06; F23B7/00

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 129 words
The method of reducing SO x emission in the combustion of coal which contains sulfur compounds comprising: combusting coal and char in an oxidizing atmosphere at high temperature; pyrolizing said coal in a reducing atmosphere to form said char and to convert said sulfur compounds to combustible gas including H 2 S; restricting the flow of air to said coal during combusting to minimize the excess oxygen present during the step of pyrolizing; adding steam during the step of combusting to produce hydrogen; supplying said hydrogen to said pyrolizing step; adding a basic mineral scavenger during pyrolizing; reacting said H 2 S with a basic mineral in said coal, said scavenger and said char to produce ash containing sulfur; and removing said ash containing sulfur from the combustion process.
Claim 2
Independent Claim 129 words
The method of reducing SO x emission in the combustion of coal which contains sulfur compounds comprising: combusting coal and char in an oxidizing atmosphere at high temperature; pyrolizing said coal in a reducing atmosphere to form said char and to convert said sulfur compounds to combustible gas including H 2 S; restricting the flow of air to said coal during combusting to minimize the excess oxygen present during the step of pyrolizing; adding steam during the step of combusting to produce hydrogen; supplying said hydrogen to said pyrolizing step; adding a basic mineral scavenger during pyrolizing; reacting said H 2 S with a basic mineral in said coal, said scavenger and said char to produce ash containing sulfur; and removing said ash containing sulfur from the combustion process.
Claim 3
Dependent Claim 21 words
The method recited in claim 1 further comprising: introducing secondary air; and combusting the unreacted combustible gas from the pyrolizing step.
Claim 4
Dependent Claim 30 words
The method recited in claim 1 wherein said basic mineral includes calcium carbonate and magnesium carbonate and the reaction is: CaCO.sub.3 +H.sub.2 S→CaS+CO.sub.2 +H.sub.2 O MgCO.sub.3 +H.sub.2 S→MgS+CO.sub.2 +H.sub.2 O
Claim 5
Dependent Claim 14 words
The method recited in claim 1 wherein said basic mineral scavenger is calcium carbonate.
Claim 6
Dependent Claim 13 words
The method recited in claim 1 wherein said basic mineral scavenger is dolomite.
Claim 7
Dependent Claim 14 words
The method recited in claim 1 wherein said basic mineral scavenger is soda ash.
Claim 8
Dependent Claim 20 words
The method recited in claim 1 wherein the step of pyrolizing is carried out at a temperature above 500° C.
Claim 9
Dependent Claim 21 words
The method recited in claim 1 wherein the step of pyrolizing is carried out at a temperature of approximately 600° C.
Claim 10
Independent Claim 154 words
A method of operating a furnace for the combustion of coal, containing sulfur compounds, with reduced SO x emission comprising: supplying primary air to a first zone in said furnace for combustion of materials in said first zone; maintaining a reducing atmosphere in a second zone in said furnace above said first zone for pyrolizing coal supplied to said second zone forming char in said second zone; adding steam to said first zone to produce hydrogen during combustion; supplying said hydrogen to said second zone during pyrolizing; converting said sulfur compounds to combustible gas in said second zone, said combustible gas including H 2 S: supplying a basic mineral scavenger to said second zone; reacting with H 2 S with said coal, said scavenger and said char in said second zone to produce ash containing sulfur; supplying said char to said first zone for combustion; and removing said ash containing sulfur from said furnace.
Claim 11
Independent Claim 154 words
A method of operating a furnace for the combustion of coal, containing sulfur compounds, with reduced SO x emission comprising: supplying primary air to a first zone in said furnace for combustion of materials in said first zone; maintaining a reducing atmosphere in a second zone in said furnace above said first zone for pyrolizing coal supplied to said second zone forming char in said second zone; adding steam to said first zone to produce hydrogen during combustion; supplying said hydrogen to said second zone during pyrolizing; converting said sulfur compounds to combustible gas in said second zone, said combustible gas including H 2 S: supplying a basic mineral scavenger to said second zone; reacting with H 2 S with said coal, said scavenger and said char in said second zone to produce ash containing sulfur; supplying said char to said first zone for combustion; and removing said ash containing sulfur from said furnace.
Claim 12
Dependent Claim 32 words
The method recited in claim 9 further comprising: supplying secondary air to a third zone in said furnace above said second zone for combustion of said combustible gas from said second zone.
Claim 13
Dependent Claim 23 words
The method recited in claim 9 further comprising: removing said ash from said first zone, said sulfur compounds being fixed in said ash.
Claim 14
Dependent Claim 15 words
The method recited in claim 10 further comprising: removing flue gas from said third zone.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-09-04 1988-03-05 1988-09-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-09-04 1992-03-05 1992-09-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-09-04 1996-03-05 1996-09-04 $7700.00 Window Closed / Lapsed

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