Treatment of heterogeneous liquid materials

Claim 2

A continuous process for the treatment of a feed stream of heterogeneous liquid material in the form of a heavy hydrocarbon-water dispersion or dispersions, in which process the feed is diluted with a hydrocarbon solvent, water and solids are removed from the diluted feed stream in a single stage by contacting the feed stream with a stream of water in a contactor in which the two streams move in discrete adjacent, continuous phases and in which water from the water phase is repeatedly showered through the feed phase and feed from the feed phase is repeatedly showered through the water phase, and a product stream containing the hydrocarbon and a discard stream comprising water and solids are separately removed from the contactor at separate discharge points.

Claim 3

A process according to claim 1, in which the feed material is a bitumen froth obtained from tar sand or from other hydrocarbon impregnated material.

Claim 4

A process according to claim 2, in which the quantity of solvent added to the bitumen froth is such that the specific gravity of the diluted froth in the product stream is less than 0.94.

Claim 5

A process according to claim 2, in which the flow rate of the water stream is in the ratio of 0.25 to 1.0 (on weight basis) to that of the diluted froth.

Claim 6

A process according to claim 2, in which the temperature of the treatment within the contactor is between 50° C. and 100° C.

Claim 7

A process according to claim 2, in which the water content of the bitumen froth is reduced to 5 to 20 weight percent of the bitumen content of the product stream.

Claim 8

A process according to claim 2, in which the solids content of bitumen froth is reduced to 0.5 to 2 weight percent of the bitumen content of the product stream.

Claim 9

A process according to claim 2, in which the contactor is of the low-speed rotary tape, having series of buckets which rotate to disperse the bitumen froth in the water stream and shower water from the water stream into the bitumen froth.

Claim 10

A process according to claim 1, in which a de-emulsifier is added to the feed before its contact with water and/or at one or more points during the treatment in the contactor.

Claim 11

A process according to claim 9, in which the amount of de-emulsifier added is in the range of 10 to 2,000 ppm.

Claim 12

A continuous process for the treatment of a feed stream of heterogeneous liquid material in the form of a heavy hydrocarbon-water dispersion or dispersions including fine solids, the process comprising: (a) diluting said feed stream with a hydrocarbon solvent and thereby forming a diluted stream having a specific gravity below the specific gravity of water; (b) contacting said diluted stream in a contactor with a water stream, the flow rate of which is in the ratio of 0.25 to 1.0 (on a weight ratio) to the flow rate of said feed stream; (c) said diluted and water streams passing through said contactor in discrete adjacent, continuous phases; (d) during the passage of said streams through said contactor, repeatedly showering said water from said water stream through said diluted stream and hydrocarbon from said diluted stream through said water stream whereby water and solids dispersed in said diluted stream are captured by said water stream; and (e) separately removing from said contactor at separate discharge points a product stream containing said diluted stream having a reduced water and solids content and a discard stream comprising water and solids.

Claim 13

A continuous process for the treatment of a feed stream of heterogeneous liquid material in the form of a heavy hydrocarbon-water dispersion or dispersions including fine solids, the process comprising: (a) diluting said feed stream with a hydrocarbon solvent and thereby forming a diluted stream having a specific gravity below the specific gravity of water; (b) contacting said diluted stream in a contactor with a water stream, the flow rate of which is in the ratio of 0.25 to 1.0 (on a weight ratio) to the flow rate of said feed stream; (c) said diluted and water streams passing through said contactor in discrete adjacent, continuous phases; (d) during the passage of said streams through said contactor, repeatedly showering said water from said water stream through said diluted stream and hydrocarbon from said diluted stream through said water stream whereby water and solids dispersed in said diluted stream are captured by said water stream; and (e) separately removing from said contactor at separate discharge points a product stream containing said diluted stream having a reduced water and solids content and a discard stream comprising water and solids.

Claim 14

A continuous process for the treatment of a feed of oil and water emulsion containing water in a ratio to oil ranging from 50 to 100% by weight and solids in a ratio to oil ranging from 6 to 20% by weight, and process comprising: (a) diluting said emulsion with a light hydrocarbon in an amount to bring the specific gravity of said feed to the range of 0.85 to 0.94 and the viscosity of said feed to less than 50 centipoises at an operating temperature of 50° to 100° C., (b) adding to said diluted feed with 10 to 2000 ppm of a demulsifier, and (c) contacting said diluted and demulsified feed in a contactor of the low-speed rotary type provided with buckets with a water stream, the ratio of said water to said diluted and demulsified feed being between 0.25 and 1.0 by weight, and in which said diluted and demulsified feed and said water move in discrete adjacent, continuous phases and in which water from the water phase is repeatedly showered through the feed phase and feed from the feed phase is repeatedly showered through the water phase, (d) whereby the water content in the treated feed is reduced to 5 to 20% and the solids content to 0.5 to 2% by weight of said emulsion feed.

Claim 15

A continuous process for the treatment of a feed of oil and water emulsion containing water in a ratio to oil ranging from 50 to 100% by weight and solids in a ratio to oil ranging from 6 to 20% by weight, and process comprising: (a) diluting said emulsion with a light hydrocarbon in an amount to bring the specific gravity of said feed to the range of 0.85 to 0.94 and the viscosity of said feed to less than 50 centipoises at an operating temperature of 50° to 100° C., (b) adding to said diluted feed with 10 to 2000 ppm of a demulsifier, and (c) contacting said diluted and demulsified feed in a contactor of the low-speed rotary type provided with buckets with a water stream, the ratio of said water to said diluted and demulsified feed being between 0.25 and 1.0 by weight, and in which said diluted and demulsified feed and said water move in discrete adjacent, continuous phases and in which water from the water phase is repeatedly showered through the feed phase and feed from the feed phase is repeatedly showered through the water phase, (d) whereby the water content in the treated feed is reduced to 5 to 20% and the solids content to 0.5 to 2% by weight of said emulsion feed.