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US4076505A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal desulfurization process

Assignee: Mobil Oil AS
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Filing: 1976-11-22
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Granted: 1978-02-28
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Expires: 1996-11-22
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Abstract

Abstract This invention provides an improved process for reducing the pyritic sulfur content of coal, which process involves (1) contacting finely divided coal under sink-float separation conditions with a heavy organic parting medium which contains dissolved therein a dispersant quantity of a novel type of soluble sulfanilate ionic surfactant; and (2) separating a coal float phase from the liquid medium system, and recovering coal which has a lower sulfur and ash content than the untreated raw coal.

Inventors

  • 👤 Ralph M. Dessau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 10:24
CPC Classifications
B; B03; B03B; B03B9/00; B03B9/005; B03B5/00; B03B5/28

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 84 words
In a process for reducing the pyritic sulfur and ash content of coal under sink-float separation conditions, the improvement which comprises ( 1) contacting finely comminuted coal with a heavy organic liquid medium having a specific gravity of at least 1.1, and having dissolved therein a dispersant quantity of ionic surfactant which is a hydrocarbyl-succinimide derivative of an aminoarylsulfonic acid salt; and (2) separating the coal float phase from the heavy organic liquid medium, and recovering coal with a reduced sulfur and ash content.
Claim 2
Dependent Claim 84 words
In a process for reducing the pyritic sulfur and ash content of coal under sink-float separation conditions, the improvement which comprises ( 1) contacting finely comminuted coal with a heavy organic liquid medium having a specific gravity of at least 1.1, and having dissolved therein a dispersant quantity of ionic surfactant which is a hydrocarbyl-succinimide derivative of an aminoarylsulfonic acid salt; and (2) separating the coal float phase from the heavy organic liquid medium, and recovering coal with a reduced sulfur and ash content.
Claim 3
Dependent Claim 24 words
A process in accordance with claim 1 wherein the finely comminuted coal has an average particle size in the range of about 10-200 mesh.
Claim 4
Dependent Claim 16 words
A process in accordance with claim 1 wherein the heavy organic liquid is a halogenated hydrocarbon.
Claim 5
Dependent Claim 38 words
A process in accordance with claim 1 wherein the quantity of ionic surfactant dissolved in the heavy organic liquid medium is in the range between about 0.01 and 5 weight percent, based on the weight of liquid medium.
Claim 6
Dependent Claim 57 words
A process in accordance with claim 1 wherein the ionic surfactant is a salt containing the following structural elements: ##STR5## wherein R is an acyclic hyrocarbyl group containing between about 5 and 1000 carbon atoms; Ar is a polyvalent aromatic radical; X is a metal or HNR' 3 cation; and R' is hyrogen or a hydrocarbyl substituent.
Claim 7
Dependent Claim 28 words
A process in accordance with claim 5 wherein the hydrocarbyl-succinimido group of the ion surfactant is at least partially in a hydrolyzed form as an acyclic amido/carboxylate structure.

References Cited (Backward Citations)

US3252769A Cited
US2346151A Cited
US2448605A Cited
US3988120A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-02-27 1981-08-29 1982-02-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-02-27 1985-08-29 1986-02-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-02-27 1989-08-29 1990-02-28 $7700.00 Window Closed / Lapsed

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