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US4405448A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing halogenated aliphatic and aromatic compounds from petroleum products

Assignee: United States Department of Energy
•
Filing: 1982-03-31
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Granted: 1983-09-20
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Expires: 2002-03-31
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Abstract

Abstract A process for removing halogenated aliphatic and aromatic compounds, e.g., polychlorinated biphenyls, from petroleum products by solvent extraction. The halogenated aliphatic and aromatic compounds are extracted from a petroleum product into a polar solvent by contacting the petroleum product with the polar solvent. The polar solvent is characterized by a high solubility for the extracted halogenated aliphatic and aromatic compounds, a low solubility for the petroleum product and considerable solvent power for polyhydroxy compound. The preferred polar solvent is dimethylformamide. A miscible compound, such as, water or a polyhydroxy compound, is added to the polar extraction solvent to increase the polarity of the polar extraction solvent. The halogenated aliphatic and aromatic compounds are extracted from the highly-polarized mixture of water or polyhydroxy compound and polar extraction solvent into a low polar or nonpolar solvent by contacting the water or polyhydroxy compound-polar solvent mixture with the low polar or nonpolar solvent. The halogenated aliphatic and aromatic compounds and the low polar or nonpolar solvent are separated by physical means, e.g., vacuum evaporation. The polar and nonpolar solvents are recovered from recycling. The process can easily be designed for continuous operation. Advantages of the process include that the polar solvent and a major portion of the nonpolar solvent can be recycled, the petroleum products are reclaimable and the cost for disposing of waste containing polychlorinated biphenyls is significantly reduced.

Inventors

  • 👤 John M. Googin
  • 👤 John M. Napier
  • 👤 Michael A. Travaglini

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 20:45
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/06; C10G21/12; C10G21/20; C10G21/006; C10G21/18; C10G21/28; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/908; Y10S210/909

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 111 words
A process for removing polychlorinated biphenyls from petroleum products by solvent extraction, comprising the steps of: contacting a petroleum product containing a polychlorinated biphenyl with an adequate volume of a polar solvent selected from the group consisting of dimethyl formamide and furfural for extracting essentially all of the polychlorinated biphenyl frm the petroleum product; separating the resulting extract phase of the polar solvent and extracted polychlorinated biphenyl from the raffinate phase; contacting the extract with an adequate volume of water or a polyhydroxy compound to extract the polychlorinated biphenyl from the polar solvent; and recoverng polar solvent and water or polyhydroxy compound with essentially all of the polychlorinated biphenyl removed therefrom.
Claim 2
Dependent Claim 111 words
A process for removing polychlorinated biphenyls from petroleum products by solvent extraction, comprising the steps of: contacting a petroleum product containing a polychlorinated biphenyl with an adequate volume of a polar solvent selected from the group consisting of dimethyl formamide and furfural for extracting essentially all of the polychlorinated biphenyl frm the petroleum product; separating the resulting extract phase of the polar solvent and extracted polychlorinated biphenyl from the raffinate phase; contacting the extract with an adequate volume of water or a polyhydroxy compound to extract the polychlorinated biphenyl from the polar solvent; and recoverng polar solvent and water or polyhydroxy compound with essentially all of the polychlorinated biphenyl removed therefrom.
Claim 3
Dependent Claim 105 words
The process as claimed in claim 1 wherein the step of recovering the polar solvent and the water or polyhydroxy compound comprises stripping the polychlorinated biphenyl from the resulting mixture of polychlorinated biphenyl, polar solvent and water or polyhydroxy compound by contacting the mixture with a nonpolar solvent having a relatively low vapor pressure and a volume adequate to effect said stripping, separating the resulting polar solvent and water or polyhydroxy compound phase from the phase formed of the nonpolar solvent containing polychlorinated biphenyl, and thereafter concentrating the polychlorinated biphenyl by depleting the nonpolar solvent from the phase of the nonpolar solvent containing polychlorinated biphenyl.
Claim 4
Dependent Claim 44 words
A process as claimed in claim 1 including the additional steps of separating water or the polyhydroxy compound from the recovered polar solvent and water or polyhydroxy compound phase, and thereafter recycling the polar solvent into contact with the petroleum product containing polychlorinated biphenyl.
Claim 5
Dependent Claim 73 words
A process as claimed in claim 1 wherein a minor portion of the petroleum products is dissolved in the polar solvent, wherein water is used to extract the polychlorinated biphenyl from the polar solvent, and wherein the petroleum products dissolved in the polar solvent are released during the contact with the water to form two liquid phases defined by the released petroleum products containing extracted polychlorinated biphenyl and the polar solvent and water.
Claim 6
Dependent Claim 16 words
A process as claimed in claim 1 wherein the polyhdyroxy compound is glycerol or a glycol.
Claim 7
Dependent Claim 14 words
A process a claimed in claim 1 wherein the petroleum product is transformer oil.
Claim 8
Dependent Claim 17 words
A process as claimed in claim 2 wherein the nonpolar solvent is an n-pentane to n-octane fraction.
Claim 9
Dependent Claim 24 words
A process as claimed in claim 7 wherein the step of concentrating the polychlorinated biphenyl by depleting the nonpolar solvent is achieved by evaporation.

References Cited (Backward Citations)

US1103499A Cited
US1584588A Cited
US2484469A Cited
US3249532A Cited
US3400171A Cited
US4154670A Cited
US4105542A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-09-19 1987-03-21 1987-09-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-09-19 1991-03-21 1991-09-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-09-19 1995-03-21 1995-09-20 $7700.00 Window Closed / Lapsed

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