# US 4,392,892 A · Process for separating hydrocarbons from particulate solids > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,392,892 A - Document ID: US4392892A - Status: Granted - Kind: A - Application number: 06/307,092 - Filed: 1981-09-18 - Granted: 1983-07-12 - Earliest claimed: 1978-10-06 - Assignees: Wintershall Aktiengesellschaft; Gesellschaft fur Biotechnologische Forschung - Inventors: Fritz Wagner; Walter Lindorfer; Wilhelm Jahn-Held; Walther Schulz - Web page: https://patentgrep.com/patent/US4392892A ## CPC - B01D 12/00: Displacing liquid, e.g. from wet solids or from dispersions of liquids or from solids in liquids, by means of another liquid - C09K 3/32: for absorbing liquids to remove pollution, e.g. oil, gasoline, fat - C10C 3/007: {winning and separation of asphalt from mixtures with aggregates, fillers and other products, e.g. winning from natural asphalt and regeneration of waste asphalt} - 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) - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - C09K: MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE - C10C: WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID (compositions of bituminous materials C08L95/00; carbon filaments by decomposition of organic filaments D01F9/14) - 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 ## Abstract Oils or petroleum hydrocarbons are separated from solid or solid/liquid mixtures thereof with soil, sand or oil processing residues, by treating these oil-containing mixtures with an aqueous solution or dispersion of a crude extract of microbially produced glycolipids and separating the oil-containing phase from the aqueous phase. ## Claims ### Claim 1 A process for separating oils or petroleum hydrocarbons from solid or solid/liquid mixtures thereof with particles of soil, sand or petroleum processing residues, which comprises the steps of (a) mixing said oil-containing mixture with an aqueous solution or dispersion of a crude extract of microbially produced glycolipids to form a slurry, said extract being obtained by a method consisting essentially of the steps of extracting a microbial culture solution with a solvent for glycolipids and evaporating the solvent from the extract; and (b) adding water, an aqueous salt solution or sea water to the slurry in an amount sufficient to cause a rapid rising of an oil phase from an aqueous phase; and (c) separating the oil phase from the aqueous phase, whereby said particles are rendered substantially oil-free. ### Claim 2 (depends on 1) The process according to claim 1, wherein said glycolipids are produced by microorganisms from a mixture of alkanes with 12 to 19 carbon atoms in the molecule or from crude oil. ### Claim 3 (depends on 1) The process according to claim 1, wherein said glycolipids are mono- and diesters of .alpha.,.alpha.'-trehalose and long-chained .alpha.-alkyl-.beta.-hydroxy fatty acids. ### Claim 4 (depends on 1) The process according to claim 1, wherein said glycolipids are produced by the microorganisms Nocardia rhodochrous species or Mycobacterium phlei from a mixture of alkanes with 12 to 19 carbon atoms in the molecule or from crude oil. ### Claim 5 (depends on 1) The process according to claim 1, wherein said glycolipids are used in the form of an aqueous solution or dispersion containing said glycolipids, in a concentration of from 0.01 to 5.0 g/l. ### Claim 6 (depends on 5) The process according to claim 5, wherein the solution or dispersion of glycolipids is sprayed onto the oil-containing mixtures. ### Claim 7 (depends on 5) The process according to claim 5, wherein the solution or dispersion of glycolipids is introduced into the oil-containing mixtures from below or laterally. ### Claim 8 (depends on 1) The process according to claim 1, wherein sea water or water enriched with rock salt is added to the oil-containing mixture in order to increase the difference between the specific gravities of the aqueous phase and the oil phase. ### Claim 9 (depends on 7) The process according to claim 7, wherein the separation of the oily phase is effected by flotation separation, by adding a sufficient quantity of water to the oily mixture to bring about the attachment of the oil droplets to air bubbles, by blowing air in, and thus causing fairly rapid ascension of the oil phase. ### Claim 10 (depends on 7) The process according to claim 7, wherein the introduction of the oil-containing soil and/or sand or residues is effected with a mixture of water and a dispersion of the crude extract of glycolipids or these components are simultaneously or separately added in sufficient quantities to ensure that the oil phase leaving the cavities and capillaries of the soil, sand or residues rises up out of the aqueous phase, the ratio of glycolipids to oil being designed to ensure practically total separation of the oil phase. ### Claim 11 (depends on 1) The process according to claim 1, wherein oil splitting agents are added to the oil phase.