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US4329222A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for selectively removing basic nitrogen compounds from lube oils using transition metal halides or transition metal tetrafluoroborates

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1980-09-26
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Granted: 1982-05-11
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Expires: 2000-09-26
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Abstract

Abstract A method is disclosed for the selective removal of basic nitrogen compounds (BNC) from natural and synthetic hydrocarbon feedstocks, preferably petroleum feedstocks, most preferably lube and transformer oils, which method comprises mixing the feedstock oil with a nonaqueous solution of anhydrous nonpolymeric Group IVb, Group Vb, Group VIb, Group VIIb, the non-noble (iron group) metals of Group VIII, copper, zinc, cadmium, and mercury halides (except TiCl4 or FeCl3) or tetrafluoroborates, complexed with non-aqueous polar solvents under conditions of agitation and mild heating whereby the basic nitrogen compounds exchange with the polar solvent to complex with the above-recited metal halides and metal tetrafluoroborates. The preferred halide is bromide, and the preferred polar solvent is methanol. The oil is then decanted to separate it from the metal halides: BNC complexes and the decantate washed with a polar solvent, which preferably includes water, and dried. The basic nitrogen compound-metal halide or metal tetrafluoroborate complex dissolves in the polar solvent, and that which is in the oil is removed by the polar solvent wash. The preferred polar solvent for the wash step is water. By the practice of this method, the basic nitrogen compound content of the oil is reduced by at least 90%. The anhydrous nonpolymeric metal halide or metal tetrafluoroborate-nonaqueous polar solvent complex can be used as such, or they can be impregnated onto a support material.

Inventors

  • 👤 Jacob J. Habeeb

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 04:36
CPC Classifications
C; C10; C10G; C10G29/00; C10G29/06; C10G29/12

Claims Analysis

Total Claims: 23
Claim 1
Independent Claim 104 words
A method for selectively removing basic nitrogen compounds (BNC) from natural and synthetic hydrocarbon feedstocks comprising mixing the feedstock under conditions of agitation and mild heating with anhydrous nonpolymeric Group IVB, Group VB, Group VIB, Group VIIB, the non-noble Group VIII, copper, zinc, cadmium and mercury halides, except that the halide may not be chlorine, which metal halides are complexed with nonaqueous polar solvent and wherein the metal halide-nonaqueous polar solvent complex is impregnated onto a support material, whereby the BNC exchange with the complexed nonaqueous polar solvents and themselves become complexed with the metal halides of the supported metal halide-nonaqueous polar solvent complex.
Claim 2
Independent Claim 104 words
A method for selectively removing basic nitrogen compounds (BNC) from natural and synthetic hydrocarbon feedstocks comprising mixing the feedstock under conditions of agitation and mild heating with anhydrous nonpolymeric Group IVB, Group VB, Group VIB, Group VIIB, the non-noble Group VIII, copper, zinc, cadmium and mercury halides, except that the halide may not be chlorine, which metal halides are complexed with nonaqueous polar solvent and wherein the metal halide-nonaqueous polar solvent complex is impregnated onto a support material, whereby the BNC exchange with the complexed nonaqueous polar solvents and themselves become complexed with the metal halides of the supported metal halide-nonaqueous polar solvent complex.
Claim 3
Dependent Claim 56 words
The method of claim 1 further comprising the step of separating the feedstock from which the basic nitrogen compounds have been removed from the supported metal halide nonaqueous polar solvent complex with which the basic nitrogen compounds are now complexed by their exchange with the polar solvent, washing the separated feedstock with polar solvent and drying.
Claim 4
Dependent Claim 15 words
The method of claim 1 or 2 wherein the metal halide is a metal bromide.
Claim 5
Dependent Claim 20 words
The method of claim 1 or 2 wherein the polar solvent which is complexed with the metal halide is methanol.
Claim 6
Dependent Claim 18 words
The method of claim 3 wherein the polar solvent which is complexed with the metal bromide is methanol.
Claim 7
Dependent Claim 30 words
The method of claim 1 or 2 wherein the metal is selected from the group consisting of nickel, chromium, vanadium, zinc, copper, manganese, iron, cobalt, titanium, molybdenum, cadmium and mercury.
Claim 8
Dependent Claim 32 words
The method of claim 3 wherein the metal bromide is selected from the group consisting of chromium tribromide, nickel dibromide, vanadium dibromide, zinc dibromide and the copper, manganese, iron and cobalt bromides.
Claim 9
Dependent Claim 31 words
The method of claim 1 or 2 wherein the nonaqueous polar solvent with which the metal halide is complexed is selected from the group consisting of methanol, ethanol, acetone and acetonitrile.
Claim 10
Dependent Claim 24 words
The method of claim 1 or 2 wherein the mild heating is conducted at a temperature ranging from between about 25° to 120° C.
Claim 11
Dependent Claim 16 words
The method of claim 2 wherein the polar solvent wash employs water as the polar solvent.
Claim 12
Dependent Claim 32 words
The method of claim 1 wherein the supported metal halide nonaqueous polar solvent complex is regenerated after use by washing with nonaqueous polar solvent at temperatures between about 25° to 75° C.
Claim 13
Dependent Claim 32 words
The method of claim 2 wherein the supported metal halide nonaqueous polar solvent complex is regenerated after use by washing with nonaqueous polar solvent at temperatures between about 25° to 75° C.
Claim 14
Independent Claim 74 words
A method for selectively removing basic nitrogen compounds (BNC) from natural and synthetic hydrocarbon feedstocks comprising mixing the feedstock under conditions of agitation and mild heating with anhydrous nonpolymeric Group IVb, Group Vb, Group VIb, Group VIIb, the non-noble Group VIII, copper, zinc, cadmium and mercury tetrafluoroborates which metal tetrafluoroborates are complexed with nonaqueous polar solvents whereby the BNC exchange with the complexed nonaqueous polar solvents and themselves become complexed with the metal tetrafluoroborates.
Claim 15
Independent Claim 74 words
A method for selectively removing basic nitrogen compounds (BNC) from natural and synthetic hydrocarbon feedstocks comprising mixing the feedstock under conditions of agitation and mild heating with anhydrous nonpolymeric Group IVb, Group Vb, Group VIb, Group VIIb, the non-noble Group VIII, copper, zinc, cadmium and mercury tetrafluoroborates which metal tetrafluoroborates are complexed with nonaqueous polar solvents whereby the BNC exchange with the complexed nonaqueous polar solvents and themselves become complexed with the metal tetrafluoroborates.
Claim 16
Dependent Claim 54 words
The method of claim 13 further comprising the step of separating the feedstock from which the basic nitrogen compounds have been removed from the metal tetrafluoroborate-nonaqueous polar solvent complex with which the basic nitrogen compounds are now complexed by their exchange with the polar solvent, washing the separated feedstock with polar solvent and drying.
Claim 17
Dependent Claim 21 words
The method of claim 13 or 14 wherein the nonaqueous polar solvent which is complexed with the metal tetrafluoroborate is methanol.
Claim 18
Dependent Claim 19 words
The method of claim 13 or 14 wherein the metal tetrafluoroborate-nonaqueous polar solvent is impregnated onto a support material.
Claim 19
Dependent Claim 30 words
The method of claim 13 or 14 wherein the metal is selected from the group consisting of nickel, chromium, vanadium, zinc, copper, manganese, iron, cobalt, titanium, molybdenum, cadmium and mercury.
Claim 20
Dependent Claim 31 words
The method of claim 13 or 14 wherein the nonaqueous polar solvent with which the metal tetrafluoroborate is complexed is selected from the group consisting of methanol, ethanol, acetone and acetonitrile.
Claim 21
Dependent Claim 24 words
The method of claim 13 or 14 wherein the mild heating is conducted at a temperature ranging from between about 25° to 120° C.
Claim 22
Dependent Claim 16 words
The method of claim 14 wherein the polar solvent wash employs water as the polar solvent.
Claim 23
Dependent Claim 31 words
The method of claim 16 wherein the supported metal tetrafluoroborate-nonaqueous polar solvent complex is regenerated after use by washing with nonaqueous polar solvent at temperatures between about 25° to 75° C.

References Cited (Backward Citations)

US2796387A Cited
US3055825A Cited
US2970105A Cited
US3193496A Cited
US3326798A Cited
US4071435A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-10 1985-11-09 1986-05-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-10 1989-11-09 1990-05-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-10 1993-11-09 1994-05-11 $7700.00 Window Closed / Lapsed

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