Feed hydrotreating for improved thermal cracking

Claim 2

In a process for pretreating a feed for the subsequent production of light olefins and mononuclear aromatics by thermal cracking wherein the feed is catalytically hydrotreated without excessive hydrocracking and gas production, the improvement comprising:

Claim 3

said hydrotreating being effected at a temperature of from 640° F. to 950° F. and a pressure of from 750 to 2500 psig, in the presence of a catalyst containing at least one group VI metal selected from the group consisting of tungsten and molybdenum and at least one group VIII metal selected from the group consisting of nickel and cobalt, said catalyst being promoted with at least 0.5 weight% of a member selected from the group consisting of fluorine, chlorine and mixtures thereof to thereby alter the feed to increase the yield of light olefins and mononuclear aromatics in the subsequent thermal cracking thereof.

Claim 4

said hydrotreating being effected at a temperature of from 640° F. to 950° F. and a pressure of from 750 to 2500 psig, in the presence of a catalyst containing at least one group VI metal selected from the group consisting of tungsten and molybdenum and at least one group VIII metal selected from the group consisting of nickel and cobalt, said catalyst being promoted with at least 0.5 weight% of a member selected from the group consisting of fluorine, chlorine and mixtures thereof to thereby alter the feed to increase the yield of light olefins and mononuclear aromatics in the subsequent thermal cracking thereof.

Claim 5

The process of claim 1 wherein the catalyst is promoted with chlorine.

Claim 6

The process of claim 2 wherein the feed has an initial boiling point of at least 350° F. and end point of no greater than 1100° F.

Claim 7

The process of claim 3 wherein the hydrotreating is effected at a temperature of from 650° F. to 750° F. and a pressure of from 900 to 1500 psig.

Claim 8

The process of claim 4 wherein a chloro-substituted hydrocarbon is included in the feed to maintain said catalyst promoted with chlorine.

Claim 9

The process of claim 3 wherein the hydrotreated feed contains a 400° to 800° F. fraction in an amount which is no less than 85% of the amount of the 400° to 800° F. fraction present in the feed.

Claim 10

The process of claim 6 wherein said catalyst contains at least 1 weight % of chlorine and no greater than 10 weight % of chlorine.

Claim 11

The process of claim 7 wherein the hydrotreating is effected with hydrogen in an amount of from 1000 to 15,000 SCF/bbl, and the liquid hourly space velocity is from 0.5 to 3.0 V/H/V.

Claim 12

The process of claim 1 wherein the catalyst is promoted with fluorine.

Claim 13

The process of claim 9 wherein the feed has an initial boiling point of at least 350° F. and end point of no greater than 1100° F.

Claim 14

The process of claim 10 wherein the hydrotreated feed contains a 400° to 800° F. fraction in an amount which is no less than 85% of the amount of the 400° to 800° F. fraction present in the feed.

Claim 15

The process of claim 6 wherein the feed is a gas oil fraction.