Refinery desalter improvement
The improved methods relate to desalting hydrocarbon feeds using a separator with a stacked disk centrifuge to separate an emulsified oil and water rag layer. This method is effective for desalting heavy, high ionic, and non-traditional crude oils.
1. A method of reducing a crude oil emulsion rag layer comprising:
a) separating an oil and water feedstream in a separator into at least three outgoing streams including an outgoing crude oil stream, an outgoing wastewater stream and an outgoing rag layer stream, wherein the rag layer is an emulsion formed between the crude oil and water;
b) removing said outgoing rag layer stream from said separator;
c) centrifuging the rag layer stream from the separator in a disk stack centrifuge and separating the rag layer stream into at least three separate streams including an outgoing crude oil stream, an outgoing wastewater stream and an outgoing solids rich stream;
d) removing a crude oil stream from the separator and the disk stack centrifuge; and
e) removing a wastewater stream from the separator and the disk stack centrifuge.
2. The method of claim 1 , wherein said separating step (a) additionally comprises separating the oil and water feedstream with a separator selected from the group consisting of one or more low pressure separators, high pressure separators, 2 phase separators, electrostatic coalescence separators, AC deep-field electrostatic separators, dual frequency separators, dual polarity combination AC/DC electrostatic separators, 3 phase separators, high velocity electrostatic coalescing separators, vessel internal electrostatic coalescers, and combinations thereof.
3. The method of claim 1 , wherein said centrifuging step (c) additionally comprises centrifugally separating the rag layer steam with a disk stack centrifuge is selected from the group consisting of nozzle separators, self-cleaning disk separators, solid-wall separators, and the like which contain a stack of conical disks either with or without chambers to collect a variety of materials separated using centrifugal forces.
4. The method of claim 1 , wherein said method further comprises heating said crude oil emulsion to a temperature between approximately 140° F. and 300° F., prior to said centrifuging step (c) in the stacked disk centrifuge.
5. The method of claim 1 , wherein said crude oil in the oil and water feedstream is selected from the group consisting of Athabasca oil sands (crude bitumen), Orinoco oil sands (extra heavy oil), Canadian Extra Heavy Oil (CXHO), Western Canadian Select (WCS), MacKay River Heavy (MRH), oil shales, crude bitumens, extra heavy oils, oilsands, tarsands, sour crudes, and mixtures thereof.
6. The method of claim 1 , wherein said water in the oil and water feedstream is selected from the group consisting of tap water, de-ionized (DI) water, recycled water, distilled water, chilled water, heated water, ultra-purified water, clarified water, and mixtures thereof.
7. The method of claim 1 , wherein the rag layer formed in the separator in separating step (a) includes particles and wherein the particle size distribution is approximately 1 to 20 μm.