# US 4,392,941 A · Recovery of bitumen from tar sands sludge using additional water

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- Number: US 4,392,941 A
- Document ID: US4392941A
- Status: Granted
- Kind: A
- Application number: 06/272,616
- Filed: 1981-06-11
- Granted: 1983-07-12
- Earliest claimed: 1980-07-28
- Assignees: Suncor, Inc.
- Inventors: Robert B. Roth; Walter H. Seitzer
- Web page: https://patentgrep.com/patent/US4392941A

## CPC

- C10G 1/047: {Hot water or cold water extraction processes}
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES

## Abstract

A method is disclosed for the recovery of bitumen from a sludge. The sludge is diluted with water and subjected to high-shear agitation and aeration and the sludge settled to obtain an upper bitumen-containing froth layer and a lower sludge layer of reduced bitumen content. The recovery of bitumen is increased over that obtained with aeration and mixing with mild agitation or with aeration alone or with agitation alone.

## Claims

### Claim 1

The method of recovering bitumen from a sludge obtained from a retention pond containing tailings from the water extraction of tar sands, which comprises diluting the sludge with water, wherein the dilution range is between about 1 part water to 10 parts sludge and about 2 parts water to one part sludge, subjecting the diluted sludge to high-shear agitation and aeration, wherein during the high-shear agitation the diluted sludge is experiencing a Reynolds Number in excess of 10,000 and settling the resulting sludge to obtain an upper bitumen-containing froth layer and a lower sludge layer reduced in bitumen content, whereby the recovery of bitumen is greater than that obtained with aeration and mixing with mild agitation or with aeration alone or with agitation alone.

### Claim 2 (depends on 1)

Method according to claim 1 wherein during the high-shear agitation and aeration an alkali metal silicate is present.

### Claim 3 (depends on 1)

Method according to claim 1 wherein during the high-shear agitation and aeration an additive selected from the group consisting of phosphates, creosotes, phenols, phenol derivatives, starches, modified starches, lignin sulfonates and polycarboxylates is present.