CA2195604C - Slurrying oil sand for hydrotransport in a pipeline - Google Patents
Slurrying oil sand for hydrotransport in a pipelineInfo
- Publication number
- CA2195604C CA2195604C CA002195604A CA2195604A CA2195604C CA 2195604 C CA2195604 C CA 2195604C CA 002195604 A CA002195604 A CA 002195604A CA 2195604 A CA2195604 A CA 2195604A CA 2195604 C CA2195604 C CA 2195604C
- Authority
- CA
- Canada
- Prior art keywords
- slurry
- oil sand
- stream
- water
- produce
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
A mixer circuit, in the form of a vertically oriented stack of components, functions to slurry oil sand with water in preparation for pumping through a pipeline.
The oil sand is initially dropped from the end of a conveyor. It is contacted in mid-air with a stream of water to distribute the water through the oil sand and to wet the latter.
The mixture drops into a downwardly slanted trough. The water and oil sand mix as they move turbulently through the open-ended trough. The slurry is deflected as it leaves the trough and is spread in the form of a thin sheet on an apron. It is then fed over screens to reject oversize lumps. The screened slurry drops into a pump box.
The rejected lumps are comminuted in an impactor positioned at the end of the screens. The comminuted oil sand is screened to remove remaining oversize lumps and the screened comminuted oil sands are delivered into the pump box. The structure is compact and the oversize reject loss is relatively low.
The oil sand is initially dropped from the end of a conveyor. It is contacted in mid-air with a stream of water to distribute the water through the oil sand and to wet the latter.
The mixture drops into a downwardly slanted trough. The water and oil sand mix as they move turbulently through the open-ended trough. The slurry is deflected as it leaves the trough and is spread in the form of a thin sheet on an apron. It is then fed over screens to reject oversize lumps. The screened slurry drops into a pump box.
The rejected lumps are comminuted in an impactor positioned at the end of the screens. The comminuted oil sand is screened to remove remaining oversize lumps and the screened comminuted oil sands are delivered into the pump box. The structure is compact and the oversize reject loss is relatively low.
Description
~ 2195604 FIELD OF THE INVENTION
2 This invention relates to a process and mixer circuit for mixing oil sand 3 with water to produce a slurry which can be pumped through a pipeline.
BACKGROUND OF THE INVENTION
6 The McMurray oil sands of Alberta constitute one of the largest deposits 7 of hydrocarbons in the world.
8 At the presenl time, there are two very large scale plants extracting 9 bitumen (a heavy and viscous oil) from these oil sands. Each of these plants incorporates a sequence of mining, bitumen extraction and bitumen upgrading 1 1 operations.
12 For many years, the as-mined oil sand was moved by conveyor belt13 assemblies from the mine site to the extraction plant.
14 In recent years, slurry pipelines have begun to replace the conveyor belt 1 5 systems.
16 In connection therewith, one needs to provide suitable means for17 slurrying the oil sand with water and entrained air, to produce a slurry that is suitable 18 for pumping down the pipeline.
19 The mixer circuit so provided is required to cope with very large volumes of throughput - typically 10,000 tons of oil sand per hour. The oil sand is highly 21 erosive, so the mixer circuit should have minimal moving parts and be very durable.
22 In addition, the as-mined oil sand contains a variety of lumps including rocks, clay 23 lumps, and oil sand lumps. The concentration of lumps is greater in winter, when 24 some of the oil sand reports in the form of frozen chunks. Usually the as-mined oil sand will have passed through a double roll crusher prior to slurrying, to reduce lump ~_ 21 95604 size below 24 inches. However, the crushed oil sand still contains oversize lumps 2 which are unsuitable for pumping and feeding into the pipeline. Therefore the mixer 3 circuit requires some means for rejecting the oversize lumps (otherwise referred to 4 herein as "oversize").
In United States patent No. 5039227, issued to Leung et al and 6 assigned to the owners of the present application, one mixer circuit for this purpose 7 has been rlisclosed.
8 In the Leung et al mixer circuit, an oil sand stream is dropped from the 9 end of a conveyor into a mixer tank. The mixer tank is open-topped, has a cylindrical 10 body and conical bottom and forms a central bottom outlet. A swirling vortex of slurry 11 is maintained in the tank and the incoming oil sand is fed into it. Slurry leaves the tank 12 through the bottom outlet, is screened using vibrating screens to reject oversize, and 13 is temporarily collected in an underlying pump box. Some of the slurry in the pump 14 box is withdrawn and pumped back through a return line to be introduced tangentially into the mixer tank to form the swirling vortex. The balance of slurry in the pump box 16 is withdrawn and pumped into the pipeline.
17 The Leung et al mixer circuit has been successfully applied on a 18 commercial scale. However, it is characterized by certain shortcomings.
19 One problem has to do with the fact that a large proportion of the 20 produced slurry has to be pumped back into the mixer tank to maintain the vortex. As 21 a result, the slurry volume that undergoes screening is about twice the volume 22 pumped into the pipeline. This requires provision of a very large screen area. The 23 screens are necessarily located in confined quarters. As a result, one cannot increase 24 the throughput of the circuit because the screens constitute a bottleneck that is not easily resolved.
Another problem lies in the oversize reject rate. At present the screens 2 reject lumps having a diameter greater than 2 inches. About 10% of the oil sand feed 3 is so rejected. These rejects represent a significant oil loss. To reduce this loss, the 4 rejects are conveyed to a second mixer circuit and are re-processed. This is expensive 5 to implement.
BACKGROUND OF THE INVENTION
6 The McMurray oil sands of Alberta constitute one of the largest deposits 7 of hydrocarbons in the world.
8 At the presenl time, there are two very large scale plants extracting 9 bitumen (a heavy and viscous oil) from these oil sands. Each of these plants incorporates a sequence of mining, bitumen extraction and bitumen upgrading 1 1 operations.
12 For many years, the as-mined oil sand was moved by conveyor belt13 assemblies from the mine site to the extraction plant.
14 In recent years, slurry pipelines have begun to replace the conveyor belt 1 5 systems.
16 In connection therewith, one needs to provide suitable means for17 slurrying the oil sand with water and entrained air, to produce a slurry that is suitable 18 for pumping down the pipeline.
19 The mixer circuit so provided is required to cope with very large volumes of throughput - typically 10,000 tons of oil sand per hour. The oil sand is highly 21 erosive, so the mixer circuit should have minimal moving parts and be very durable.
22 In addition, the as-mined oil sand contains a variety of lumps including rocks, clay 23 lumps, and oil sand lumps. The concentration of lumps is greater in winter, when 24 some of the oil sand reports in the form of frozen chunks. Usually the as-mined oil sand will have passed through a double roll crusher prior to slurrying, to reduce lump ~_ 21 95604 size below 24 inches. However, the crushed oil sand still contains oversize lumps 2 which are unsuitable for pumping and feeding into the pipeline. Therefore the mixer 3 circuit requires some means for rejecting the oversize lumps (otherwise referred to 4 herein as "oversize").
In United States patent No. 5039227, issued to Leung et al and 6 assigned to the owners of the present application, one mixer circuit for this purpose 7 has been rlisclosed.
8 In the Leung et al mixer circuit, an oil sand stream is dropped from the 9 end of a conveyor into a mixer tank. The mixer tank is open-topped, has a cylindrical 10 body and conical bottom and forms a central bottom outlet. A swirling vortex of slurry 11 is maintained in the tank and the incoming oil sand is fed into it. Slurry leaves the tank 12 through the bottom outlet, is screened using vibrating screens to reject oversize, and 13 is temporarily collected in an underlying pump box. Some of the slurry in the pump 14 box is withdrawn and pumped back through a return line to be introduced tangentially into the mixer tank to form the swirling vortex. The balance of slurry in the pump box 16 is withdrawn and pumped into the pipeline.
17 The Leung et al mixer circuit has been successfully applied on a 18 commercial scale. However, it is characterized by certain shortcomings.
19 One problem has to do with the fact that a large proportion of the 20 produced slurry has to be pumped back into the mixer tank to maintain the vortex. As 21 a result, the slurry volume that undergoes screening is about twice the volume 22 pumped into the pipeline. This requires provision of a very large screen area. The 23 screens are necessarily located in confined quarters. As a result, one cannot increase 24 the throughput of the circuit because the screens constitute a bottleneck that is not easily resolved.
Another problem lies in the oversize reject rate. At present the screens 2 reject lumps having a diameter greater than 2 inches. About 10% of the oil sand feed 3 is so rejected. These rejects represent a significant oil loss. To reduce this loss, the 4 rejects are conveyed to a second mixer circuit and are re-processed. This is expensive 5 to implement.
6 From the foregoing, it is apparent that there is a need for a mixer circuit 7 which operales without slurry recycle and which has improved reject rates.
8 It is the purpose of the present invention to provide such a mixer circuit.
SUMMARY OF THE INVENTION
11 In a preferred form of the invention, we have provided a stack of 12 vertically oriented components which convey the oil sand and water downwardly along 13 a generally zig-zag path, comprising:
14 ~ A conveyor having a discharge end for delivering a continuous stream of oil sand that falls through air into a trough;
16 ~ A pipe for delivering a stream of water which contacts and wets 17 the falling oil sand in mid-air;
18 ~ The trough being downwardly slanted, open-topped and 19 positioned in spaced relation below the conveyor discharge end and the water pipe. The trough is operative to receive the 21 mixture of oil sand and water and confine it temporarily to allow 22 the oil sand and water to turbulently mix and form a slurry stream 23 as they flow along its length and discharge from its open lower 24 end;
~ An upstanding wall positioned adjacent the trough's lower end 2 and spaced therefrom so that the slurry stream hits it and is 3 deflected, with the result that its direction of flow is changed and 4 further mixing is induced;
~ An apron providing a broad surface for receiving the deflected 6 stream, whereby the stream is spread out and thinned to form a 7 slurry sheet adapted to efficiently utilize the screen area;
8 ~ A first screen assembly for receiving and screening the slurry 9 sheet to reject oversize and produce a screened slurry stream;
and 11 ~ A pump box for collecting the screened slurry stream and feeding 12 a pump to deliver the slurry into the pipeline.
13 This assembly has successfully been tested to demonstrate:
14 ~ that a slurry suitable for pipeline conveyance can be formed using only the amount of water required for hydrotransport in the 16 pipeline; and 17 ~ that the screen area required for each unit volume of oil sand 18 treated is reduced in comparison to our prior art system.
19 It has been found that the water needs to contact the curtain of falling 20 oil sand in mid-air. If the water is added at the trough, it has a tendency to channel 21 through the oil sand and mixing is inadequate. The oil sand then does not flow easily 22 along the trough. It has been found that contacting the oil sand in mid-air with water 23 yields good distribution of the water in the oil sand and produces a slurry that flows 24 easily on contacting the trough surface.
-In a prefer,ed extension of the invention, the rejected oversize lumps 2 from the first screen assembly are fed directly into an impactor and co",r,linuted. The 3 comminuted product is screened by a second screen assembly to reject any remaining 4 oversize. The comminuted, screened product is then delivered into the same pump 5 box which receives the screened slurry from the first screen assembly.
6 As a result of combining components in this way, the following 7 improvements have been achieved:
8 ~ the vertical stacking of the components yields a structure that is 9 compact relative to the prior assembly amd relies on gravity to ",obili~e the oil sand and water;
11 ~ the need for recycling slurry has been eliminated, with the result 12 that screen loading is decreased; and 13 ~ reject rates have been reduced below 3%.
14 Broadly stated, in one aspect the invention comprises a process for 15 slurrying oil sand, containing oversize lumps, with water to produce a slurry and 16 removing oversize lumps from the slurry to produce slurry suitable for pumping through 17 a pipeline, comprising: dloppi.1g the oil sand through air from the discharge end of a 18 conveyor onto a downwardly slanted surface spaced below the conveyor discharge 19 end; contacting the oil sand with a stream of water as the oil sand moves through the 20 air between the conveyor discharge end and the surface, to wet the oil sand; mixing 21 the oil sand and water as they move together along the surface, to form a slurry 22 stream; discharging the slurry stream onto first screen means and screening it to reject 23 oversize lumps; and directing the screened slurry into a pump box prior to pumping it 24 into a pipeline.
Broadly stated, in another aspect the invention comprises an assembly 2 of vertically oriented components for slurrying oil sand, containing oversize lumps, with 3 water to produce a slurry and removing oversize lumps from the slurry to produce 4 slurry suitable for pumping through a pipeline, comprising: conveyor means, having a discharge end, for delivering and dropping a stream of oil sand; a downwardly 6 slanted surface positioned in spaced relation below the conveyor means discharge end, 7 so that the oil sand drops thereon; means for delivering a stream of water so that it 8 contacts and wets the oil sand as it drops bel-veen the conveyor means discharge end 9 and the support surface; whereby the oil sand and water may mix as they move along the surface and form a slurry stream; first screen means for screening the slurry stream 11 to reject oversize lumps and produce screened slurry; and pump box means for 12 receiving the screened slurry.
Figure 1 is a schematic side view showing the preferred embodiment of 16 the invention.
19 As-mined oil sand to be pipelined is first crushed before conveying it to a mixer circuit 1. This is commonly done by passing it through a set of double rolls, 21 producing 24 inch product. This pre-treatment (which forms no part of the invention) 22 is done to break down the very large contained lumps.
23 The crushed oil sand contains lumps of varying size and con,posilion.
24 The mixer circuit 1 comprises a series of downwardly arranged components.
The uppermost component is a conveyor 2 for continuously delivering a 2 stream of crushed oil sand 3. The oil sand c~cc~des or falls from the discharge end 3 4 of the conveyor 2- it drops downwardly through an air space 5.
4 A horizontal pipe 6 is positioned opposite to the conveyor discharge end 4. The pipe discharges a stream 7 of water into the falling oil sand in mid-air at a 6 sufficient rate so that the water/oil sand ratio is equivalent to that of the pipeline slurry.
7 Typically this ratio is about 1:3 by weight. The stream 7 contacts the downwardly 8 descending oil sand is distributed through it and wets it.
9 The oil sand and water drop into a downwardly slanted, open-topped, open-ended trough 8. The trough is formed of plate steel.
11 AS the oil sand and water move through the trough, they mix turbulently 12 and form a slurry.
13 A solid, vertical wall 10 formed of steel is positioned adjacent the lower 14 end 11 of the trough 8. The wall 10 is spaced from the trough's lower end 11 and extends across the trajectory path of the slurry stream 13 discharging from the trough.
16 A downwardly slanted apron 14 extends downwardly from the wall 10 in 17 a direction opposile to that of the trough 8.
18 The slurry stream 13 hits the wall 10, is deflected and changes its 19 direction of movement, being discharged onto an apron 14 having solid and then apertured portions. In the course of these movements, further turbulent mixing of the 21 oil sand and water occurs. On reaching the apron, the slurry spreads out laterally and 22 is thinned, to form a slurry sheet 15. Some slurry drops through the apertures into the 23 pump box 18.
24 The slurry sheet 15 flows from the apron 14 onto a contiguous first vibrating screen 16. It is sized to retain +4 inch material.
~ 1 9~604 The slurry 17 passing through the screen drops into a pump box 18.
2 Here the slurry is collected and temporarily retained before being pumped from an 3 outlet into a pipeline (not shown).
4 The oversize lumps 20 retained by the vibrating screen 16 are delivered into an impactor 24. The lumps 20 are largely oil sand in composition and many 6 disinlegrale when impacted by the rotating arms of the impactor, producing 7 comminuted product 27. This product discharges from the outlet of the impactor onto 8 a second vibrating screen 30. The screened comminuted product is discharged 9 through hopper 31 into pump box 18. The oversize lumps retained by the screen 30 are discarded.
SUMMARY OF THE INVENTION
11 In a preferred form of the invention, we have provided a stack of 12 vertically oriented components which convey the oil sand and water downwardly along 13 a generally zig-zag path, comprising:
14 ~ A conveyor having a discharge end for delivering a continuous stream of oil sand that falls through air into a trough;
16 ~ A pipe for delivering a stream of water which contacts and wets 17 the falling oil sand in mid-air;
18 ~ The trough being downwardly slanted, open-topped and 19 positioned in spaced relation below the conveyor discharge end and the water pipe. The trough is operative to receive the 21 mixture of oil sand and water and confine it temporarily to allow 22 the oil sand and water to turbulently mix and form a slurry stream 23 as they flow along its length and discharge from its open lower 24 end;
~ An upstanding wall positioned adjacent the trough's lower end 2 and spaced therefrom so that the slurry stream hits it and is 3 deflected, with the result that its direction of flow is changed and 4 further mixing is induced;
~ An apron providing a broad surface for receiving the deflected 6 stream, whereby the stream is spread out and thinned to form a 7 slurry sheet adapted to efficiently utilize the screen area;
8 ~ A first screen assembly for receiving and screening the slurry 9 sheet to reject oversize and produce a screened slurry stream;
and 11 ~ A pump box for collecting the screened slurry stream and feeding 12 a pump to deliver the slurry into the pipeline.
13 This assembly has successfully been tested to demonstrate:
14 ~ that a slurry suitable for pipeline conveyance can be formed using only the amount of water required for hydrotransport in the 16 pipeline; and 17 ~ that the screen area required for each unit volume of oil sand 18 treated is reduced in comparison to our prior art system.
19 It has been found that the water needs to contact the curtain of falling 20 oil sand in mid-air. If the water is added at the trough, it has a tendency to channel 21 through the oil sand and mixing is inadequate. The oil sand then does not flow easily 22 along the trough. It has been found that contacting the oil sand in mid-air with water 23 yields good distribution of the water in the oil sand and produces a slurry that flows 24 easily on contacting the trough surface.
-In a prefer,ed extension of the invention, the rejected oversize lumps 2 from the first screen assembly are fed directly into an impactor and co",r,linuted. The 3 comminuted product is screened by a second screen assembly to reject any remaining 4 oversize. The comminuted, screened product is then delivered into the same pump 5 box which receives the screened slurry from the first screen assembly.
6 As a result of combining components in this way, the following 7 improvements have been achieved:
8 ~ the vertical stacking of the components yields a structure that is 9 compact relative to the prior assembly amd relies on gravity to ",obili~e the oil sand and water;
11 ~ the need for recycling slurry has been eliminated, with the result 12 that screen loading is decreased; and 13 ~ reject rates have been reduced below 3%.
14 Broadly stated, in one aspect the invention comprises a process for 15 slurrying oil sand, containing oversize lumps, with water to produce a slurry and 16 removing oversize lumps from the slurry to produce slurry suitable for pumping through 17 a pipeline, comprising: dloppi.1g the oil sand through air from the discharge end of a 18 conveyor onto a downwardly slanted surface spaced below the conveyor discharge 19 end; contacting the oil sand with a stream of water as the oil sand moves through the 20 air between the conveyor discharge end and the surface, to wet the oil sand; mixing 21 the oil sand and water as they move together along the surface, to form a slurry 22 stream; discharging the slurry stream onto first screen means and screening it to reject 23 oversize lumps; and directing the screened slurry into a pump box prior to pumping it 24 into a pipeline.
Broadly stated, in another aspect the invention comprises an assembly 2 of vertically oriented components for slurrying oil sand, containing oversize lumps, with 3 water to produce a slurry and removing oversize lumps from the slurry to produce 4 slurry suitable for pumping through a pipeline, comprising: conveyor means, having a discharge end, for delivering and dropping a stream of oil sand; a downwardly 6 slanted surface positioned in spaced relation below the conveyor means discharge end, 7 so that the oil sand drops thereon; means for delivering a stream of water so that it 8 contacts and wets the oil sand as it drops bel-veen the conveyor means discharge end 9 and the support surface; whereby the oil sand and water may mix as they move along the surface and form a slurry stream; first screen means for screening the slurry stream 11 to reject oversize lumps and produce screened slurry; and pump box means for 12 receiving the screened slurry.
Figure 1 is a schematic side view showing the preferred embodiment of 16 the invention.
19 As-mined oil sand to be pipelined is first crushed before conveying it to a mixer circuit 1. This is commonly done by passing it through a set of double rolls, 21 producing 24 inch product. This pre-treatment (which forms no part of the invention) 22 is done to break down the very large contained lumps.
23 The crushed oil sand contains lumps of varying size and con,posilion.
24 The mixer circuit 1 comprises a series of downwardly arranged components.
The uppermost component is a conveyor 2 for continuously delivering a 2 stream of crushed oil sand 3. The oil sand c~cc~des or falls from the discharge end 3 4 of the conveyor 2- it drops downwardly through an air space 5.
4 A horizontal pipe 6 is positioned opposite to the conveyor discharge end 4. The pipe discharges a stream 7 of water into the falling oil sand in mid-air at a 6 sufficient rate so that the water/oil sand ratio is equivalent to that of the pipeline slurry.
7 Typically this ratio is about 1:3 by weight. The stream 7 contacts the downwardly 8 descending oil sand is distributed through it and wets it.
9 The oil sand and water drop into a downwardly slanted, open-topped, open-ended trough 8. The trough is formed of plate steel.
11 AS the oil sand and water move through the trough, they mix turbulently 12 and form a slurry.
13 A solid, vertical wall 10 formed of steel is positioned adjacent the lower 14 end 11 of the trough 8. The wall 10 is spaced from the trough's lower end 11 and extends across the trajectory path of the slurry stream 13 discharging from the trough.
16 A downwardly slanted apron 14 extends downwardly from the wall 10 in 17 a direction opposile to that of the trough 8.
18 The slurry stream 13 hits the wall 10, is deflected and changes its 19 direction of movement, being discharged onto an apron 14 having solid and then apertured portions. In the course of these movements, further turbulent mixing of the 21 oil sand and water occurs. On reaching the apron, the slurry spreads out laterally and 22 is thinned, to form a slurry sheet 15. Some slurry drops through the apertures into the 23 pump box 18.
24 The slurry sheet 15 flows from the apron 14 onto a contiguous first vibrating screen 16. It is sized to retain +4 inch material.
~ 1 9~604 The slurry 17 passing through the screen drops into a pump box 18.
2 Here the slurry is collected and temporarily retained before being pumped from an 3 outlet into a pipeline (not shown).
4 The oversize lumps 20 retained by the vibrating screen 16 are delivered into an impactor 24. The lumps 20 are largely oil sand in composition and many 6 disinlegrale when impacted by the rotating arms of the impactor, producing 7 comminuted product 27. This product discharges from the outlet of the impactor onto 8 a second vibrating screen 30. The screened comminuted product is discharged 9 through hopper 31 into pump box 18. The oversize lumps retained by the screen 30 are discarded.
Claims (9)
1. A process for slurrying oil sand, containing oversize lumps, with water to produce a slurry and removing oversize lumps from eth slurry to produce slurry suitable for pumping through a pipeline, comprising:
dropping the oil sand through air from the discharge end of a conveyor onto a downwardly slanted surface spaced below the conveyor discharge end;
contacting the oil sand with a stream of water as the oil sand moves through the air between the conveyor discharge end and the surface, to wet the oil sand;
mixing the oil sand and water as they move together along the surface, to form a slurry stream;
discharging the slurry stream onto first screen means and screening it to reject oversize lumps; and directing the screened slurry into a pump box prior to pumping it into a pipeline.
dropping the oil sand through air from the discharge end of a conveyor onto a downwardly slanted surface spaced below the conveyor discharge end;
contacting the oil sand with a stream of water as the oil sand moves through the air between the conveyor discharge end and the surface, to wet the oil sand;
mixing the oil sand and water as they move together along the surface, to form a slurry stream;
discharging the slurry stream onto first screen means and screening it to reject oversize lumps; and directing the screened slurry into a pump box prior to pumping it into a pipeline.
2. The process as set forth in claim 1 wherein:
the initial portion of the downwardly slanted surface is provided by an open-topped trough having a discharge outlet at its lower end.
the initial portion of the downwardly slanted surface is provided by an open-topped trough having a discharge outlet at its lower end.
3. The process as set forth in claim 2 comprising:
discharging the slurry stream from the trough and deflecting the stream with upstanding wall means to change its direction of flow and induce further mixing of the slurry; and spreading the deflected slurry stream over a downwardly slanted apron extending from the wall means, to establish a sheet of slurry which is discharged onto the first screen means.
discharging the slurry stream from the trough and deflecting the stream with upstanding wall means to change its direction of flow and induce further mixing of the slurry; and spreading the deflected slurry stream over a downwardly slanted apron extending from the wall means, to establish a sheet of slurry which is discharged onto the first screen means.
4. The process as set forth in claims 1, 2 or 3 comprising comminuting rejected oversize lumps discharged from the first screen means, to produce comminuted product;
and discharging the comminuted product into the pump box.
and discharging the comminuted product into the pump box.
5. The process as set forth in claims 1, 2 or 3 comprising:
comminuting rejected oversize lumps discharged from the first screen means, to produce comminuted product associated with residual oversize lumps;
screening the comminuted product to reject residual oversize lumps; and discharging the comminuted product into the pump box.
comminuting rejected oversize lumps discharged from the first screen means, to produce comminuted product associated with residual oversize lumps;
screening the comminuted product to reject residual oversize lumps; and discharging the comminuted product into the pump box.
6. An assembly of vertically oriented components for slurrying oil sand, containing oversize lumps, with water to produce a slurry and removing oversize lumps from the slurry to produce slurry suitable for pumping through a pipeline, comprising:
conveyor means, having a discharge end, for delivering and dropping a stream of oil sand;
a downwardly slanted surface positioned in spaced relation below the conveyor means discharge end, so that the oil sand drops thereon;
means for delivering a stream of water so that it contacts and wets the oil sand as it drops between the conveyor means discharge end and the support surface;
whereby the oil sand and water may mix as they move along the surface and form a slurry stream;
first screen means for screening the slurry stream to reject oversize lumps and produce screened slurry; and pump box means for receiving the screened slurry.
conveyor means, having a discharge end, for delivering and dropping a stream of oil sand;
a downwardly slanted surface positioned in spaced relation below the conveyor means discharge end, so that the oil sand drops thereon;
means for delivering a stream of water so that it contacts and wets the oil sand as it drops between the conveyor means discharge end and the support surface;
whereby the oil sand and water may mix as they move along the surface and form a slurry stream;
first screen means for screening the slurry stream to reject oversize lumps and produce screened slurry; and pump box means for receiving the screened slurry.
7. The assembly as set forth in claim 6 comprising:
means for comminuting the rejected oversize lumps as they leave the first screen means to produce comminuted product; and means for transferring the comminuted product into the pump box means.
means for comminuting the rejected oversize lumps as they leave the first screen means to produce comminuted product; and means for transferring the comminuted product into the pump box means.
8. The assembly as set forth in claim 7 comprising:
second screen means for screening the comminuted product to reject residual oversize lumps before the comminuted product is transferred into the pump box means.
second screen means for screening the comminuted product to reject residual oversize lumps before the comminuted product is transferred into the pump box means.
9. An assembly of vertically oriented components for slurrying oil sand, containing oversize lumps, with water to produce a slurry and removing oversize lumps from the slurry to produce slurry suitable for pumping through a pipeline, comprising:
conveyor means, having a discharge end, for delivering and dropping a stream of oil sand;
a downwardly slanted, open-topped trough having a discharge opening at its lower end, said trough being positioned in spaced relation below the conveyor means discharge end, so that the oil sand drops therein;
means for delivering a stream of water so that it contacts and wets the oil sand as it drops between the conveyor means discharge end and the trough;
whereby the oil sand and water may mix as they move through the trough and form a slurry stream discharging from its lower end;
wall means, spaced from the trough's lower end, for deflecting the slurry stream and changing its direction of flow and spreading the stream to form a sheet of slurry;
first screen means for screening the slurry stream to reject oversize lumps and produce screened slurry;
pump box means for receiving the screened slurry;
means for comminuting the rejected oversize lumps as they leave the first screen means to produce comminuted product;
second screen means for screening the comminuted product to reject uncomminuted oversize lumps and produce screened comminuted product; and means for transferring the screened comminuted product into the pump box means.
conveyor means, having a discharge end, for delivering and dropping a stream of oil sand;
a downwardly slanted, open-topped trough having a discharge opening at its lower end, said trough being positioned in spaced relation below the conveyor means discharge end, so that the oil sand drops therein;
means for delivering a stream of water so that it contacts and wets the oil sand as it drops between the conveyor means discharge end and the trough;
whereby the oil sand and water may mix as they move through the trough and form a slurry stream discharging from its lower end;
wall means, spaced from the trough's lower end, for deflecting the slurry stream and changing its direction of flow and spreading the stream to form a sheet of slurry;
first screen means for screening the slurry stream to reject oversize lumps and produce screened slurry;
pump box means for receiving the screened slurry;
means for comminuting the rejected oversize lumps as they leave the first screen means to produce comminuted product;
second screen means for screening the comminuted product to reject uncomminuted oversize lumps and produce screened comminuted product; and means for transferring the screened comminuted product into the pump box means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002195604A CA2195604C (en) | 1997-01-21 | 1997-01-21 | Slurrying oil sand for hydrotransport in a pipeline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002195604A CA2195604C (en) | 1997-01-21 | 1997-01-21 | Slurrying oil sand for hydrotransport in a pipeline |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2195604A1 CA2195604A1 (en) | 1998-07-21 |
| CA2195604C true CA2195604C (en) | 1999-11-23 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002195604A Expired - Lifetime CA2195604C (en) | 1997-01-21 | 1997-01-21 | Slurrying oil sand for hydrotransport in a pipeline |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2195604C (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7677397B2 (en) | 2004-07-30 | 2010-03-16 | Suncor Energy Inc. | Sizing roller screen ore processing apparatus |
| US8025341B2 (en) | 2005-11-09 | 2011-09-27 | Suncor Energy Inc. | Mobile oil sands mining system |
| US8328126B2 (en) | 2008-09-18 | 2012-12-11 | Suncor Energy, Inc. | Method and apparatus for processing an ore feed |
| US8393561B2 (en) | 2005-11-09 | 2013-03-12 | Suncor Energy Inc. | Method and apparatus for creating a slurry |
| US9016799B2 (en) | 2005-11-09 | 2015-04-28 | Suncor Energy, Inc. | Mobile oil sands mining system |
| US9207019B2 (en) | 2011-04-15 | 2015-12-08 | Fort Hills Energy L.P. | Heat recovery for bitumen froth treatment plant integration with sealed closed-loop cooling circuit |
| US9546323B2 (en) | 2011-01-27 | 2017-01-17 | Fort Hills Energy L.P. | Process for integration of paraffinic froth treatment hub and a bitumen ore mining and extraction facility |
| US9587176B2 (en) | 2011-02-25 | 2017-03-07 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
| US9676684B2 (en) | 2011-03-01 | 2017-06-13 | Fort Hills Energy L.P. | Process and unit for solvent recovery from solvent diluted tailings derived from bitumen froth treatment |
| US9791170B2 (en) | 2011-03-22 | 2017-10-17 | Fort Hills Energy L.P. | Process for direct steam injection heating of oil sands slurry streams such as bitumen froth |
| US10041005B2 (en) | 2011-03-04 | 2018-08-07 | Fort Hills Energy L.P. | Process and system for solvent addition to bitumen froth |
| US10226717B2 (en) | 2011-04-28 | 2019-03-12 | Fort Hills Energy L.P. | Method of recovering solvent from tailings by flashing under choked flow conditions |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA3036668C (en) | 2004-01-08 | 2021-07-06 | Fort Hills Energy L.P. | Paraffinic froth treatment techniques |
| US8535485B2 (en) | 2004-09-02 | 2013-09-17 | Syncrude Canada Ltd. | Apparatus and process for wet crushing oil sand |
| US7431830B2 (en) | 2004-09-02 | 2008-10-07 | Canadian Oil Sands Limited Partnership | Compact slurry preparation system for oil sand |
| US8062511B2 (en) | 2008-06-27 | 2011-11-22 | Syncrude Canada Ltd. | Primary froth recycle |
| CA2812125A1 (en) | 2009-07-24 | 2011-01-24 | Suncor Energy Inc. | Screening disk, roller, and roller screen for screening an ore feed |
| CA2832269C (en) | 2011-05-18 | 2017-10-17 | Fort Hills Energy L.P. | Temperature control of bitumen froth treatment process with trim heating of solvent streams |
-
1997
- 1997-01-21 CA CA002195604A patent/CA2195604C/en not_active Expired - Lifetime
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8851293B2 (en) | 2004-07-30 | 2014-10-07 | Suncor Energy, Inc. | Sizing roller screen ore processing apparatus |
| US8136672B2 (en) | 2004-07-30 | 2012-03-20 | Suncor Energy, Inc. | Sizing roller screen ore processing apparatus |
| US7677397B2 (en) | 2004-07-30 | 2010-03-16 | Suncor Energy Inc. | Sizing roller screen ore processing apparatus |
| US8025341B2 (en) | 2005-11-09 | 2011-09-27 | Suncor Energy Inc. | Mobile oil sands mining system |
| US8393561B2 (en) | 2005-11-09 | 2013-03-12 | Suncor Energy Inc. | Method and apparatus for creating a slurry |
| US9016799B2 (en) | 2005-11-09 | 2015-04-28 | Suncor Energy, Inc. | Mobile oil sands mining system |
| US8328126B2 (en) | 2008-09-18 | 2012-12-11 | Suncor Energy, Inc. | Method and apparatus for processing an ore feed |
| US8622326B2 (en) | 2008-09-18 | 2014-01-07 | Suncor Energy, Inc. | Method and apparatus for processing an ore feed |
| US9546323B2 (en) | 2011-01-27 | 2017-01-17 | Fort Hills Energy L.P. | Process for integration of paraffinic froth treatment hub and a bitumen ore mining and extraction facility |
| US10125325B2 (en) | 2011-02-25 | 2018-11-13 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
| US9587176B2 (en) | 2011-02-25 | 2017-03-07 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
| US9676684B2 (en) | 2011-03-01 | 2017-06-13 | Fort Hills Energy L.P. | Process and unit for solvent recovery from solvent diluted tailings derived from bitumen froth treatment |
| US10041005B2 (en) | 2011-03-04 | 2018-08-07 | Fort Hills Energy L.P. | Process and system for solvent addition to bitumen froth |
| US9791170B2 (en) | 2011-03-22 | 2017-10-17 | Fort Hills Energy L.P. | Process for direct steam injection heating of oil sands slurry streams such as bitumen froth |
| US9207019B2 (en) | 2011-04-15 | 2015-12-08 | Fort Hills Energy L.P. | Heat recovery for bitumen froth treatment plant integration with sealed closed-loop cooling circuit |
| US10226717B2 (en) | 2011-04-28 | 2019-03-12 | Fort Hills Energy L.P. | Method of recovering solvent from tailings by flashing under choked flow conditions |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2195604A1 (en) | 1998-07-21 |
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| EEER | Examination request | ||
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