Petroleum Upgrading and Desulfurizing Process

• US 20120181217A1
• Filed: 01/19/2011
• Published: 07/19/2012
• Est. Priority Date: 01/19/2011
• Status: Active Grant

• Current Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Original Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Inventors: Choi, Ki-Hyouk, Aljishi, Mohammad F.
• Granted Patent: US 8,535,518 B2
• Time in Patent Office: Days
• US Class Current: 208/99
• CPC Class Codes: C10G 21/08 Inorganic compounds only
• CPC Class Codes: C10G 2300/1033 Oil well production fluids
• CPC Class Codes: C10G 2300/202 Heteroatoms content, i.e. S, N, O, P
• CPC Class Codes: C10G 2300/205 Metal content
• CPC Class Codes: C10G 2300/308 Gravity, density, e.g. API
• CPC Class Codes: C10G 2300/4006 Temperature
• CPC Class Codes: C10G 2300/4012 Pressure
• CPC Class Codes: C10G 2300/805 Water
• CPC Class Codes: C10G 2400/04 Diesel oil
• CPC Class Codes: C10G 25/00 Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
• CPC Class Codes: C10G 45/02 to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
• CPC Class Codes: C10G 47/00 Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06
• CPC Class Codes: C10G 47/32 in the presence of hydrogen-generating compounds
• CPC Class Codes: C10G 55/04 including at least one thermal cracking step

Abstract

A petroleum feedstock upgrading method is provided. The method includes supplying a mixed stream that includes hydrocarbon feedstock and water to a hydrothermal reactor where the mixed stream is maintained at a temperature and pressure greater than the critical temperatures and pressure of water in the absence of catalyst for a residence time sufficient to convert the mixed stream into a modified stream having an increased concentration of lighter hydrocarbons and/or concentration of sulfur containing compounds. The modified stream is then supplied to an adsorptive reaction stage charged with a solid adsorbent operable to remove at least a portion of the sulfur present to produce a trimmed. The trimmed stream is then separated into a gas and a liquid streams, and the liquid stream is separated into a water stream and an upgraded hydrocarbon product stream.

Claims

1. A method of upgrading a hydrocarbon feedstock, the method comprising the steps of:

supplying a mixed stream comprising the hydrocarbon feedstock and water to a hydrothermal reactor, wherein the mixed stream is maintained at a pressure between about 22.06 and 25 MPa and a temperature of between about 372°

C. and about 425°

C., wherein the hydrothermal reactor does not include a catalyst;

maintaining the mixed stream in the hydrothermal reactor at said pressure and temperature for a period of at least about 10 minutes to produce a first product stream, said first product stream comprising a higher concentration of lighter hydrocarbons than the hydrocarbon feedstock;

supplying the first product stream from the hydrothermal reactor to an adsorptive reaction stage to produce an trimmed stream;

separating the trimmed stream into a gas-phase stream and a liquid-phase stream; and

separating the liquid stream into a water stream and an upgraded hydrocarbon product stream.

2. The method of claim 1 wherein the adsorptive reaction stage is charged with a solid adsorbent.

3. The method of claim 1 wherein the adsorptive reaction stage is charged with a solid adsorbent, wherein the solid adsorbent includes up to four active materials selected from the group consisting of elements from Group IB, Group IIB, Group IVB, Group VB, Group VIB, Group VIIB, and Group VIIIB of the periodic table.

4. The method of claim 3 wherein the solid adsorbent further includes a promoting material selected from up to four elements selected from the group consisting of elements from Group IA, Group IIA, Group IIIA and Group IVA of the periodic table.

5. The method of claim 3 wherein the solid adsorbent further includes a modifying material selected from up to four elements selected from the group consisting of elements from Group VIA and Group VIIA of the periodic table.

6. The method of claim 1 wherein solid adsorbent includes a support material selected from up to four compounds selected from the group consisting of aluminum oxide, silicon oxide, titanium oxide, magnesium oxide, yttrium oxide, lanthanum oxide, cerium oxide, zirconium oxide and activated carbon.

7. The method of claim 1 wherein the mixed stream is pre-heated to a temperature of at least 350°

C. before being supplied to the hydrothermal reactor.

8. The method of claim 1 wherein the hydrocarbon feedstock is selected from whole range crude oil, topped crude oil, liquefied coal, a product stream from a petroleum refinery, a product stream from a steam cracker, or a liquid product recovered from oil sand, bitumen or asphaltene.

9. The method of claim 1, wherein the upgraded hydrocarbon produce stream has at least one of a higher API gravity, higher middle distillate yield, lower content of sulfur containing compounds, lower content of nitrogen compounds, or lower content of metal containing compounds.

10. A method of upgrading a hydrocarbon feedstock, the method comprising the steps of:

supplying a hydrocarbon feedstock stream to a pump to produce a pressurized hydrocarbon feedstock having a pressure of between about 24 MPa and about 26 MPa;

supplying the pressurized hydrocarbon feedstock to a first pre-heater to produce a pre-heated pressurized hydrocarbon feedstock, wherein the pressurized hydrocarbon feedstock is pre-heated to a temperature of between about 200°

C. and 250°

C.;

supplying a water stream to a pump to produce a pressurized water stream having a pressure of between about 24 MPa and about 26 MPa;

supplying the pressurized water stream to a second pre-heater to produce a pre-heated pressurized water stream, wherein the pressurized water stream is preheated to a temperature of between about 400°

C. and about 550°

C.;

combining the pre-heated pressurized hydrocarbon feedstock and pre-heated pressurized water stream to a mixing device to produce a pre-heated pressurized hydrocarbon feedstock,

supplying the pre-heated pressurized hydrocarbon feedstock to a hydrothermal reactor, wherein the hydrothermal reactor is catalyst-free and is maintained at a temperature of between about 22.06 MPa and about 25 MPa and a temperature of between about 372°

C. and about 425°

C., wherein the hydrocarbon feedstock is maintained in the hydrothermal reactor for a residence time of between about 30 seconds and about 10 minutes to produce a first product stream, wherein the first product stream has a lower sulfur content and a higher content of light hydrocarbons than the hydrocarbon feedstock;

reducing the temperature and pressure of the first product stream to produce a product stream having a temperature of less than about 372°

C. and a pressure of less than about 22.06 MPa;

supplying the product stream to an adsorptive reaction stage charged with a solid adsorbent to produce an trimmed stream, wherein the trimmed stream has a lower sulfur content than the first product stream;

separating the trimmed stream into a gas-phase stream and a liquid-phase stream; and

separating the liquid stream into a water stream and an upgraded hydrocarbon product stream, wherein the upgraded hydrocarbon product stream has at least one of a higher API gravity, a higher middle distillate yield, or a lower sulfur content than the hydrocarbon feedstock.

11. The method of claim 10 wherein the adsorptive reaction stage is charged with a solid adsorbent, wherein the solid adsorbent includes up to four active materials selected from the group consisting of elements from Group IB, Group IIB, Group IVB, Group VB, Group VIB, Group VIIB, and Group VIIIB of the periodic table.

12. The method of claim 11 wherein the solid adsorbent further includes a promoting material selected from up to four elements selected from the group consisting of elements from Group IA, Group IIA, Group IIIA and Group IVA of the periodic table.

13. The method of claim 11 wherein the solid adsorbent further includes a modifying material selected from up to four elements selected from the group consisting of elements from Group VIA and Group VIIA of the periodic table.

14. The method of claim 11 wherein solid adsorbent includes a support material selected from up to four compounds selected from the group consisting of aluminum oxide, silicon oxide, titanium oxide, magnesium oxide, yttrium oxide, lanthanum oxide, cerium oxide, zirconium oxide and activated carbon.

15. The method of claim 10 wherein the hydrocarbon feedstock is selected from whole range crude oil, topped crude oil, liquefied coal, a product stream from a petroleum refinery, a product stream from a steam cracker, or a liquid product recovered from oil sand, bitumen or asphaltene.