Method for controlling a pretreatment process

Claim 2

In a process for decarbonizing, demetallizing and/or desalting a hydrocarbon feed stock by: contacting, in a selective vaporization step, for a short hydrocarbon residence time of less than 3 seconds at an elevated contact temperature, the feed stock with an inert solid contact material in a confined rising vertical column to vaporize a major portion of the feed stock and to provide, as combustible deposits on the contact material, an unvaporized minor portion of the feed stock which includes high Conradson Carbon components and/or metal-containing components of the feed stock; separating the vaporized major portion of the feed stock from the contact material bearing the combustible deposits and quenching to arrest thermal cracking; contacting in a combusion step the contact material, bearing the combustible deposits, with an oxidizing gas to oxidize the combustible deposits and generate heat, whereby the contact material is heated by combustion of the combustible deposits; and recycling the so-heated contact material to contact further feed stock in the selective vaporization step, the improvement comprising: contacting the contact material in the combustion step with less than the stoichiometric amount of oxidizing gas, required to oxidize completely the combustible deposits, so that oxidizable high Conradson Carbon and/or metal-containing components of the combustible deposits are only partially oxidized to carbon monoxide and so that there is a reducing atmosphere in the combustion step.

Claim 3

The process of claim 1 wherein the reducing atmosphere in the combustion step comprises about 0.1 to 10% by volume carbon monoxide.

Claim 4

The process of claim 1 wherein the reducing atmosphere in the combustion step comprises about 2 to 8% by volume carbon monoxide.

Claim 5

The process of claim 1 wherein the contact material comprises a high metal content solid.

Claim 6

The process of claim 4 wherein the contact material comprises microspheres of kaolin clay containing about 2 to 9% Fe 2 O 3 .

Claim 7

The process of claim 1 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a volatile material which is added to the feed stock in the selective vaporization step.

Claim 8

The process of claim 6 wherein the volatile material comprises steam, water or a hydrocarbon which can decrease the partial pressure of hydrocarbons in the feed stock.

Claim 9

The process of claim 1 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a fluidizing medium which is added to the contact material in the selective vaporization step before the contact material contacts the feed stock and which serves to transport the contact material up the confined rising vertical column.

Claim 10

The process of claim 8 wherein the fluidizing medium comprises steam or water.

Claim 11

The process of claim 1 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a cooling medium which is added to the contact material in the combustion step.

Claim 12

The process of claim 10 wherein the cooling medium comprises steam or water.

Claim 13

The process of claim 1 wherein carbonaceous deposits are formed on the contact material in the selective vaporization step and at least a portion of the carbonaceous deposits is maintained on the surface of the contact material during the combustion step and when the contact material is recycled to the selective vaporization step.

Claim 14

The process of claim 12 wherein the carbonaceous deposits, maintained on the surface of the contact material, comprise about 0.05% by weight or more of the contact material.

Claim 15

The process of claim 13 wherein the carbonaceous deposits, maintained on the contact material, comprise about 0.1-5% of the contact material.

Claim 16

In a process for decarbonizing, demetallizing and/or desalting a hydrocarbon feed stock by: contacting, in a selective vaporization step, for a short hydrocarbon residence time of less than 3 seconds at an elevated contact temperature, the feed stock with an inert solid contact material in a confined rising vertical column to vaporize a major portion of the feed stock and to provide, as combustible deposits on the contact material, an unvaporized minor portion of the feed stock which includes high Conradson Carbon components and/or metal-containing components of the feed stock; separating the vaporized major portion of the feed stock from the contact material bearing the combustible deposits and quenching to arrest thermal cracking; contacting in a combustion step the contact material, bearing the combustible deposits, with an oxidizing gas to oxidize the combustible deposits and generate heat, whereby the contact material is heated by combustion of the combustible deposits; and recycling the so-heated contact material to contact further feed stock in the selective vaporization step, the improvement comprising: contacting the contact material in the combustion step with less than the stoichiometric amount of oxidizing gas, required to oxidize completely the combustible deposits, so that oxidizable high Conradson Carbon and/or metal-containing components of the combustible deposits are only partially oxidized to carbon monoxide and so that there is a reducing atmosphere in the combustion step, and maintaining the temperature of the combustion step at a predetermined maximum by increasing or decreasing the contact temperature in the selective vaporization step within a range of preferred temperatures for vaporizing most of the feed stock but not the majority of its high Conradson Carbon components or its metal-containing components in order to respectively decrease or increase the unvaporized minor portion of the feedstock, deposited on the contact material.

Claim 17

In a process for decarbonizing, demetallizing and/or desalting a hydrocarbon feed stock by: contacting, in a selective vaporization step, for a short hydrocarbon residence time of less than 3 seconds at an elevated contact temperature, the feed stock with an inert solid contact material in a confined rising vertical column to vaporize a major portion of the feed stock and to provide, as combustible deposits on the contact material, an unvaporized minor portion of the feed stock which includes high Conradson Carbon components and/or metal-containing components of the feed stock; separating the vaporized major portion of the feed stock from the contact material bearing the combustible deposits and quenching to arrest thermal cracking; contacting in a combustion step the contact material, bearing the combustible deposits, with an oxidizing gas to oxidize the combustible deposits and generate heat, whereby the contact material is heated by combustion of the combustible deposits; and recycling the so-heated contact material to contact further feed stock in the selective vaporization step, the improvement comprising: contacting the contact material in the combustion step with less than the stoichiometric amount of oxidizing gas, required to oxidize completely the combustible deposits, so that oxidizable high Conradson Carbon and/or metal-containing components of the combustible deposits are only partially oxidized to carbon monoxide and so that there is a reducing atmosphere in the combustion step, and maintaining the temperature of the combustion step at a predetermined maximum by increasing or decreasing the contact temperature in the selective vaporization step within a range of preferred temperatures for vaporizing most of the feed stock but not the majority of its high Conradson Carbon components or its metal-containing components in order to respectively decrease or increase the unvaporized minor portion of the feedstock, deposited on the contact material.

Claim 18

The process of claim 15 wherein the reducing atmosphere in the combustion step comprises about 0.1 to 10% by volume carbon monoxide.

Claim 19

The process of claim 15 wherein the reducing atmosphere in the combustion step comprises about 2 to 8% by volume carbon monoxide.

Claim 20

The process of claim 15 which further comprises increasing the contact temperature in the selective vaporization step by increasing the recycle of heated contact material in order to decrease the temperature of the combustion step to its predetermined maximum when the reducing atmosphere in the combustion step contains more than about 8% carbon monoxide.

Claim 21

The process of claim 15 which further comprises decreasing the contact temperature in the selective vaporization step by decreasing the recycle of heated contact material in order to increase the temperature of the combustion step to its predetermined maximum when the reducing atmosphere in the combustion step contains less than about 2% carbon monoxide.

Claim 22

The process of claim 15 wherein the contact material comprises a high metal content solid.

Claim 23

The process of claim 20 wherein the contact material comprises microspheres of kaolin clay containing about 2 to 9% Fe 2 O 3 .

Claim 24

The process of claim 15 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a volatile material which is added to the feed stock in the selective vaporization step.

Claim 25

The process of claim 22 wherein the volatile material comprises steam, water or a hydrocarbon which can decrease the partial pressure of hydrocarbons in the feed stock.

Claim 26

The process of claim 15 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a fluidizing medium which is added to the contact material in the selective vaporization step before the contact material contacts the feed stock and which serves to transport the contact material up the confined rising vertical column.

Claim 27

The process of claim 24 wherein the fluidizing medium comprises steam or water.

Claim 28

The process of claim 15 which further comprises maintaining the temperature of the combustion step at a predetermined maximum by varying the feed rate and/or the temperature of a cooling medium which is added to the contact material in the combustion step.

Claim 29

The process of claim 26 wherein the cooling medium comprises steam or water.

Claim 30

The process of claim 15 wherein carbonaceous deposits are formed on the contact material in the selective vaporization step and at least a portion of the carbonaceous deposits is maintained on the surface of the contact material during the combustion step and when the contact material is recycled to the selective vaporization step.

Claim 31

The process of claim 28 wherein the carbonaceous deposits, maintained on the surface of the contact material, comprise about 0.05% by weight or more of the contact material.

Claim 32

The process of claim 29 wherein the carbonaceous deposits, maintained on the contact material, comprise about 0.1-5% of the contact material.