Simultaneous crude oil dehydration, desalting, sweetening, and stabilization with compression
Integrated gas oil separation plant systems and methods, one system including a crude oil inlet feed stream; a low pressure production trap (LPPT); a low pressure degassing tank (LPDT); a first heat exchanger, where the first heat exchanger is fluidly disposed between the LPPT and LPDT, and is fluidly coupled to both the LPPT and LPDT, and where the first heat exchanger is operable to heat the LPDT inlet feed stream with compressed gas removed from the crude oil inlet feed stream; a first inline gas mixer preceding the LPPT to directly mix compressed gas from the LPDT into the LPPT inlet feed stream; and a LPDT recycle water stream, where the LPDT recycle water stream is operable to supply recycle water from the LPDT to the LPPT inlet feed stream.
1. A method for integrated gas oil separation, the method comprising the steps of:
supplying a crude oil inlet feed stream;
removing from the crude oil inlet feed stream a low pressure crude oil off-gas stream for compression;
heating the crude oil inlet feed stream with heat provided by processed dry crude oil;
mixing the crude oil inlet feed stream with compressed low pressure gas from a low pressure degassing tank (LPDT) and a cold stabilizer;
initially separating the crude oil inlet feed stream in a low pressure production trap (LPPT) into a LPPT off-gas stream, the LPPT off-gas stream to be compressed with the
low pressure crude oil off-gas stream, a partially-dried crude oil stream, and an oily-water stream for treatment;
heating the partially-dried crude oil stream with compressed gas from the low pressure crude oil off-gas stream and the LPPT off-gas stream;
further separating the partially-dried crude oil stream in the LPDT to produce a LPDT off-gas stream, a dried crude oil stream, and a recycle water stream for recycle to the crude oil inlet feed stream;
desalting the dried crude oil stream to produce a dried, desalted crude oil stream and a recycle water stream for recycle to the LPDT;
stabilizing the dried, desalted crude oil stream to produce a crude oil export stream, the crude oil export stream used to heat the crude oil inlet feed stream, and an atmospheric off-gas stream; and
compressing the LPDT off-gas stream and the atmospheric off-gas stream for the step of mixing the crude oil inlet feed stream with compressed low pressure gas from the low pressure degassing tank (LPDT) and the cold stabilizer.
2. The method according to claim 1 , wherein the LPPT comprises an inlet mixing device operable to thoroughly mix an LPPT inlet feed stream, a plurality of insulated electrostatic electrodes, and a weir; and wherein the LPDT comprises an inlet mixing device operable to thoroughly mix an LPDT inlet feed stream, a plurality of insulated electrostatic electrodes, and a weir.
3. The method according to claim 1 , wherein the step of removing from the crude oil inlet feed stream a low pressure crude oil off-gas stream for compression includes the use of an inline gas separator preceding the LPPT.
4. The method according to claim 1 , further comprising the step of removing condensate from compressed off-gas using at least one knock-out drum.
5. The method according to claim 1 , further comprising the step of supplying a fresh water wash stream to aid in the step of desalting.
6. The method according to claim 1 , further comprising the step of supplying a stripping gas stream, the stripping gas stream to supply steam, in addition to or alternative to a low concentration H 2 S stripping gas.
7. The method according to claim 1 , where the method 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 (B SW) 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.).