Additives for supercritical water process to upgrade heavy oil

Patent metadata

Field	Value
Publication number	US-11021659-B2
Application number	US-201815905089-A
Country	US
Kind code	B2
Filing date	Feb 26, 2018
Priority date	Feb 26, 2018
Publication date	Jun 1, 2021
Grant date	Jun 1, 2021

Abstract

A method of upgrading a petroleum feedstock, the method comprising the steps of introducing a disulfide oil, a water feed, and a petroleum feedstock to a supercritical water upgrading unit, and operating the supercritical water upgrading unit to produce a product gas stream, a product oil stream, and a used water stream.

First claim

That which is claimed is:

1. A method of upgrading a petroleum feedstock, the method comprising the steps of:
introducing a disulfide oil, a water feed, and the petroleum feedstock to a supercritical water upgrading unit, the disulfide oil comprising disulfides operable to enhance radical reactions and hydrogen transfer reactions of the petroleum feedstock in the supercritical water upgrading unit, wherein the disulfide oil comprises disulfides, wherein the disulfides comprise sulfur-containing compounds of the form Ci-SS-Cj, where C refers to carbon, where S refers to sulfur, where i is selected from 1, 2, 3, 4, 5, and 6, where 1 is selected from 1, 2, 3, 4, 5, and 6, wherein the disulfide oil comprises a total sulfur content of greater than 30% by weight; and
operating the supercritical water upgrading unit to produce a product gas stream, a product oil stream, and a used water stream, wherein a supercritical water reactor of the supercritical water upgrading unit is operated at a temperature between 380 deg C. and 600 deg C. and a pressure in the range between 3203 psig and 5150 psig.

2. The method of claim 1 , where the step of operating the supercritical water upgrading unit to produce the product gas stream, the product oil stream, and the used water stream comprises the steps of:
mixing the disulfide oil and the petroleum feedstock in a petroleum mixer to produce a mixed petroleum stream;
introducing the mixed petroleum stream to a petroleum pump;
increasing a pressure of the mixed petroleum stream to produce a pressurized petroleum stream;
introducing the pressurized petroleum stream to a petroleum heater;
increasing a temperature of the pressurized petroleum stream to produce a hot petroleum stream;
mixing the hot petroleum stream and a supercritical water stream to produce a mixed feed;
introducing the mixed feed to the supercritical water reactor;
allowing conversion reactions to occur in the supercritical water reactor to produce a modified stream;
introducing the modified stream to a cooling device;
reducing a temperature of the modified stream in the cooling device to produce a cooled stream;
introducing the cooled stream to a depressurizing device;
reducing the pressurizing in the depressurizing device to produce a discharged stream;
introducing the discharged stream to a gas-liquid separator;
separating the discharged stream in the gas-liquid separator to produce a product gas stream and a liquid phase stream;
introducing the liquid phase stream to an oil-water separator; and
separating the liquid phase stream in the oil-water separator to produce the product oil stream and the used water stream.

3. The method of claim 1 , further comprising the steps of:
introducing the product oil stream to a fractionator;
separating the product oil stream in the fractionator into a light fraction and a heavy fraction;
introducing the light fraction to a disulfide oil unit; and
producing a sweetened light fraction and the disulfide oil in the disulfide oil unit.

4. The method of claim 3 , where the disulfide oil unit is a merox unit.

5. The method of claim 3 , further comprising the step of:
mixing the sweetened light fraction and the heavy fraction to produce an upgraded oil product.

6. The method of claim 1 , further comprising the step of:
introducing a disulfide oil unit feed to a disulfide oil unit, where the disulfide oil unit feed is selected from the group consisting of natural gas, LPG, naphtha, and kerosene; and
producing the disulfide oil in the disulfide oil unit, where the disulfide oil unit is a caustic extraction process.

7. The method of claim 1 , where the petroleum feedstock is selected from the group consisting of an atmospheric residue, a vacuum residue, a vacuum gas oil, and a deasphalted oil.

8. The method of claim 1 , where the disulfide oil comprises greater than 50% by weight disulfides.

9. The method of claim 1 , where the product oil stream comprises an increased amount of upgraded hydrocarbons relative to the petroleum feedstock.

10. The method of claim 2 , where a total sulfur content of the mixed petroleum stream is in the range from between 0.05% by weight to 3% by weight greater than the total sulfur content in the petroleum feedstock.

Assignees

• Saudi Arabian Oil Co
• Saudi Arabia Oil Company

Inventors

• Choi Ki-Hyouk
• Shafei Emad N
• Albahar Mohammed Zuhair
• Ghabbani Abdulaziz A

Classifications

• C10G49/007 Primary

  in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment · CPC title

• C10G53/06

  including only extraction steps, e.g. deasphalting by solvent treatment followed by extraction of aromatics · CPC title

• C10G67/06

  including a sorption process as the refining step in the absence of hydrogen · CPC title

• C10G21/003

  Solvent de-asphalting · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title