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

Patent metadata

Field	Value
Publication number	US-10808180-B2
Application number	US-201816007817-A
Country	US
Kind code	B2
Filing date	Jun 13, 2018
Priority date	Sep 8, 2016
Publication date	Oct 20, 2020
Grant date	Oct 20, 2020

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 plant system, the system comprising:
a crude oil inlet feed stream;
a low pressure production trap (LPPT), where the LPPT comprises an inlet mixing device operable to thoroughly mix an LPPT inlet feed stream;
a low pressure degassing tank (LPDT), where the LPDT is fluidly coupled to the LPPT;
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; and
a second KOD fluidly coupled to the LPPT and operable to accept a low pressure off-gas from the LPPT.

2. The system according to claim 1 , further comprising at least one heat exchanger operable to heat crude oil.

3. The system according to claim 1 , further comprising a low pressure compressor fluidly coupled to the second KOD and operable to compress low pressure off-gas from the LPPT; a cooler, where the cooler is fluidly coupled to the low pressure compressor; and a third KOD, where the third KOD is fluidly coupled to the cooler.

4. The system according to claim 3 , further comprising at least one dehydrator unit operable to substantially dehydrate crude oil and at least one desalter unit operable to substantially desalt crude oil.

5. The system according to claim 4 , further comprising a cold stabilizer, where an atmospheric off-gas outlet of the cold stabilizer is fluidly coupled to the first KOD.

6. The system according to claim 5 , further comprising an oil/water separator device operable to accept an oily water output stream from the LPPT, and accept an oily water output stream from the LPDT, and where the oil/water separator device is operable to separate oil from water, and operable to recycle oil to the LPDT.

7. The system according to claim 6 , where the cold stabilizer further comprises a stripping gas stream, where the stripping gas stream is operable to supply steam in addition to or alternative to an additional stripping gas low in H 2 S concentration relative to crude oil in the cold stabilizer, where the stripping gas stream is operable to lower concentration of H 2 S in crude oil in the cold stabilizer.

8. The system according to claim 7 , where the system is operable to refine crude oil in the crude oil inlet feed stream 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.).

9. The system according to claim 1 , where operating pressure within the LPPT is greater than operating pressure in the LPDT.

10. The system according to claim 7 , where the system is operable to dehydrate, desalt, sweeten, and stabilize crude oil to produce crude oil safe for storage and shipment with only three KOD's.

Assignees

• Saudi Arabian Oil Co

Inventors

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

Classifications

• C10G2300/207

  Acid gases, e.g. H2S, COS, SO2, HCN · CPC title

• C10G33/00

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

• C10G5/06

  by cooling or compressing · CPC title

• C10G33/02

  with electrical or magnetic means · CPC title

• C10G2300/205

  Metal content · CPC title