GB826144A - Process for removing oil from oil-in-water emulsions - Google Patents

Process for removing oil from oil-in-water emulsions

Info

Publication number
GB826144A
GB826144A GB706156A GB706156A GB826144A GB 826144 A GB826144 A GB 826144A GB 706156 A GB706156 A GB 706156A GB 706156 A GB706156 A GB 706156A GB 826144 A GB826144 A GB 826144A
Authority
GB
United Kingdom
Prior art keywords
resin
oil
regenerated
passed
sodium chloride
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB706156A
Inventor
Adolf Richter
Friedrich Wolf
Manfred Morgner
Gunter Moebius
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Filmfabrik Wolfen VEB
Original Assignee
Filmfabrik Wolfen VEB
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Filmfabrik Wolfen VEB filed Critical Filmfabrik Wolfen VEB
Priority to GB706156A priority Critical patent/GB826144A/en
Publication of GB826144A publication Critical patent/GB826144A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G33/00Dewatering or demulsification of hydrocarbon oils
    • C10G33/04Dewatering or demulsification of hydrocarbon oils with chemical means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G25/00Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/02Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

To recover oil from an oil-in-water emulsion which may contain an emulsifier, stabilizer, salts or the like, the emulsion is passed through an adsorbent artificial resin capable of anion exchange and the exhausted resin is regenerated in a manner appropriate to it. In one example an anion-exchange resin based on a polyalkylene-imine resin is converted into salt form and there is passed through it an emulsion containing crude oil, an anion-active wetting agent and sodium chloride, and having a pH value of from 10 to 11. The treated liquid has a pH below 3. The oil is removed from the resin by carbon tetrachloride, and the resin is regenerated by a mixture of sodium chloride and hydrochloric acid. The solvent layer of the regenerant effluent is separated, and after being re-used several times, the solvent and crude oil are recovered by distillation. In a second example a tanker rinsing water containing crude mineral oil (containing naphthenic acids), an anion-active wetting agent and sodium chloride, and having a pH value of 9.5 is passed through a wide-latticed condensation resin based on an aromatic amine, e.g. metaphenylene diamine, and formaldehyde, and previously converted to the chlorineladen condition. After use the resin is washed, and then regenerated with caustic soda and hydrochloric acid with a short intermediate washing. The rinsing water and regenerant washings are combined, and removed from the oil, which precipitates rapidly. In a third example, an oil-in-water emulsion containing mineral oil, an alcohol sulphonate as an emulsifier, and dissolved salt, is passed through a copolymer of 2-vinyl-pyridine which is crosslinked with para-divinyl-benzene and quaternated at the pyridine nitrogen atom. The resin is regenerated with hydrochloric acid and caustic soda solution saturated with sodium chloride, and after brief washing the resin is washed with petroleum ether from which latter the oil is recovered by distillation.ALSO:To remove oil from an oil-in-water emulsion which may contain an emulsifier, stabiliser, salts or the like, the emulsion is passed through an adsorbent artificial resin capable of anion exchange and the exhausted resin is regenerated in a manner appropriate to it. In one example an anion-exchange resin based on a polyalkylene imine resin is converted into salt form and there is passed through it an emulsion containing crude oil, an anion-active wetting agent and sodium chloride, and having a pH value of from 10 to 11. The treated liquid has a pH below 3. The oil is removed from the resin by carbon tetrachloride, and the resin is regenerated by a mixture of sodium chloride and hydrochloric acid. The solvent layer of the regenerant effluent is separated, and after being re-used several times, the solvent and crude oil are recovered by distillation. In a second example, a tanker rinsing water containing crude mineral oil (containing naphthenic acids), an anion-active wetting agent and sodium chloride, and having a pH value of 9,5 is passed through a wide-latticed condensation resin based on an aromatic amine, e.g. metaphenylene diamine, and formaldehyde, and previously converted to the chloride-laden condition. After use the resin is washed, and then regenerated with caustic soda solution and hydrochloric acid with a short intermediate washing. The rinsing water and regenerant washings are combined, and removed from the oil which precipitates rapidly. In a third example an oil-in-water emulsion containing mineral oil, an alcohol sulphonate as an emulsifier and dissolved salt is passed through a copolymer of 2-vinyl-pyridine which is cross-linked with paradivinyl-benzene and quaternated at the pyridine nitrogen atom. The resin is regenerated with hydrochloric acid and caustic soda solution saturated with sodium chloride, and after brief washing the resin is washed with petroleum ether (boiling at 40-60 DEG C.), residual amounts of the latter, remaining in the resin, being removed by methanol. The dissolved oil is recovered by distilling the petroleum ether.
GB706156A 1956-03-06 1956-03-06 Process for removing oil from oil-in-water emulsions Expired GB826144A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB706156A GB826144A (en) 1956-03-06 1956-03-06 Process for removing oil from oil-in-water emulsions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB706156A GB826144A (en) 1956-03-06 1956-03-06 Process for removing oil from oil-in-water emulsions

Publications (1)

Publication Number Publication Date
GB826144A true GB826144A (en) 1959-12-31

Family

ID=9825865

Family Applications (1)

Application Number Title Priority Date Filing Date
GB706156A Expired GB826144A (en) 1956-03-06 1956-03-06 Process for removing oil from oil-in-water emulsions

Country Status (1)

Country Link
GB (1) GB826144A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0535910A2 (en) * 1991-10-02 1993-04-07 Exxon Research And Engineering Company Method for improving the demulsibility of base oils
US5466364A (en) * 1993-07-02 1995-11-14 Exxon Research & Engineering Co. Performance of contaminated wax isomerate oil and hydrocarbon synthesis liquid products by silica adsorption
US6416670B1 (en) 1999-03-12 2002-07-09 Mpr Services, Inc. Regenerable hydrocarbon filter
WO2016149506A1 (en) * 2015-03-17 2016-09-22 Donaldson Company, Inc. Hydrocarbon-in-water purification anion-exchange system
US20180079972A1 (en) * 2015-03-17 2018-03-22 Donaldson Company, Inc. Hydrocarbon-in-water purification system
CN112694911A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for treating crude oil containing petroleum sulfonate

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0535910A2 (en) * 1991-10-02 1993-04-07 Exxon Research And Engineering Company Method for improving the demulsibility of base oils
EP0535910A3 (en) * 1991-10-02 1993-05-19 Exxon Research And Engineering Company Method for improving the demulsibility of base oils
US5282960A (en) * 1991-10-02 1994-02-01 Exxon Research And Engineering Company Method for improving the demulsibility of base oils
US5466364A (en) * 1993-07-02 1995-11-14 Exxon Research & Engineering Co. Performance of contaminated wax isomerate oil and hydrocarbon synthesis liquid products by silica adsorption
US6416670B1 (en) 1999-03-12 2002-07-09 Mpr Services, Inc. Regenerable hydrocarbon filter
WO2016149506A1 (en) * 2015-03-17 2016-09-22 Donaldson Company, Inc. Hydrocarbon-in-water purification anion-exchange system
US20180079972A1 (en) * 2015-03-17 2018-03-22 Donaldson Company, Inc. Hydrocarbon-in-water purification system
US20180079971A1 (en) * 2015-03-17 2018-03-22 Donaldson Company, Inc. Hydrocarbon-in-water purification anion-exchange system
US10526548B2 (en) * 2015-03-17 2020-01-07 Donaldson Company, Inc. Hydrocarbon-in-water purification system
US10604707B2 (en) * 2015-03-17 2020-03-31 Donaldson Company, Inc. Hydrocarbon-in-water purification anion-exchange system
US11220636B2 (en) 2015-03-17 2022-01-11 Donaldson Company, Inc. Hydrocarbon-in-water purification system
CN112694911A (en) * 2019-10-23 2021-04-23 中国石油化工股份有限公司 Method for treating crude oil containing petroleum sulfonate

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