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US4146367A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal desulfurization

Assignee: National Aeronautics and Space Administration
•
Filing: 1978-02-16
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Granted: 1979-03-27
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Expires: 1998-02-16
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Abstract

Abstract Organic sulfur is removed from coal by treatment with an organic solution of iron pentacarbonyl. Organic sulfur compounds can be removed by reaction of the iron pentacarbonyl with coal to generate CO and COS off-gases. The CO gas separated from COS can be passed over hot iron filings to generate iron pentacarbonyl.

Inventors

  • 👤 George C. Hsu

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 22:52
CPC Classifications
C; C10; C10L; C10L9/00; C10L9/02

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 77 words
A method of removing organic bound sulfur from organic carbonaceous material comprising the steps of: suspending the material in an organic solvent containing excess iron pentacarbonyl with respect to bound sulfur; heating the suspension to a temperature of at least 40° C. but below 160° C. for a time sufficient to react with at least 50% of the organic bound sulfur; and recovering a desulfurized material from the suspension containing at least 50% less organic bound sulfur.
Claim 2
Independent Claim 77 words
A method of removing organic bound sulfur from organic carbonaceous material comprising the steps of: suspending the material in an organic solvent containing excess iron pentacarbonyl with respect to bound sulfur; heating the suspension to a temperature of at least 40° C. but below 160° C. for a time sufficient to react with at least 50% of the organic bound sulfur; and recovering a desulfurized material from the suspension containing at least 50% less organic bound sulfur.
Claim 3
Dependent Claim 15 words
A method according to claim 1 in which the material is particulate high sulfur coal.
Claim 4
Dependent Claim 29 words
A method according to claim 2 in which the coal contains at least 1% organic bound sulfur and the coal particles range in size from 60 to 325 mesh.
Claim 5
Dependent Claim 25 words
A method according to claim 2 in which the solvent is an aromatic hydrocarbon having a boiling point from 40° C. to below 150° C.
Claim 6
Dependent Claim 18 words
A method according to claim 4 in which the solvent is selected from benzene, toluene or anthracene oils.
Claim 7
Dependent Claim 39 words
A method according to claim 4 in which the coal is present in the slurry in an amount from 10% to 50% by weight and at least 3% by weight of the iron pentacarbonyl is present in the solution.
Claim 8
Dependent Claim 19 words
A method according to claim 6 in which the iron pentacarbonyl is present from 10% to 50% by weight.
Claim 9
Dependent Claim 16 words
A method according to claim 2 further including the step of recovery and recycling the solvent.
Claim 10
Dependent Claim 31 words
A method according to claim 8 in which the treated suspension is heated to a temperature of at least 160° C. to decompose the iron pentacarbonyl into CO and magnetic iron.
Claim 11
Dependent Claim 22 words
A method according to claim 9 further including the step of passing the CO over hot iron filings to generate iron pentacarbonyl.
Claim 12
Dependent Claim 177 words
A coal desulfurization system including in combination: a reactor having a first coal inlet, a second solvent inlet and a third iron pentacarbonyl inlet for forming a slurry of coal in an organic solvent solution of iron pentacarbonyl, having gas outlet means for venting a mixture of CO and COS gases from the reactor and having a slurry outlet; a distillation column connected to a reboiler for receiving said slurry and heating it to a temperature of at least 160° C. and having a treated slurry outlet, a solvent recycle outlet connected to said second inlet and a CO gas outlet; gas separator means for receiving the flow from both said gas outlets and for forming a COS by-product stream and a CO stream outlet; iron pentacarbonyl generation means containing a bed of iron filings and including means for heating said bed, said generation means having a gas inlet connected to the CO stream outlet for generating iron pentacarbonyl and having an iron pentacarbonyl outlet; and conduit means connecting the generation means outlet to the third inlet.
Claim 13
Dependent Claim 177 words
A coal desulfurization system including in combination: a reactor having a first coal inlet, a second solvent inlet and a third iron pentacarbonyl inlet for forming a slurry of coal in an organic solvent solution of iron pentacarbonyl, having gas outlet means for venting a mixture of CO and COS gases from the reactor and having a slurry outlet; a distillation column connected to a reboiler for receiving said slurry and heating it to a temperature of at least 160° C. and having a treated slurry outlet, a solvent recycle outlet connected to said second inlet and a CO gas outlet; gas separator means for receiving the flow from both said gas outlets and for forming a COS by-product stream and a CO stream outlet; iron pentacarbonyl generation means containing a bed of iron filings and including means for heating said bed, said generation means having a gas inlet connected to the CO stream outlet for generating iron pentacarbonyl and having an iron pentacarbonyl outlet; and conduit means connecting the generation means outlet to the third inlet.

References Cited (Backward Citations)

US3938966A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-03-26 1982-09-25 1983-03-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-03-26 1986-09-25 1987-03-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-03-26 1990-09-25 1991-03-27 $7700.00 Window Closed / Lapsed

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