Desalting process

Claim 2

In a process wherein an oil-water mixture containing water-insoluble solids is introduced continuously into a separating zone to produce an upper oil phase, a lower water phase and an interfacial cuff emulsion containing water-insoluble solids, and wherein oil and water are withdrawn from the oil phase and water phase respectively, the improvement comprising: (a) withdrawing said interfacial cuff emulsion from said separating zone; (b) recycling a major portion of said withdrawn cuff emulsion back to said separating zone; (c) treating the remaining portion of said withdrawn cuff emulsion with a diluent oil having a higher API gravity than that of the oil in said cuff emulsion, whereby said cuff emulsion is broken to form an oil phase and a water phase containing solids; and (d) recovering said oil phase step (c).

Claim 3

The process of claim 1 in which the oil in the oil water mixture is a salty crude oil containing water insoluble solids.

Claim 4

The process of claim 2 in which the diluent oil is a petroleum fraction boiling between about 150° and about 625° F.

Claim 5

The process of claim 3 in which the diluent oil is a petroleum naphtha.

Claim 6

The process of claim 3 in which the diluent oil is kerosene.

Claim 7

The process of claim 5 in which a chemical demulsifying agent is added prior to mixing the interfacial cuff emulsion with the diluent oil.

Claim 8

In the desalting of salty crude oil containing water-insoluble solids in which the crude oil is mixed with between about one and about fifteen percent by volume water, the resulting mixture is introduced to a separating zone where it separates into an upper oil phase, a lower water phase, and an interfacial cuff emulsion containing water-insoluble solids, and in which oil and water are withdrawn from the oil phase and water phase respectively, the improvement comprising: (a) withdrawing said interfacial cuff emulsion; (b) combining a major portion of said withdrawn cuff emulsion with said salty crude oil prior to mixing said salty crude oil with water; (c) mixing the remaining portion of said withdrawn cuff emulsion with a diluent oil having an API gravity greater than that of said salty crude oil whereby said remaining portion of said cuff emulsion is separated into an oil phase and a water phase containing water-insoluble solids; and (d) recovering the oil phase from step (c).

Claim 9

In the desalting of salty crude oil containing water-insoluble solids in which the crude oil is mixed with between about one and about fifteen percent by volume water, the resulting mixture is introduced to a separating zone where it separates into an upper oil phase, a lower water phase, and an interfacial cuff emulsion containing water-insoluble solids, and in which oil and water are withdrawn from the oil phase and water phase respectively, the improvement comprising: (a) withdrawing said interfacial cuff emulsion; (b) combining a major portion of said withdrawn cuff emulsion with said salty crude oil prior to mixing said salty crude oil with water; (c) mixing the remaining portion of said withdrawn cuff emulsion with a diluent oil having an API gravity greater than that of said salty crude oil whereby said remaining portion of said cuff emulsion is separated into an oil phase and a water phase containing water-insoluble solids; and (d) recovering the oil phase from step (c).

Claim 10

The process of claim 7 in which separation of the salty crude oil-water mixture is effected by coalescing the water electrically.

Claim 11

The process of claim 8 in which a chemical demulsifying agent is used to aid in the separation of the salty crude oil-water mixture.

Claim 12

The process of claim 8 in which the diluent oil is a petroleum naphtha.

Claim 13

The process of claim 8 in which the diluent oil is kerosene.

Claim 14

The process of claim 11 in which a chemical demulsifying agent is used to aid in the separation of the interfacial cuff emulsion into oil and water phases.

Claim 15

The process of claim 12 in which the amount of diluent oil is between about 3 and about 10 times the volume of the interfacial cuff emulsion.

Claim 16

The process of claim 13 in which separation of the interfacial cuff emulsion into oil and water phases is effected in a settling zone.

Claim 17

The process of claim 14 in which separation of the interfacial cuff emulsion into oil and water phases is effected in a series of settling zones.

Claim 18

A process for recovering oil from an oil-water mixture containing water-insoluble solids comprising: (a) introducing said mixture into a first separation zone to form an upper oil phase, a lower water phase and an interfacial cuff emulsion containing water-insoluble solids; (b) withdrawing water from said first separation zone; (c) withdrawing oil and said interfacial cuff emulsion together from said first separation zone and introducing said withdrawn oil and cuff emulsion into a second separation zone where said oil and said cuff emulsion collect as separate phases; (d) withdrawing oil from said second separation zone; (e) withdrawing cuff emulsion from said second separation zone; (f) returning a major portion of said cuff emulsion from step (e) to the oil used to form said oil-water mixture; (g) mixing the remaining portion of said cuff emulsion with a diluent oil having an API gravity higher than that of said oil in said oil-water mixture to break said cuff emulsion and to form an oil phase and a water phase containing accumulated solids; and (h) recovering said oil phase from step (g).

Claim 19

A process for recovering oil from an oil-water mixture containing water-insoluble solids comprising: (a) introducing said mixture into a first separation zone to form an upper oil phase, a lower water phase and an interfacial cuff emulsion containing water-insoluble solids; (b) withdrawing water from said first separation zone; (c) withdrawing oil and said interfacial cuff emulsion together from said first separation zone and introducing said withdrawn oil and cuff emulsion into a second separation zone where said oil and said cuff emulsion collect as separate phases; (d) withdrawing oil from said second separation zone; (e) withdrawing cuff emulsion from said second separation zone; (f) returning a major portion of said cuff emulsion from step (e) to the oil used to form said oil-water mixture; (g) mixing the remaining portion of said cuff emulsion with a diluent oil having an API gravity higher than that of said oil in said oil-water mixture to break said cuff emulsion and to form an oil phase and a water phase containing accumulated solids; and (h) recovering said oil phase from step (g).

Claim 20

The process of claim 16 in which the oil in the oil water mixture is a salty crude oil containing water insoluble solids.

Claim 21

The process of claim 17 in which the diluent oil is a petroleum fraction boiling between about 150° and about 625° F.

Claim 22

The process of claim 18 in which the diluent oil is a petroleum naphtha.

Claim 23

The process of claim 18 in which the diluent oil is kerosene.

Claim 24

The process of claim 20 in which a chemical demulsifying agent is added prior to mixing the interfacial cuff emulsion with the diluent oil.