Method to remove metals from petroleum

Patent metadata

Field	Value
Publication number	US-9926497-B2
Application number	US-201514885315-A
Country	US
Kind code	B2
Filing date	Oct 16, 2015
Priority date	Oct 16, 2015
Publication date	Mar 27, 2018
Grant date	Mar 27, 2018

Abstract

A method to remove a metals impurity from a petroleum feedstock for use in a power generating process is provided. The method comprising the steps of mixing a heated feedstock with a heated water stream in a mixing device to produce a mixed stream; introducing the mixed stream to a supercritical water reactor in the absence of externally provided hydrogen and externally provided oxidizing agent to produce a reactor effluent comprising a refined petroleum portion; cooling the reactor effluent to produce a cooled stream; feeding the cooled stream to a rejecter configured to separate a sludge fraction to produce a de-sludged stream; reducing the pressure of the de-sludged stream to produce a depressurized product; separating the depressurized product to produce a gas phase product and a liquid product; separating the liquid product to produce a petroleum product, having a reduced asphaltene content, reduced concentration of metals impurity, and reduced sulfur.

First claim

That which is claimed is:

1. A method to remove a metals impurity from a petroleum feedstock for use in a power generating process, the method comprising the steps of:
mixing a heated feedstock with a heated water stream in a mixing device to produce a mixed stream, the heated feedstock comprising the metals impurity, wherein the heated feedstock is heated to a feedstock temperature of 150° C. and a feedstock pressure greater than the critical pressure of water, wherein the heated water stream is heated to a water temperature above the critical temperature of water and a water pressure above the critical pressure of water,
wherein the mixed stream comprises an asphaltene and resin portion, a hydrocarbon portion, and a supercritical water portion;

introducing the mixed stream to a supercritical water reactor in the absence of externally provided hydrogen and externally provided oxidizing agent to produce a reactor effluent, the reactor effluent comprising a refined petroleum portion, converted metals, and an amount of solid coke, wherein demetallization reactions and a set of conversion reactions occur in the supercritical water reactor, wherein the demetallization reactions are operable to convert the metals impurity to converted metals, wherein the set of conversion reactions is operable to refine the hydrocarbon portion in the presence of the supercritical water portion to produce the refined petroleum portion;
cooling the reactor effluent in a cooling device to produce a cooled stream;
feeding the cooled stream to a rejecter separator process vessel, the rejecter separator process vessel configured to separate a sludge fraction from the cooled stream to produce a de-sludged stream, the rejecter separator process vessel having a rejecter temperature, the sludge fraction comprising the asphaltene and resin portion and the converted metals;
reducing the pressure of the de-sludged stream in a depressurizing device to produce a depressurized product;
separating the depressurized product in a gas-liquid separator to produce a gas phase product and a liquid product;
separating the liquid product in an oil-water separator to produce a petroleum product and a water product, the petroleum product having a liquid yield, the petroleum product having a reduced asphaltene content, reduced concentration of metals impurity, and reduced sulfur as compared to the petroleum feedstock.

2. The method of claim 1 , wherein the petroleum feedstock is a petroleum-based hydrocarbon selected from the group consisting of whole range crude oil, reduced crude oil, fuel oil, refinery streams, residues from refinery streams, cracked product streams from crude oil refinery, atmospheric residue streams, vacuum residue streams, coal-derived hydrocarbons, liquefied coal, bitumen, biomass-derived hydrocarbons, and hydrocarbon streams from other petrochemical processes.

3. The method of claim 1 , wherein the metals impurity is selected from the group consisting of vanadium, nickel, iron and combinations thereof.

4. The method of claim 1 , wherein the metals impurity comprises a metal porphyrin.

5. The method of claim 1 , wherein the set of conversion reactions is selected from the consisting of upgrading, desulfurization, denitrogenation, deoxygenation, cracking, isomerization, alkylation, condensation, dimerization, hydrolysis, hydration, and combinations thereof.

6. The method of claim 1 , wherein the rejecter separator process vessel comprises a rejecter adsorbent.

7. The method of claim 1 , wherein the rejecter separator process vessel comprises a rejecter solvent.

8. The method of claim 1 , wherein the rejecter separator process vessel is selected from the group consisting of a cyclone-type vessel, a tubular-type vessel, a CSTR, and a centrifuge.

9. The method of claim 1 , wherein the amount of solid coke in the reactor effluent is less than 1.5 wt % by petroleum feedstock.

10. The method of claim 1 , wherein the concentration of metals impurity in the petroleum product is less than 2 ppm by wt.

11. The method of claim 1 , wherein the liquid yield of the petroleum product is greater than 96%.

12. A method to remove a metals impurity from a petroleum feedstock for use in a power generating process, the method comprising the steps of:
mixing a heated feedstock with a heated water stream in a mixing device to produce a mixed stream, the heated feedstock comprising the metals impurity, wherein the heated feedstock is heated to a feedstock temperature of 150° C. and a feedstock pressure greater than the critical pressure of water, wherein the heated water stream is heated to a water temperature above the critical temperature of water and a water pressure above the critical pressure of water,
wherein the mixed stream comprises an asphaltene and resin portion, a hydrocarbon portion, and a supercritical water portion;

introducing the mixed stream to a supercritical water reactor in the absence of externally provided hydrogen and externally provided oxidizing agent to produce a reactor effluent, the reactor effluent comprising a refined petroleum portion and converted metals, wherein a demetallization reaction and a set of conversion reactions occur in the supercritical water reactor, wherein the demetallization reactions are operable to convert the metals impurity to converted metals, wherein the set of conversion reactions is operable to refine the hydrocarbon portion in the presence of the supercritical water portion to produce the refined petroleum portion;
cooling the reactor effluent in a cooling device to produce a cooled stream;
reducing the pressure of the cooled stream in a depressurizing device to produce a depressurized stream, wherein the depressurized stream comprises the refined petroleum portion, an asphaltene fraction, a water fraction, and a gas phase product fraction;
separating the depressurized stream in a gas-liquid separator to produce a gas product and a liquid phase stream;
separating the liquid phase stream in an oil-water separator to produce a liquid-phase petroleum stream and a water phase stream;
feeding the liquid-phase petroleum stream to a solvent extractor;
extracting a petroleum product from the liquid-phase petroleum stream in the solvent extractor to leave a metal-containing fraction, the petroleum product having reduced asphaltene content, reduced concentration of metals impurity, and reduced sulfur as compared to the petroleum feedstock.

13. The method of claim 11 , wherein the petroleum feedstock is a petroleum-based hydrocarbon selected from the group consisting of whole range crude oil, reduced crude oil, fuel oil, refinery streams, residues from refinery streams, cracked product streams from crude oil refinery, atmospheric residue streams, vacuum residue streams, coal-derived hydrocarbons, liquefied coal, bitumen, biomass-derived hydrocarbons, and hydrocarbon streams from other petrochemical processes.

14. The method of claim 11 , wherein the metals impurity is selected from the group consisting of vanadium, nickel, iron and combinations thereof.

15. The method of claim 11 , wherein the metals impurity comprises a metal porphyrin.

16. The method of claim 11 , wherein the set of conversion reactions is selected from the consisting of upgrading, desulfurization, denitrogenation, deoxygenation, cracking, isomerization, alkylation, condensation, dimerization, hydrolysis, hydration, and combinations thereof.

17. The method of claim 11 , wherein the solvent extractor comprises a solvent deasphalting process.

18. The method of claim 11 , wherein the a

Assignees

• Saudi Arabian Oil Co

Inventors

• Choi Ki-Hyouk
• Shafei Emad N
• Punetha Ashok K
• Lee Joo-Hyeong
• Alabdullah Mohammad A

Classifications

• C10G2300/202

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

• C10G31/10

  with the aid of centrifugal force · CPC title

• C10G31/08

  by treating with water · CPC title

• C10G31/06

  by heating, cooling, or pressure treatment · CPC title

• C10G21/08 Primary

  Inorganic compounds only · CPC title