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US4387653A Expired / Lapsed US ⏱️ 0.0 years remaining

Limestone-based sorbent agglomerates for removal of sulfur compounds in hot gases and method of making

Assignee: BASF Catalysts LLC
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Filing: 1981-10-05
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Granted: 1983-06-14
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Expires: 2001-10-05
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Abstract

Abstract Sulfur-containing compounds such as hydrogen sulfide and sulfur oxides arising from gasification or combustion of organic fuels such as coal may be removed from the hot gases by attrition resistant, highly reactive limestone-based sorbent agglomerates. The agglomerates are formed by crushing and powdering naturally occurring limestone into grains of fine particle size and binding the powdered limestone grains with a binder that is stable at high temperature, for example a colloidal grade of attapulgite clay. Volatile liquid is added to the mix of binder and powdered limestone to form a paste-like mixture, which is then agglomerated in compression-type agglomerating equipment to form spheroidal agglomerates having good green strength. In fluidized bed combustion applications, these agglomerates have attrition resistance equivalent to conventional natural limestone granules and are far more reactive in terms of sulfur pickup.

Inventors

  • 👤 Kenneth E. Voss

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 06:12
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/002; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/52; B01D53/523; B01J; B01J20/00; B01J20/02; B01J20/04; B01J20/043; B01J20/28; B01J20/28014; B01J20/2803; B01J20/30; B01J20/3021; B01J20/3028; B01J20/3042; B01J20/34; B01J20/3433; B01J20/345; B01J20/3458

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 97 words
In a process for fluidized bed combustion of sulfur containing fuel such as coal or heavy oil, wherein said fuel generates sulfur oxides in the flue gas stream upon combustion, and limestone is added to said bed to react with said sulfur oxides to remove them from the flue gas stream, the improvement which comprises enhancing the removal of sulfur oxides by utilizing said limestone in the form of agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof in binder-effective amount.
Claim 2
Dependent Claim 97 words
In a process for fluidized bed combustion of sulfur containing fuel such as coal or heavy oil, wherein said fuel generates sulfur oxides in the flue gas stream upon combustion, and limestone is added to said bed to react with said sulfur oxides to remove them from the flue gas stream, the improvement which comprises enhancing the removal of sulfur oxides by utilizing said limestone in the form of agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof in binder-effective amount.
Claim 3
Dependent Claim 95 words
In a process for fixed bed combustion of sulfur containing solid fuel such as coal, wherein said fuel generates sulfur oxides in the flue gas stream upon combustion, and limestone mingled with the coal in said bed to react with said sulfur oxides to remove them from the flue gas stream, the improvement which comprises enhancing the removal of sulfur oxides by utilizing said limestone in the form of agglomerates comprising finely powdered, naturally occurring, uncalcined limestone and cementitious clay selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof in binder-effective amount.
Claim 4
Dependent Claim 95 words
In a process for fixed bed combustion of sulfur containing solid fuel such as coal, wherein said fuel generates sulfur oxides in the flue gas stream upon combustion, and limestone mingled with the coal in said bed to react with said sulfur oxides to remove them from the flue gas stream, the improvement which comprises enhancing the removal of sulfur oxides by utilizing said limestone in the form of agglomerates comprising finely powdered, naturally occurring, uncalcined limestone and cementitious clay selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof in binder-effective amount.
Claim 5
Dependent Claim 11 words
The process of claim 2 wherein said solid fuel is coal.
Claim 6
Dependent Claim 42 words
In a process for removing hydrogen sulfide from gases, the improvement which comprises utilizing agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay, selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof, in binder-effective amount.
Claim 7
Dependent Claim 42 words
In a process for removing hydrogen sulfide from gases, the improvement which comprises utilizing agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay, selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof, in binder-effective amount.
Claim 8
Dependent Claim 42 words
In a process for removing sulfur oxides from gases, the improvement which comprises utilizing agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay, selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof, in binder-effective amount.
Claim 9
Dependent Claim 42 words
In a process for removing sulfur oxides from gases, the improvement which comprises utilizing agglomerates comprising fine grains of naturally occurring, uncalcined limestone and a cementitious clay, selected from the group consisting of attapulgite, sepiolite, smectite and mixtures thereof, in binder-effective amount.
Claim 10
Dependent Claim 35 words
The process of claims 1, 2, 4, or 5 wherein at least a portion of said agglomerates are recovered, regenerated and recycled to further charge of fuel after initial use for removal of sulfur compounds.

References Cited (Backward Citations)

US4115518A Cited
US3976747A Cited
US4108969A Cited
US4177158A Cited
US4262610A Cited
US4312280A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-06-13 1986-12-13 1987-06-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-06-13 1990-12-13 1991-06-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-06-13 1994-12-13 1995-06-14 $7700.00 Window Closed / Lapsed

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