PROCESS TO REDUCE ACIDITY OF CRUDE OIL

• US 20090159504A1
• Filed: 11/24/2008
• Published: 06/25/2009
• Est. Priority Date: 11/28/2007
• Status: Active Grant

• Current Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Original Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Inventors: Al-Shareef, Ali, Choi, Ki-Hyouk
• Granted Patent: US 9,295,957 B2
• Time in Patent Office: Days
• US Class Current: 208/249
• CPC Class Codes: B01J 3/008 Processes carried out under supercritical conditions
• 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 2300/206 Asphaltenes
• CPC Class Codes: C10G 2300/4081 Recycling aspects
• CPC Class Codes: C10G 2300/805 Water
• CPC Class Codes: C10G 31/08 by treating with water
• CPC Class Codes: C10G 45/26 Steam or water
• CPC Class Codes: C10G 47/32 in the presence of hydrogen-generating compounds
• CPC Class Codes: C10G 75/00 Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general C10G7/10, C10G9/16 take precedence
• CPC Class Codes: C10G 9/00 Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
• CPC Class Codes: E21B 43/16 Enhanced recovery methods for obtaining hydrocarbons

Abstract

A process to reduce the acidity of acidic crude oils for preventing corrosion during processing of the crude oils, including transferring through pipe lines, tanker ships and tank vehicles. Crude oil having substantial amount of organic acid, in particular, naphthenic acid compounds is contacted with supercritical water and a catalyst for deacidification. A treated crude oil product has lower amounts of organic acid compounds than the original crude oil.

Claims

1. A process for reducing the acidity of an acidic crude oil, comprising the steps of:

obtaining a petroleum reservoir supply of acidic crude oil, wherein the petroleum reservoir has an on-site production facility;

mixing the acidic crude oil with water at a weight ratio of about 10;

1 to about 1;

50 to form a crude oil/water mixture, such mixing operable to occur at the on-site production facility;

heating the crude oil/water mixture to a crude oil/water temperature in the range of about 10°

C. to about 150°

C. to form a pumpable crude oil/water mixture;

pumping the pumpable crude oil/water mixture to a pressure of at least about 22.1 MPa to form a pressurized crude oil/water mixture;

pre-heating the pressurized crude oil/water mixture to a pressurized temperature in the range of about 150°

C. to about 350°

C.;

contacting the pressurized crude oil/water mixture with a metal oxide catalyst in a reaction zone, wherein the reaction zone comprises main reactor having an interior portion;

heating the pressurized crude oil/water mixture to a reaction temperature range of about 374°

to about 600°

C. while maintaining the pressure at or above at least about 22.1 MPa for a reaction period of time operable to produce a treated crude oil having a significantly reduced TAN in comparison to the TAN of the acidic crude oil;

reducing the pressure of the treated crude oil using a pressure regulating device to create a pressure-reduced treated mixture;

separating the pressure-reduced treated mixture into a gas portion and a liquid portion;

separating the liquid portion into recovered water and low acidity oil; and

collecting the low acidity oil wherein the low acidity oil is an upgraded crude oil having reduced amounts of asphaltene, sulfur, nitrogen or metal containing substances as compared to the acidic crude oil.

2. The process of claim 1 where the acidic crude oil has a TAN of at least about 0.3

3. The process of claim 1, wherein the main reactor is generally vertically in orientation, such that the pressurized crude oil/water mixture flows downwardly through the vertically oriented reactor, such that the pressurized crude oil water mixture flows downwardly through the reaction zone.

4. The process of claim 1, wherein the step of separating the liquid portion into recovered water and low acidity oil further comprises the step of feeding the pressure-reduced treated mixture to an oil-water separation facility, such that the low acidity oil is generally separated from the water.

5. The process of claim 1, wherein the step of mixing the acidic crude oil with water is conducted at a weight ratio of about 10:

1 to about 1;

10 to form a crude oil/water mixture.

6. The process of claim 1, wherein the pressure regulating device comprises at least one pressure regulating device.

7. The process of claim 1, wherein the process is conducted without an external supply of hydrogen.

8. The process of claim 1, wherein the metal oxide catalyst comprises ZrO₂.

9. The process of claim 1, wherein the petroleum reservoir supply of acidic crude oil contains an initial density and viscosity and an initial concentration of sulfur and heavy metals;

wherein the low acidity oil has a density and viscosity lower than the density and viscosity of the acidic crude oil; and

wherein concentration of sulfur and heavy metals in the low acidity oil is lower than the concentration of sulfur and heavy metals in the acidic crude oil.

10. The process of claim 1, further comprising the steps of:

recycling the recovered water by combining at least a portion of the recovered water with the water to form the crude oil/water mixture.

11. The process of claim 10, further comprising the steps of

pumping and heating the recovered water to at or above supercritical conditions;

adding oxygen to the recovered water

treating the recovered water with oxygen at or above supercritical conditions in an oxidation reactor to create a cleaned recovered water stream such that the cleaned recovered water stream contains substantially less hydrocarbon content than the recovered water.

12. The process of claim 11,

wherein the step of treating the recovered water with oxygen in the oxidation reactor creates thermal energy released from oxidation reaction;

and

further comprising the step of transferring, through heat exchange, at least a portion of the thermal energy released from oxidation reaction upstream in the process for reducing the acidity of an acidic crude oil.

13. The process of claim 10, wherein the oxygen is supplied by an oxygen source selected from the group of oxygen sources consisting of:

air, liquefied oxygen, hydrogen peroxide, organic peroxide and combinations of the same.

14. A process to reducing the acidity of an acidic crude oil at an on-site production facility, comprising the steps of:

pumping the acidic crude oil to a pressure at or exceeding the critical pressure of water to create pressurized acidic crude oil, the pressurized acidic crude oil being maintained at a temperature not to exceed 150 degrees C.;

obtaining a supply of water and pumping the water to a pressure at or exceeding the critical pressure of water and heating the water to a temperature at or above the critical temperature of water to create pressurized water;

at the on-site production facility, mixing the pressurized acidic crude oil and the pressurized water to form a pressurized crude oil/water mixture;

pre-heating the pressurized crude oil/water mixture to about 150°

C. to about 350°

C. to form a pre-heated mixture;

contacting the preheated mixture with a metal oxide catalyst in a reaction zone and heating the preheated mixture to between about 3740 to about 600°

C. while maintaining pressure at least at or above about 22.1 MPa for a reaction period of time operable to produce a treated crude oil having a significantly reduced TAN in comparison to the TAN of the acidic crude oil;

cooling the treated crude oil in a cooler;

reducing the pressure of the treated crude oil using a pressure regulating device to create a pressure-reduced treated mixture;

separating the pressure-reduced treated mixture into a gas portion and a liquid portion;

separating the liquid portion into recovered water and low acidity oil; and

collecting the low acidity oil wherein the low acidity oil is an upgraded crude oil having reduced amounts of asphalthene, sulfur, nitrogen or metal containing substances as compared to the acidic crude oil.

15. The process of claim 14, wherein the acidic crude oil and the water are mixed at a weight ratio of about 10:

1 to about 1;

10

16. The process of claim 14, wherein the reaction zone comprises a main reactor, and the main reactor is generally vertically in orientation, such that the pressurized crude oil/water mixture flows downwardly through the vertically oriented reactor, such that the pressurized crude oil water mixture flows downwardly through the reaction zone.

17. The process of claim 14, wherein the step of separating the liquid portion into recovered water and low acidity oil further comprises the step of feeding the pressure-reduced treated mixture to an oil-water separation facility, such that the low acidity oil is generally separated from the water.

18. The process of claim 14, wherein the step of mixing the acidic crude oil with water is conducted at a weight ratio of about 10:

1 to about 1;

10 to form a crude oil/water mixture.

19. The process of claim 14, wherein the pressure regulating device comprises at least one pressure regulating device.

20. The process of claim 14, wherein the process is conducted without an external supply of hydrogen.

21. The process of claim 14, wherein the metal oxide catalyst comprises ZrO₂.

22. The process of claim 14, wherein the petroleum reservoir supply of acidic crude oil contains an initial density and viscosity and an initial concentration of sulfur and heavy metals;

wherein the low acidity oil has a density and viscosity lower than the density and viscosity of the acidic crude oil; and

wherein concentration of sulfur and heavy metals in the low acidity oil is lower than the concentration of sulfur and heavy metals in the acidic crude oil.

23. The process of claim 14, further comprising the steps of:

recycling the recovered water by combining at least a portion of the recovered water with the water to form the crude oil/water mixture.

24. The process of claim 23, further comprising the steps of

pumping and heating the recovered water to at or above supercritical conditions;

adding oxygen to the recovered water

treating the recovered water with oxygen at or above supercritical conditions in an oxidation reactor to create a cleaned recovered water stream such that the cleaned recovered water stream contains substantially less hydrocarbon content than the recovered water

25. The process of claim 23,

wherein the step of treating the recovered water with oxygen in the oxidation reactor creates thermal energy released from oxidation reaction;

and

further comprising the step of transferring through heat exchange at least a portion of the thermal energy released from oxidation reaction upstream in the process for reducing the acidity of an acidic crude oil.