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 media containing said contaminant which comprises contact of said hydrocarbon media at a temperature below the boiling point thereof with a solid sorbent 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 wherein 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 wherein 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 4 where said sorbent is amorphous silica-alumina.

Claim 7

The process of claim 4 where said sorbent is an amorphous silica-alumina, silica-clay, or other gel-type matrix containing a minor proportion of crystalline aluminosilicate zeolite.

Claim 8

Process of claim 6 where said crystalline aluminocilicate is a form of zeolite X.

Claim 9

Process of claim 7 where said crystalline aluminosilicate is a form of zeolite Y.

Claim 10

The process of claim 4 where said sorbent is a synthetic faujasite.

Claim 11

The process of claim 9 where average pore diameter is about 8-9 Å and the average surface area is from about 200-1000 m 2 /g.

Claim 12

The process of claim 9 where the amount of HCl adsorbed is from about 00.1 to 17.5 wt. %.

Claim 13

The process of claim 11 where the amount of HCl adsorbed is at least about 0.1 wt. %.

Claim 14

The process of claim 5 where the amount of HCl adsorbed is from about 0.1-17.5 wt. %.

Claim 15

The process of claim 13 where the amount of HCl adsorbed is at least about 1 wt. %.

Claim 16

The process of claim 5 where the average pore diameter is from about 20 to about 100 Å and the average surface area is from about 150 to about 600 m 2 /g.

Claim 17

The process of claim 15 where the sorbent is an amorphous silica/alumina having from about 5 to about 95 wt. % silica.

Claim 18

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

Claim 19

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

Claim 20

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

Claim 21

The process of claim 19 where said motor fuel is an unleaded gasoline.

Claim 22

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 23

A process for effecting the removal of alkyl lead contaminant from liquid hydrocarbon media containing said contaminant which comprises contacting it at a temperature of from about 25°-60° C. and a LHSV of from about 5-20 with a solid sorbent 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 0.001-20 wt. % of anhydrous hydrogen chloride until substantially all of said contaminant is removed therefrom.

Claim 24

A process for effecting the removal of alkyl lead contaminant from liquid hydrocarbon media containing said contaminant which comprises contacting it at a temperature of from about 25°-60° C. and a LHSV of from about 5-20 with a solid sorbent 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 0.001-20 wt. % of anhydrous hydrogen chloride until substantially all of said contaminant is removed therefrom.

Claim 25

The process of claim 22 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 26

The process of claim 22 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.