# US 4,392,940 A · Coal-oil slurry preparation > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,392,940 A - Document ID: US4392940A - Status: Granted - Kind: A - Application number: 06/252,690 - Filed: 1981-04-09 - Granted: 1983-07-12 - Earliest claimed: 1981-04-09 - Assignees: International Coal Refining Company - Inventors: John C. Tao - Web page: https://patentgrep.com/patent/US4392940A ## CPC - C10G 1/065: {in the presence of a solvent} - C10L 1/322: {Coal-oil suspensions} - C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES - C10L: FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS ## Abstract A pumpable slurry of pulverized coal in a coal-derived hydrocarbon oil carrier which slurry is useful as a low-ash, low-sulfur clean fuel, is produced from a high sulfur-containing coal. The initial pulverized coal is separated by gravity differentiation into (1) a high density refuse fraction containing the major portion of non-coal mineral products and sulfur, (2) a lowest density fraction of low sulfur content and (3) a middlings fraction of intermediate sulfur and ash content. The refuse fraction (1) is gasified by partial combustion producing a crude gas product from which a hydrogen stream is separated for use in hydrogenative liquefaction of the middlings fraction (3). The lowest density fraction (2) is mixed with the liquefied coal product to provide the desired fuel slurry. Preferably there is also separately recovered from the coal liquefaction LPG and pipeline gas. ## Claims ### Claim 1 A process for producing a pumpable coal/oil slurry product, useful as a liquid fuel, from pulverized sulfur-containing coal which comprises the steps of: (1) subjecting said pulverized coal to gravity separation to provide (a) a highest density refuse portion comprising the major portion of the ash and sulfur content of the coal feed, (b) a middlings coal portion of lower ash and sulfur content than said high density portion, and (c) a deep-cleaned lowest density coal portion having a sulfur content of less than about 1%; (2) subjecting said highest density refuse portion to gasification by partial combustion in oxygen (a) thereby obtaining a crude gas product comprising hydrogen, oxides of carban, hydrogen sulfide and steam, thereafter (b) subjecting said crude gas product to a water gas shift reaction in the presence of steam and over sulfur-resistant catalyst, to convert contained carbon monoxide to carbon dioxide with accompanying further production of hydrogen, and (c) removing said carbon dioxide and hydrogen sulfide from the products of said shift reaction to recover a purified hydrogen-rich gas; (3) introducing said middlings coal portion into a liquefaction zone and treating the same with a coal derived solvent and with said purified hydrogen-rich gas under conditions of elevated temperature and pressure, thereby effecting liquefaction of said middlings coal portion to produce a coal derived, benzene soluble hydrocarbon oil distillate; (4) slurrying said deep-cleaned coal portion of lowest density from step (1) with said coal derived hydrocarbon oil of step (3) to provide said coal/oil slurry product. ### Claim 2 (depends on 1) The process as defined in claim 1 wherein said pulverized coal subjected to gravity separation in step (1) has a particle size of up to about 2 millimeters. ### Claim 3 (depends on 1) The process as defined in claim 1 wherein said pulverized coal subjected to gravity separation in step (1) has a sulfur content in excess of 2.5% by weight. ### Claim 4 (depends on 1) The process as defined in claim 1 wherein said gravity separation is effected in an aqueous medium comprising a suspension of magnetite. ### Claim 5 (depends on 4) The process as defined in claim 4 wherein said highest density portion has an ash content in excess of 60% by weight and a sulfur content in excess of 6% by weight. ### Claim 6 (depends on 1) The process as defined in claim 1 wherein said lowest density coal portion is further pulverized to a size range to pass through a 200 mesh screen, prior to admixture with said coal derived hydrocarbon oil. ### Claim 7 (depends on 1) The process as defined in claim 1 wherein said coal/oil slurry product formed in step (4) further contains unconverted solid coal recovered as residual bottoms in said liquefaction of step (3). ### Claim 8 (depends on 1) The process as defined in claim 1 wherein solvent containing unliquefied coal is separated from said liquefaction in step (3) and at least a portion thereof is subjected to said gasification reaction carried out in step (2). ### Claim 9 (depends on 1) The process as defined in claim 1 wherein solvent containing unliquefied coal is separated from said liquefaction in step (3) and at least a portion thereof is admixed in said coal/oil slurry product. ### Claim 10 (depends on 1) The process as defined in claim 1 wherein the liquefaction product obtained in said liquefaction of step (3) also includes a gas mixture which is separated from said coal derived hydrocarbon oil. ### Claim 11 (depends on 10) The process as defined in claim 10 wherein said gas mixture is separated to provide a liquefied petroleum gas fraction and a pipeline gas fraction. ### Claim 12 (depends on 10) The process as defined in claim 10 wherein hydrogen-rich gas is separated from said gas mixture and recycled to said coal liquefaction step (3).