Apparatus for processing bituminous froth

Claim 3

An improved hot water extraction separation cell suitable for use in recovering bitumen from tar sands comprising: a. a tank having a bottom with an exit means therein; b. an inlet means in the side of said tank for feeding tar sands to the tank; c. an overflow launder positioned adjacent to the wall of said tank at the upper end thereof, said launder having a bottom disposed at an angle in the range of about 5° to 45° from the horizontal plane, said bottom having an outlet at the lowest point thereof and containing a plurality of steam inlet means disposed along the bottom of said launder for providing steam into said launder and containing a plurality of deflecting baffles disposed at intermittent intervals along the bottom of said launder, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said launder.

Claim 4

An improved hot water extraction separation cell suitable for use in recovering bitumen from tar sands comprising: a. a tank having a bottom with an exit means therein; b. an inlet means in the side of said tank for feeding tar sands to the tank; c. an overflow launder positioned adjacent to the wall of said tank at the upper end thereof, said launder having a bottom disposed at an angle in the range of about 5° to 45° from the horizontal plane, said bottom having an outlet at the lowest point thereof and containing a plurality of steam inlet means disposed along the bottom of said launder for providing steam into said launder and containing a plurality of deflecting baffles disposed at intermittent intervals along the bottom of said launder, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said launder.

Claim 5

In a system for extracting bitumen from tar sands by the hot water process, said system including: a. a primary separation cell for separating the bitumen from the sand wherein the bitumen floats to the upper liquid level in the cell in the form of a froth; b. overflow launder means adjacent the top of the separation cell for receiving the bitumen froth; c. means for further separating the bitumen from other impurities in the bitumen froth; and d. conduit means for providing fluid communication between overflow launder means and the means for further separating the bitumen; an improvement for deaerating the bitumen froth so that its fluid flow and pumping characteristics are improved, said improvement comprising: e. means for deflecting the flow of bitumen froth before it flows into the means for further separating the bitumen, so that the length of the flow path of bitumen froth is increased, and the flow directions are intermittently changed; and f. means, located in conjunction with the deflecting means, for injecting steam into the flow of bitumen froth.

Claim 6

In a system for extracting bitumen from tar sands by the hot water process, said system including: a. a primary separation cell for separating the bitumen from the sand wherein the bitumen floats to the upper liquid level in the cell in the form of a froth; b. overflow launder means adjacent the top of the separation cell for receiving the bitumen froth; c. means for further separating the bitumen from other impurities in the bitumen froth; and d. conduit means for providing fluid communication between overflow launder means and the means for further separating the bitumen; an improvement for deaerating the bitumen froth so that its fluid flow and pumping characteristics are improved, said improvement comprising: e. means for deflecting the flow of bitumen froth before it flows into the means for further separating the bitumen, so that the length of the flow path of bitumen froth is increased, and the flow directions are intermittently changed; and f. means, located in conjunction with the deflecting means, for injecting steam into the flow of bitumen froth.

Claim 7

The improvement recited in claim 3, wherein the overflow launder has a bottom disposed at an angle and an outlet connected to the conduit means at the lowermost portion of the bottom, and wherein the conduit means slopes downward from the outlet in the overflow launder, and wherein the deflecting means is located both in the overflow launder and the conduit means.

Claim 8

The improvement recited in claim 4, wherein the deflecting means located in the overflow launder comprises a plurality of baffles, disposed at intermittent points along at least part of the angled bottom of the overflow launder, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said overflow launder, thereby providing a continuous channel for bitumen froth to flow through which is longer than, and generally along the length of, the deflecting means in the launder, and wherein the deflecting means located in the conduit means comprises a plurality of baffles, disposed at intermittent points along at least part of the bottom of the conduit means, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said conduit means, thereby providing a continuous channel for bitumen froth to flow through, which is longer than, and generally along the length of, the deflecting means in the conduit means.

Claim 9

The improvement recited in claim 3, wherein the conduit means slopes downward from the overflow launder and wherein the deflecting means is located in the conduit means, so that the bitumen froth flowing from the overflow launder is subjected to the deflecting means and the steam injecting means to be deaerated and heated before it reaches the means for further separation of the bitumen.

Claim 10

The improvement recited in claim 6, wherein the deflecting means comprises a plurality of baffles, disposed at intermittent points along at least part of the bottom of the conduit means, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said conduit means, thereby providing a continuous channel for bitumen froth to flow through, which is longer than, and generally along the length of, the deflecting means in the conduit.

Claim 11

The improvement recited in claim 7, wherein the steam injection means comprises a plurality of steam outlet means located along the bottom of the conduit means.

Claim 12

The improvement recited in claim 3, wherein the overflow launder has a bottom surface disposed at an angle and an outlet connected to the conduit means at the lowermost point of the bottom of the launder, and wherein the deflecting means is located on the angled bottom of the overflow launder, so that the bitumen froth from the primary separation cell is subjected to the deflecting means and the steam injecting means to be deaerated and heated before it reaches the conduit means.

Claim 13

The improvement recited in claim 9, wherein the deflecting means comprises a plurality of baffles, disposed at intermittent points along at least part of the angled bottom of the overflow launder, each baffle being in contact with and extending over less than the whole of the width of the upper surface of the bottom of said overflow launder, thereby providing a continuous channel for bitumen froth to flow through which is longer than, and generally along the length of, the deflecting means in the launder.

Claim 14

The improvement recited in claim 10, wherein the steam injection means comprises a plurality of steam outlet means located along the bottom of overflow launder.