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US4523532A Expired / Lapsed US ⏱️ 0.0 years remaining

Combustion method

Assignee: Transalta Resources Corp
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Filing: 1984-01-17
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Granted: 1985-06-18
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Expires: 2004-01-17
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Abstract

Abstract A method and apparatus for combustion of a sulfur-containing fuel which substantially reduces the amount of gaseous sulfur compounds which would otherwise be emitted. A source of oxygen, a sulfur-containing fuel, and an inorganic alkaline absorbent are reacted under controlled conditions of temperature, stoichiometry, and residence time whereby the inorganic alkaline absorbent reacts with the fuel sulfur to form a mixture of combustion products and desired solid sulfur compounds, the latter being readily removed utilizing conventional filtration equipment. In a preferred embodiment of the invention, the mixture of fuel and combustion products is passed into a nitrogenous compound destruction zone wherein, under controlled conditions, the concentration of nitrogenous compounds present are reduced to a desired level.

Inventors

  • 👤 Michael P. Moriarty

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 12:53
CPC Classifications
F; F23; F23C; F23C6/00; F23C6/04

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 321 words
A method for the entrained-flow combustion of a carbon-, nitrogen- and sulfur-containing fuel for substantially reducing emission of gaseous sulfur compounds and nitrogenous compounds formed during the combustion of the fuel with a substoichiometric amount of oxygen-comprising; introducing said fuel, an inorganic alkaline absorbent and an oxygen-containing gas into a first combustion sulfur capture zone of an entrained-flow combustor to form a fluent mixture therein of fuel and absorbent entrained in said gas, the oxygen being present in said zone in an amount to provide from about 25%-40% of the total stoichiometric amount required for the complete combustion of the fuel, the inorganic alkaline absorbent being present in an amount to provide a molar ratio of alkaline absorbent to sulfur compounds of from about 1.0:1 to 3.0:1, said ratio including any alkaline absorbents contained in the fuel; reacting said fuel and absorbent entrained in said oxygen-containing gas by maintaining them in said zone at a temperature from about 1000°-1800° K. for a time sufficient (a) to gasify at least about 75% of the carbon content of the fuel and substantially all of the sulfur in a fuel, (b) to combust the gasified fuel and oxygen to produce a fuel-rich stoichiometry in the gas-phase, and (c) to react in excess of about 70% of the fuel sulfur with the inorganic alkaline absorbent to form a solid alkaline sulfide compound introducing the resultant combustion mixture into a second combustion zone; maintaining said mixture at a temperature in the range of 1800° K.-2500° K. in said second combustion zone while introducing additional air in an amount to provide about 45%-75% of the total stoichiometric amount of air required for complete combustion of the fuel; maintaining said mixture including said alkaline sulfide compound, at said temperature for a time sufficient to reduce said nitrogenous compound content to a desired level; and discharging said mixture having a substantially reduced gaseous sulfur compound and nitrogenous compound content.
Claim 2
Independent Claim 321 words
A method for the entrained-flow combustion of a carbon-, nitrogen- and sulfur-containing fuel for substantially reducing emission of gaseous sulfur compounds and nitrogenous compounds formed during the combustion of the fuel with a substoichiometric amount of oxygen-comprising; introducing said fuel, an inorganic alkaline absorbent and an oxygen-containing gas into a first combustion sulfur capture zone of an entrained-flow combustor to form a fluent mixture therein of fuel and absorbent entrained in said gas, the oxygen being present in said zone in an amount to provide from about 25%-40% of the total stoichiometric amount required for the complete combustion of the fuel, the inorganic alkaline absorbent being present in an amount to provide a molar ratio of alkaline absorbent to sulfur compounds of from about 1.0:1 to 3.0:1, said ratio including any alkaline absorbents contained in the fuel; reacting said fuel and absorbent entrained in said oxygen-containing gas by maintaining them in said zone at a temperature from about 1000°-1800° K. for a time sufficient (a) to gasify at least about 75% of the carbon content of the fuel and substantially all of the sulfur in a fuel, (b) to combust the gasified fuel and oxygen to produce a fuel-rich stoichiometry in the gas-phase, and (c) to react in excess of about 70% of the fuel sulfur with the inorganic alkaline absorbent to form a solid alkaline sulfide compound introducing the resultant combustion mixture into a second combustion zone; maintaining said mixture at a temperature in the range of 1800° K.-2500° K. in said second combustion zone while introducing additional air in an amount to provide about 45%-75% of the total stoichiometric amount of air required for complete combustion of the fuel; maintaining said mixture including said alkaline sulfide compound, at said temperature for a time sufficient to reduce said nitrogenous compound content to a desired level; and discharging said mixture having a substantially reduced gaseous sulfur compound and nitrogenous compound content.
Claim 3
Dependent Claim 23 words
The method of claim 1 wherein said solid sulfur compounds are removed from the gas stream between said first and second combustion zones.
Claim 4
Dependent Claim 26 words
The method of claim 1 wherein said alkaline absorbent is selected from the group consisting of the oxides, hydroxides, and carbonates of magnesium, calcium, and sodium.
Claim 5
Dependent Claim 24 words
The method of claim 1 wherein said temperature is maintained in said first and second combustion zones by the introduction thereto of preheated air.
Claim 6
Dependent Claim 69 words
The method of claim 1 further including introducing the combustion products from said second combustion zone into at least a third combustion zone and maintaining said products at a temperature of from about 1600° to 2000° K. while completing the combustion by the introduction of additional air in an amount to provide from about 100% to about 120% of the total stoichiometric requirements for complete combustion of the fuel.

References Cited (Backward Citations)

US4381718A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-06-17 1988-12-17 1989-06-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-06-17 1992-12-17 1993-06-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-06-17 1996-12-17 1997-06-18 $7700.00 Window Closed / Lapsed

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