Integrated gas oil separation plant for crude oil and natural gas processing

Patent metadata

Field	Value
Publication number	US-11168262-B2
Application number	US-202017024205-A
Country	US
Kind code	B2
Filing date	Sep 17, 2020
Priority date	Sep 8, 2016
Publication date	Nov 9, 2021
Grant date	Nov 9, 2021

Abstract

Systems and methods of integrated gas oil separation are disclosed. Systems include a high pressure production trap (HPPT), a low pressure production trap (LPPT), a low pressure degassing tank (LPDT), a first knockout drum (KOD) fluidly coupled to the LPDT and operable to accept an atmospheric pressure off-gas from the LPDT, an atmospheric pressure compressor fluidly coupled to the first KOD and operable to compress the atmospheric pressure off-gas to introduce the atmospheric pressure off-gas from the LPDT into the LPPT inlet feed stream, a second KOD fluidly coupled to the LPPT and operable to accept a low pressure off-gas from the LPPT, and a low pressure compressor fluidly coupled to the second KOD and operable to compress the low pressure off-gas to introduce the low pressure off-gas from the LPPT into the crude oil inlet feed stream.

First claim

What is claimed is:

1. An integrated gas oil separation method, the method comprising the steps of:
separating crude oil into a high pressure off-gas, an oily water output, and a partially dry, partially degassed crude oil output;
separating the partially dry, partially degassed crude oil output into a low pressure off-gas, and a further partially dry, further partially degassed crude oil output;
removing condensates from the low pressure off-gas;
compressing the low pressure off-gas;
separating the further partially dry, further partially degassed crude oil output into an atmospheric pressure off-gas, an oily water output, and a substantially degassed, partially dry crude oil output;
removing condensates from the atmospheric pressure off-gas;
compressing the atmospheric pressure off-gas;
increasing the temperature of the crude oil with the compressed low pressure off-gas; and
increasing temperature of the partially dry, partially degassed crude oil output with the compressed atmospheric pressure off-gas.

2. The method according to claim 1 , further comprising the steps of removing condensates from the high pressure off-gas; compressing the high pressure off-gas; cooling the high pressure off-gas; and removing condensates from the compressed high pressure off-gas.

3. The method according to claim 2 , further comprising the steps of substantially dehydrating the substantially degassed, partially dry crude oil output and substantially desalting the substantially degassed, partially dry crude oil output to produce a substantially degassed and substantially dry crude oil output.

4. The method according to claim 3 , further comprising the steps of cold stabilizing the substantially degassed and substantially dry crude oil output; removing condensates from an atmospheric off-gas of the cold stabilizing of the substantially degassed and substantially dry crude oil output; and compressing the atmospheric off-gas of the cold stabilizing of the substantially degassed and substantially dry crude oil output to heat the partially dry, partially degassed crude oil output.

5. The method according to claim 4 , further comprising the steps of separating oily water into oil and water and recycling the oil for further processing.

6. The method according to claim 5 , further comprising the step of gas stripping the substantially degassed and substantially dry crude oil output, where the step of gas stripping is operable to lower concentration of H 2 S in the substantially degassed and substantially dry crude oil output.

7. The method according to claim 6 , where the method is operable to refine crude oil to produce a refined crude oil product safe for storage and shipment meeting the following specifications: (1) a salt concentration of not more than about 10 pound (lbs.) of salt/1000 barrels (PTB); (2) basic sediment and water (BSW) of not more than about 0.3 volume percent (V %); (3) H 2 S concentration of less than about 60 ppm; and (4) a maximum RVP of about 7 pounds per square inch absolute (psia) and a maximum true vapor pressure (TVP) of about 13.5 psia at 130 degrees Fahrenheit (° F.).

8. The method according to claim 1 , where the method is operable to dehydrate, desalt, sweeten, and stabilize crude oil to produce crude oil safe for storage and shipment with only four knock out drums (KOD's).

9. An integrated gas oil separation method, the method comprising the steps of:
separating crude oil into a low pressure off-gas, an oily water output, and a partially dry, partially degassed crude oil output;
separating the partially dry, partially degassed crude oil output into an atmospheric pressure off-gas, an oily water output, and a substantially degassed, partially dry crude oil output;
removing condensates from the atmospheric pressure off-gas;
compressing the atmospheric pressure off-gas; and
increasing the temperature of the crude oil with the compressed low pressure off-gas.

10. The method according to claim 9 , further comprising the steps of removing condensates from the low pressure off-gas; compressing the low pressure off-gas; cooling the low pressure off-gas; and removing condensates from the cooled low pressure off-gas.

11. The method according to claim 10 , further comprising the steps of substantially dehydrating the substantially degassed, partially dry crude oil output and substantially desalting the substantially degassed, partially dry crude oil output to produce a substantially degassed, substantially dry crude oil output.

12. The method according to claim 11 , further comprising the steps of cold stabilizing the substantially degassed, substantially dry crude oil output; removing condensates from an atmospheric off-gas of the substantially degassed, substantially dry crude oil output; and compressing the atmospheric off-gas of the cold stabilizing of the substantially degassed, substantially dry crude oil output to heat the crude oil.

13. The method according to claim 12 , further comprising the steps of separating oily water into oil and water and recycling the oil for further processing.

14. The method according to claim 13 , further comprising the step of gas stripping the substantially degassed, substantially dry crude oil output, where the gas stripping is operable to lower concentration of H 2 S in the substantially degassed, substantially dry crude oil output.

15. The method according to claim 14 , where the method is operable to refine crude oil to produce a refined crude oil product safe for storage and shipment meeting the following specifications: (1) a salt concentration of not more than about 10 pound (lbs.) of salt/1000 barrels (PTB); (2) basic sediment and water (BSW) of not more than about 0.3 volume percent (V %); (3) H 2 S concentration of less than about 60 ppm; and (4) a maximum RVP of about 7 pounds per square inch absolute (psia) and a maximum true vapor pressure (TVP) of about 13.5 psia at 130 degrees Fahrenheit (° F.).

16. The method according to claim 9 , where the method is operable to dehydrate, desalt, sweeten, and stabilize crude oil to produce crude oil safe for storage and shipment with only three knock out drums (KOD's).

Assignees

• Saudi Arabian Oil Co

Inventors

• Soliman Mohamed
• Salu Samusideen Adewale
• Al-Zahrani Talal
• Ansari Nisar Ahmad K

Classifications

• C10G7/00 Primary

  Distillation of hydrocarbon oils · CPC title

• C10G33/00

  Dewatering or demulsification of hydrocarbon oils (by distillation C10G7/04) · CPC title

• C10G33/02

  with electrical or magnetic means · CPC title

• C10G31/06

  by heating, cooling, or pressure treatment · CPC title

• C10G5/06

  by cooling or compressing · CPC title