Process for removal of alkyl lead impurities from liquid hydrocarbons

Claim 2

A process for effecting the removal of alkyl lead contaminant from liquid hydrocarbon medlia containing said contaminant which comprises contact of said hydrocarbon media at a temperature below the boiling point thereof with a solid sorbent, said sorbent comprising fresh, spent or regenerated bead Thermofor cracking catalyst, having an amount of anhydrous HCl gas adsorbed therein sufficient to effect substantial reduction in the concentration of said contaminant and maintaining said contact until substantially all of said contaminant is removed therefrom.

Claim 3

The process of claim 1 where the initial amount of HCl adsorbed is from about 0.001 wt. % to about 20 wt. % based on the total weight of the sorbent.

Claim 4

The process of claim 2 where the sorbent has an average pore diameter of from about 3 to about 200 Å and an average surface area of from about 5 to about 1000 m 2 /g.

Claim 5

The process of claim 1 where said sorbent is selected from the group consisting of various forms of silica, bauxite, mordenite, faujasite, natural and synthetic clays, amorphous and crystalline aluminosilicates, alumina, and silica-alumina mixtures.

Claim 6

The process of claim 1 where said contaminant is tetra-alkyl-lead.

Claim 7

The process of claim 1 where said hydrocarbon media is a reformer feedstock comprised substantially of naphtha.

Claim 8

The process of claim 1 where said hydrocarbon media is a motor fuel.

Claim 9

The process of claim 7 where said motor fuel is an unleaded gasoline.

Claim 10

The process of claim 1 wherein after processing less than 5 parts per billion of said alkyl lead contaminant remain in said hydrocarbon media.

Claim 11

A process for effecting the removal of alkyl lead contaminant from liquid hydrocarbon media containing said contaminant which comprises contacting said liquid hydrocarbon media at a temperature of from about 25°-60° C. and a LHSV of from about 5-20 with a solid sorbent, said sorbent comprising fresh spent or regenerated bead Thermofor cracking catalyst selected from the group consisting of various forms of silica, bauxite, mordenite, natural and synthetic clays, amorphous and crystalline aluminosilicates, alumina and silica-alumina mixtures having a pore diameter of from about 3-200 Å and a surface area of from about 5-1000 m 2 /g having adsorbed therein from about 0.0001-20 wt. % of anhydrous hydrogen chloride until substantially all of said contaminant is removed therefrom.

Claim 12

A process for effecting the removal of alkyl lead contaminant from liquid hydrocarbon media containing said contaminant which comprises contacting said liquid hydrocarbon media at a temperature of from about 25°-60° C. and a LHSV of from about 5-20 with a solid sorbent, said sorbent comprising fresh spent or regenerated bead Thermofor cracking catalyst selected from the group consisting of various forms of silica, bauxite, mordenite, natural and synthetic clays, amorphous and crystalline aluminosilicates, alumina and silica-alumina mixtures having a pore diameter of from about 3-200 Å and a surface area of from about 5-1000 m 2 /g having adsorbed therein from about 0.0001-20 wt. % of anhydrous hydrogen chloride until substantially all of said contaminant is removed therefrom.

Claim 13

The process of claim 10 wherein the liquid hydrocarbon media is pre-dried prior to effecting removal of the lead contaminant by first contacting said hydrocarbon media with a suitable drying agent.

Claim 14

The process of claim 10 wherein the liquid hydrocarbon media is contacted with a suitable sorbent not having anhydrous hydrogen chloride adsorbed therein after effecting removal of the lead contaminant thereby adsorbing any anhydrous hydrogen chloride desorbed during said removal process.