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.