Incorporation of a coprocessing additive into coal/oil agglomerates

• US 5,190,566 A
• Filed: 01/08/1992
• Issued: 03/02/1993
• Est. Priority Date: 01/08/1992
• Status: Expired due to Term

• Current Assignee: Her Majesty The Queen In Right of Canada As Represented By The Minister of National Defence
• Original Assignee: Energy Mines and Resources Canada
• Inventors: Ikura, Michio, Sparks, Bryan D., Coleman, Richard D., Toll, Floyd N., Meadus, F. Weldon
• Primary Examiner(s): MCAVOY, ELLEN M
• Application Number:
  US07/818,100
• Time in Patent Office: 419 Days
• Field of Search: 44/627, 44/621
• US Class Current: 44/627
• CPC Class Codes: C10G 1/00 Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal mechanical winning of oil from oil-shales, oil-sand, or the like B03B

Abstract

In the present invention, iron sulfate is added in the form of an aqueous wash solution to coal agglomerates after separation of ash from the agglomerated coal. As the agglomerates remain in a continuous water phase, a good dispersion of the iron sulfate solution throughout the agglomerate matrix occurs. At this stage an unexpectedly strong adsorption of Fe ions onto the coal surfaces occurs without any adverse effects on agglomerate integrity and the ability to separate it selectively by floatation. Furthermore, this good dispersion also results in over 94% of the iron sulfate in the wash solution being transferred to the agglomerates. This manner of addition of iron sulphate to coal has been shown to elevate advantageously the lowest temperature at which coke formation occurs during coprocessing.

Claims

1. A method of incorporating a coprocessing additive in coal/oil agglomerates, comprising:

a) forming an aqueous slurry of particulate sub-bituminous coal, the particulate coal comprising carbonaceous particles and particulate inorganic material,

b) agitating the slurry while admixing agglomerating oil therewith, to form carbonaceous particle/oil agglomerates with particulate inorganic material, and water, separated therefrom,

c) separating, in an undried condition, the carbonaceous particle/oil agglomerates from the particulate inorganic material and water, and

d) intimately contacting the separated, undried, agglomerates with an aqueous solution of coprocessing additive comprising at least one water soluble salt of a metal from Groups 5 to 12 of the Periodic Table of Elements (International Union of Pure and Applied Chemistry,

     1983) for specific adsorption of additive in molecularly disseminated form by the separated, undried agglomerates.

2. A method according to claim 1, wherein the coprocessing additive is at least one soluble salt of at least one substance selected from the group consisting of cobalt, molybdenum, iron, tin, nickel and mixtures thereof.

3. A process according to claim 1, wherein the undried carbonaceous particle/oil agglomerates are separated from the particulate inorganic material and water by flotation/separation.

4. A process according to claim 1, wherein the separated, undried agglomerates are contacted with the aqueous solution of the coprocessing additive by being washed with a wash thereof.

5. A process according to claim 4, wherein the undried agglomerates with adsorbed coprocessing additive are centrifugally separated from the remainder of the wash, and any remaining coprocessing additive separated from the agglomerates is recirculated to the wash stream.

6. A method according to claim 2 wherein the salt is a sulphate.

7. A method according to claim 6 wherein the salt is iron sulphate.