Sizing roller screen ore processing apparatus

Information

  • Patent Grant
  • 8851293
  • Patent Number
    8,851,293
  • Date Filed
    Friday, March 9, 2012
    12 years ago
  • Date Issued
    Tuesday, October 7, 2014
    9 years ago
Abstract
A mined ore processing apparatus to process mined ores, such as oil sands ore, into granular material is disclosed. An ore processor bed receives the ore to be processed. The ore processor bed has a frame supporting several rotating elements each separately driven to provide independent rotation rate and direction from the other. The ore processing bed is operable as a sizing device to decimate mined ore supply into granular material and separating it from rocks and other large lump mineral materials found in situ. The ore processing bed may be oriented to provide an upward inclination, which, when combined with alternating rotating element rotation directions, provides a crushing action to the ore material to crush larger rock. Alternately, a rock crusher is also provided to disintegrate oversized materials.
Description
BACKGROUND OF THE INVENTION

1. Field of the Invention


This invention relates to the processing of mined ore and more particularly relates to sizing and conditioning of mined ore materials.


2. Description of the Prior Art


Earth formations are mined to recover valuable minerals that are incorporated in the earthen formations or are covered by an earthen overburden. For example, Northern Alberta has oil sands formations that contain valuable bitumen hydrocarbons. Various techniques are in use or have been discussed for recovery of bitumen hydrocarbons from oil sands formations. In accordance with one method of recovery, the oil sands formations are mined to remove in situ bitumen bearing ore from the formation in which it is found. The removed oil sands ore is then processed to separate the hydrocarbons from the sand and mineral materials. Once separated, the hydrocarbons are then further processed into intermediate or finished products such as synthetic crude oil, fuels and the like.


When the mining method of extraction is employed, the oil sands ore extracted from the earth is transported to a processing facility where separation of the bitumen hydrocarbons from the other materials in the ore can take place. The mined oil sands ore is typically transported to processing facilities by truck or by slurry transport via a pipeline or by combinations of the two or by other mechanisms. Frequently, the oil sands ore is mined at a considerable distance from where the process of separating the oil sands into hydrocarbons, sand and minerals takes, place. Distance affects conditioning and recovery in hydrotransport systems, consequently, transport of the mined ore to a separation facility typically involves transporting the mined ore significant distances. Moreover, the location from which the ore is taken changes over time as the oil sands ore is depleted as a result of formation mining, consequently resulting in migration of the mining site along the formation. Because the location of the source of oil sands ore changes over time, the ore transport start point at the mining site must be mobile to permit the ore to begin transport from the source formation site as that changes over time.


One mechanism for transport of the ore to the separation facility is by forming the mined ore into a slurry. Suitable solvents, for example water, are mixed with the processed ore to form a slurry and the slurry produced is then transported to a separation processing facility over a pipeline. To prepare the ore for slurry transport, the mined ore is preferably comminuted into the smaller particle size to facilitate transport by slurry pumping. Furthermore, large rocks and other undesirable oversized solids are not candidate slurry components. In one manner of operation these oversized solids are removed or separated from the processed ore that is to be formed into a slurry. In another manner of operation these oversized solids are crushed and included with the processed ore that is to be formed into a slurry. Because the location where the ore is extracted from will change over time, it is preferable to have readily movable slurry equipment to reduce the need for long transport from the mining area to the slurry processing equipment.


SUMMARY OF THE INVENTION

The present invention provides a mined ore processing apparatus that is operable as a sizing device in either a wet or dry process that screens, sorts and comminutes mined ore into granular material separating it from rocks and other large lump mineral materials found in situ. The invention is also operable as a crusher sizing device that comminutes mined ore into granular material and crushes oversized rock and other large lump mineral materials found in situ into and included with the granular material produced from comminution of the ore.


Moreover, the processing apparatus of the present invention is adapted for use to process the produced granular material into a slurry composition for hydrotransport. In the preferred embodiment, the mined ore processing apparatus of the present invention is portable to facilitate moving it from one location to another. Preferably it is adapted to process high volumes of mined ore material in a compact portable facility.


In one of its aspects the invention provides an ore processor bed having an upper surface portion adapted to receive mined ore material to be processed. The ore processor bed has a frame supporting at least two spacedly disposed rotating elements. The mined ore material is placed on the processor bed where it contacts the rotating elements and is processed into granular material as it passes along the processor bed and through the spacing between the rotating elements of the processor bed. Each of the rotating elements is independently operated to rotate in a clockwise or counter clockwise direction and at independent rates. The processor bed is orientable with respect to horizontal to provide a horizontal surface or incline. In one configuration, the mined ore material is contacted with a solvent and supplied to the processor bed. The solvent assists in processing the mined, ore material into granular material and to aid in dust reduction during the process. The solvent may be heated. In another configuration, the mined ore feed material is premixed with a solvent such as water before it is supplied to the processor bed. There are also applications where dry feed is added to the apparatus to produce dry products, that is, no solvent, such as water, is added. In the preferred embodiment, the produced granular material is received in a hopper vessel where solvent such as water is added to form a slurry composition facilitating fluid or hydro transport of the granular material in slurry form.


The preferred embodiments of the invention will now be described with reference to the drawings.





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 is an elevation partial cross-section view of the preferred embodiment of the invention.



FIG. 2 is an elevation partial cross-section view of an alternate embodiment of the invention including a crusher.



FIG. 3 is an elevation partial cross-section view of an alternate embodiment of the invention providing a feed hopper.



FIG. 4 shows an elevation partial cross-section view of the embodiment of FIG. 1 but in operation without a processor bed solvent supply and with the processor bed oriented horizontally above the slurry vessel.



FIG. 5 shows an elevation partial cross-section view of the embodiment of FIG. 2 but in operation without a processor bed solvent supply, with the crusher disposed at the feed end of the processor bed and with the processor bed oriented horizontally above the slurry vessel.



FIG. 6 shows an elevation partial cross-section view of the embodiment of FIG. 5 but with the processor bed oriented at an upward incline above the slurry vessel.



FIGS. 7 and 7
a are plan views of the ore processor bed rotating elements rotatably disposed therein showing variations in spacings.



FIG. 8 is an elevation view showing various disk profiles of the rotating element disk assemblies.



FIG. 9 is an elevation view showing various disk profiles of the rotating element disk assemblies adapted for crushing rock.





DETAILED DESCRIPTION OF THE INVENTION AND PREFERRED EMBODIMENTS


FIG. 1 shows an elevation partial cross-section view of the preferred embodiment of a mined sand processing facility constructed in accordance with the principles of the invention. Mined ore 10 to be processed, for example oil sands ore, is supplied to a feed conveyor 12. The ore moves along feed conveyor 12 where it is delivered at 11 onto an upper portion surface of an ore processor bed 14. The ore processor bed 14 has plurality of rotating elements 16 in the form of inter-fitting rotating disk assemblies. Each of the rotating element disk assemblies has a plurality of disks fixed to a driven axle 18. In the operation of the apparatus shown in FIG. 1, each rotating element is operated to rotate in a clockwise direction causing the ore to move along the upper portion of the ore processor bed in a left to right direction. As the ore moves along the upper portion of the ore processor bed, the weight of the ore coming to rest on the disks of rotating disk assemblies causes the finer portions of the ore to separate and fall through the interstitial spaces of the rotating elements of the ore processor bed at 20 into the upper opening 21 of slurry vessel 22.


The ore passing over the upper surface portion of the ore processor bed is preferably contacted with a solvent supply 24, such as a water spray directed toward the ore, to assist in ore disintegration. Preferably, a heater 23 is provided to heat the solvent supply 24 causing heating of the ore to further assist in obtaining disintegration of the ore passing over the ore processor bed. Larger rock and other undesirable oversized materials 25 that are too voluminous to be processed in passage over the ore processor bed 14 are carried to a waste conveyor 26 for disposal. Within slurry vessel 22, the disintegrated ore 20 is mixed with a solvent 28, such as water, to form a slurry solution 30. A heater 27 may be provided to heat the solvent 28 and thus heat the slurry solution. In the preferred embodiment, the lower portion of the slurry vessel has a decreasing cross section relative to the cross section of the upper opening 21 of slurry vessel 22. The decreasing cross section of the slurry vessel permits the force of gravity to urge the slurry solution 30 toward a slurry feed outlet 34 as it passes through the slurry vessel 22. The slurry feed outlet 34 provides an egress path for removing slurry from the slurry vessel by pumping for delivery to a transport pipeline.



FIG. 2 shows an elevation partial cross-section view of an alternate embodiment of the invention. In the embodiment of FIG. 2, a crusher apparatus 29 is provided to crush the oversize material 25 received from the ore processor bed. The crushed material produced by the crusher is supplied to the slurry vessel 22 and becomes part of the solids included in the slurry solution 30.



FIG. 3 shows an elevation partial cross-section view of an alternative embodiment of the invention providing a feed hopper 19. In the configuration of FIG. 3, the mined ore 10 is supplied to a feed hopper 19 where it is contacted with a solvent supply 28, such as water. The solvent and ore intermingle during passage through feed hopper 19 and are discharged from the feed hopper onto the upper portion of an end of the processor bed 14.



FIG. 4 shows an elevation partial cross-section view of an alternative embodiment of the invention from that of FIG. 1, wherein the ore processor bed 14 is disposed horizontally above the upper opening 21 of the slurry vessel 22. In this configuration, the ore 10, for example oil sand ore, is passed across the ore processor bed and each of the rotating disk assemblies 16 can rotate in a clockwise or counterclockwise direction as shown by the double-headed arrows. Each rotating disk assembly has a separate drive means 36 as shown more clearly in FIG. 7 which controls the direction and speed of rotation of the coupled rotating disk assembly. The disk assembly drive means 36 is variable speed and reversible permitting the driven disk assembly to rotate in a clockwise or counterclockwise direction at a suitable rate of rotation. Moreover, in the embodiment of FIG. 4 it will be noted that there are no spray nozzles shown as the ore processing can occur with or without a solvent spray being applied to the ore depending on the type of ore that is being processed. In one manner of operation, alternating rotating disk assemblies are turned in opposite directions causing the disk assemblies to apply a pinching or crushing force to the ore to assist in comminution and disintegration of the ore as it passes over ore processor bed 14.



FIG. 5 shows an elevation partial cross-section view of an alternate embodiment of the invention from that depicted in FIG. 2. In the embodiment of FIG. 5, the crusher apparatus 29 is disposed to receive the feed ore and process that ore before delivery to the ore processor bed 14. With the process arrangement of FIG. 5, any oversize material 25 received is crushed before the ore is supplied to the ore processor bed 14.



FIG. 6 shows an alternate orientation of the ore processor bed 14 which is oriented to provide an upwardly inclined surface, or a negative declination angle, for the ore 10 that passes over the ore processor bed. Providing a negative declination angle assists the ore processor bed in effecting crushing of the ore, such as oil sands ore, particularly crushing of the oversized materials when the upwardly inclined surface is used in co-operation with alternating rotation directions of the rotating elements of the ore processor bed. Thus, the ore processor bed can be oriented above the slurry vessel at differing inclinations. The ore processor bed can be oriented to provide a downwardly inclined surface, that is a positive declination angle, as shown in FIGS. 1, 2 and 3; a horizontal surface, that is a declination angle of zero, as shown in FIGS. 4 and 5; or an upwardly inclined surface, that is a negative declination angle, as depicted in FIG. 6. Preferably the ore processor bed is configured to provide a declination angle in the preferred range of −30° to +30° relative to horizontal.



FIG. 7 is a top plan view of an ore processor bed 14 showing the rotating elements in more detail. The rotating elements are provided by an inter-fitting spacing of rotating disk assemblies 16 and each associated drive axle 18 relative to one another. In the preferred arrangement, each rotating disk assembly 16 and drive axle 18 has its own drive means 36. The drive means 36 is variable speed and reversible enabling each disk assembly to rotate in a clockwise or counterclockwise direction depending on the chosen manner of operation for the ore processor bed 14. A frame 38 to which the rotating disk assemblies 16/drive axles 18 are mounted for rotation using bearings 40 supports the rotating disk assemblies 16. FIG. 7a shows a variation in spacing of the processor bed rotating elements from the spacing of FIG. 7. In FIG. 7a, a reduced inter-fitting spacing of rotating disk assemblies 16 provides for decreasing sized material that will be provided from the ore processor bed.


Preferably where the embodiment of the invention provides a solvent supply, as depicted for example as spray 24 in FIGS. 1 and 2, at least some of the spray nozzles are directed toward processor bed 14 and are operated at sufficient pressure and velocity rates to provide a jet spray cleaning action to clean the rotating elements of material that may tend to clog the ore processor bed.



FIG. 8 shows a profile view of the rotating disk assemblies 16. They can be configured with various circumference profiles including a round profile 42 which is preferably provided with a roughened circumference to assist in transporting and contacting the oil sand ore along the peripheral circumference of the rotating disk assemblies 16. An alternate circular notch 44 may be spacedly disposed about the circumference of the rotating disk assembly or a toothed circumference 46 may be employed. An alternate sinusoidal circumference 48 may also be provided. As will be understood, it is not necessary for each of the rotating disk assemblies to bear the same profile as all the others. The disk assemblies can include different profiles to assist, in crushing the mined ore, and in ore comminution.



FIG. 9 is an elevation view showing various disk profiles of the rotating element disk assemblies adapted for crushing rock. The sizes of the rotating disks can also vary to allow different sizing and size reduction capabilities. This will create variations in the sizing apertures. Elongations 50 or kickers are preferably added to the profile to promote the removal of jammed material from between the disks. The elongations may include a deflection 52 to provide a hammer-like profile for the disks assemblies provided for rock crushing.


Now that the invention has been described numerous substitutions and modifications will occur to those skilled in the art. The invention is not limited to the specific embodiments described here with reference to the drawings but rather is defined in the claims appended hereto.

Claims
  • 1. A method of forming a slurry from an oil sand ore, the method comprising: contacting the oil sand ore with an ore processor bed having a frame supporting a plurality of spaced apart rotatable elements disposed over an upper opening of a slurry vessel, the ore processor bed operative to comminute the oil sand ore and to produce a granular material while screening and sorting the oil sand ore from an oversize material unsuitable for slurry formation in the slurry vessel, the plurality of spaced apart rotatable elements comprising at least four rotatable elements, the frame comprising an elongated upper portion of the ore processor bed formed at least in part by the plurality of spaced apart rotatable elements;spraying a solvent over and along the elongated upper portion of the ore processor bed while transporting the oil sand ore by the plurality of spaced apart rotatable elements to comminute the oil sand ore and to produce the granular material while screening and sorting the oil sand ore from oversize material;allowing the granular material to fall through interstitial spaces of the plurality of spaced apart rotatable elements into the slurry vessel; anddelivering water into the slurry vessel such that the water contacts the granular material to form the slurry.
  • 2. The method as claimed in claim 1 further comprising rotating at least one rotatable element at a rotational speed different than a rotational speed of at least one other rotatable element, in a direction opposite to other rotatable elements.
  • 3. The method as claimed in claim 1 further comprising contacting the oil sand ore with the solvent before the oil sand ore contacts the frame.
  • 4. The method as claimed in claim 1 wherein spraying further comprises spraying the solvent towards a substantial portion of the ore processor bed as the oil sand ore is transported and comminuted by at least part of the plurality of spaced apart rotatable elements from a front end of the ore processor bed to towards a back end of the ore processor bed.
  • 5. The method as claimed in claim 1 wherein spraying comprises spraying the solvent over substantially all of the elongated upper portion of the ore processor bed as the oil sand ore is transported and comminuted by the at least part of the plurality of spaced apart rotatable elements from a front region of the ore processor bed towards a back region of the ore processor bed.
  • 6. The method as claimed in claim 1 wherein each of the plurality of spaced apart rotatable elements comprises a shaft and a plurality of disks coupled to the shaft, the method further comprising arranging the disks of at least one shaft to inter-fit with the disks of an adjacent shaft.
  • 7. The method as claimed in claim 1 wherein spraying comprises spraying the solvent over substantially all of the elongated upper portion of the ore processor bed as the oil sand ore is transported and comminuted by the rotatable elements from a front region of the ore processor bed towards a back region of the ore processor bed in a direction generally perpendicular to the shafts of the rotatable elements.
  • 8. The method as claimed in claim 1 further comprising inclining the ore processor bed.
  • 9. The method as claimed in claim 1 further comprising orienting the ore processor bed at an incline of between about minus 30 degrees and about plus 30 degrees relative to horizontal.
  • 10. A method of forming a slurry from an ore, the method comprising: feeding the ore to an ore processor bed having a frame supporting a plurality of spaced apart rotatable elements disposed over an upper opening of a slurry vessel, the ore processor bed operative to comminute the ore and to produce a granular material while screening and sorting the ore from an oversize material unsuitable for slurry formation in the slurry vessel, the plurality of spaced apart rotatable elements comprising at least four rotatable elements, the frame comprising an elongated upper portion of the ore processor bed formed at least in part by the plurality of spaced apart rotatable elements;contacting the ore with a solvent;processing the ore with the ore processor bed;allowing the granular material to fall through interstitial spaces of the plurality of spaced apart rotatable elements into the slurry vessel; anddelivering water into the slurry vessel such that the water contacts the granular material to form the slurry.
  • 11. The method as claimed in claim 10 wherein contacting the ore with the solvent further comprises contacting the ore with the solvent as the ore is fed to the ore processor bed causing the ore and solvent to intermingle before the ore contacts the ore processor bed.
  • 12. The method as claimed in claim 10 further comprising: supplying the ore to a feed hopper wherein the ore contacts the solvent causing the solvent and ore to intermingle; anddischarging the solvent and ore upon the elongated upper portion of the ore processor bed.
  • 13. The method as claimed in claim 10 further comprising contacting the ore with the solvent before the ore contacts the frame.
  • 14. The method as claimed in claim 10 further wherein contacting the ore with the solvent further comprises spraying the solvent over and along the elongated upper portion of the ore processor bed while transporting the ore by the plurality of spaced apart rotatable elements to comminute the ore and to produce the granular material and while screening and sorting the ore from oversize material.
  • 15. The method as claimed in claim 14 wherein spraying further comprises spraying the solvent towards a substantial portion of the ore processor bed as the ore is transported and comminuted by at least part of the plurality of spaced apart rotatable elements from a front end of the ore processor bed to towards a back end of the ore processor bed.
  • 16. The method as claimed in claim 14 wherein spraying comprises spraying the solvent over substantially all of the elongated upper portion of the ore processor bed as the ore is transported and comminuted by the at least part of the plurality of spaced apart rotatable elements from a front region of the ore processor bed towards a back region of the ore processor bed.
  • 17. The method as claimed in claim 14 wherein spraying comprises spraying the solvent over substantially all of the elongated upper portion of the ore processor bed as the ore is transported and comminuted by the rotatable elements from a front region of the ore processor bed towards a back region of the ore processor bed in a direction generally perpendicular to the shafts of the rotatable elements.
  • 18. The method as claimed in claim 14 wherein each of the plurality of spaced apart rotatable elements comprises a shaft and a plurality of disks coupled to the shaft, the method further comprising arranging the disks of at least one shaft to inter-fit with the disks of an adjacent shaft.
  • 19. The method as claimed in claim 10 further comprising rotating at least one rotatable element at a rotational speed different than a rotational speed of at least one other rotatable element, in a direction opposite to other rotatable elements.
  • 20. The method as claimed in claim 10 further comprising inclining the ore processor bed.
  • 21. The method as claimed in claim 10 further comprising orienting the ore processor bed at an incline of between about minus 30 degrees and about plus 30 degrees relative to horizontal.
Priority Claims (1)
Number Date Country Kind
2476194 Jul 2004 CA national
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a division of U.S. patent application Ser. No. 12/646,842, filed Dec. 23, 2009, to be issued as U.S. Pat. No. 8,136,672, which is a continuation of then U.S. patent application Ser. No. 11/187,977, filed Jul. 25, 2005, now U.S. Pat. No. 7,677,397. The contents of all documents listed in this paragraph are hereby incorporated by reference in their entirety.

US Referenced Citations (109)
Number Name Date Kind
183114 Blake Oct 1876 A
528974 Pike Nov 1894 A
670312 Cressonnieres Mar 1901 A
816763 Trask Apr 1906 A
1277344 McCargar Aug 1918 A
1930247 McCormick Oct 1933 A
2606861 Eastwood Aug 1952 A
2674564 Hermanson Apr 1954 A
2894824 Lanning Jul 1959 A
3159562 Bichard et al. Dec 1964 A
3161483 Morris Dec 1964 A
3260548 Reichl Jul 1966 A
3392105 Poettmann et al. Jul 1968 A
3402896 Daman Sep 1968 A
3509641 Smith et al. May 1970 A
3524597 Burden, Jr. et al. Aug 1970 A
3581875 Guis Jun 1971 A
3933651 Erskine Jan 1976 A
3941425 Reichl Mar 1976 A
3972861 Gardner, Jr. et al. Aug 1976 A
3998702 Opoku Dec 1976 A
4029568 Pittman et al. Jun 1977 A
4103972 Kochanowsky Aug 1978 A
4120776 Miller et al. Oct 1978 A
4139646 Gastrock Feb 1979 A
4244165 McElwain Jan 1981 A
4424113 Mitchell Jan 1984 A
4486294 Miller et al. Dec 1984 A
4505516 Shelton Mar 1985 A
4505811 Griffiths et al. Mar 1985 A
4512956 Robinson et al. Apr 1985 A
4538734 Gill Sep 1985 A
4549935 Tchernyak Oct 1985 A
4585180 Potts Apr 1986 A
4658964 Williams Apr 1987 A
4733828 Potts Mar 1988 A
4741444 Bielagus May 1988 A
4763845 Guggenheimer Aug 1988 A
4781331 Potts Nov 1988 A
4795036 Williams Jan 1989 A
4799627 Potts Jan 1989 A
4851123 Mishra Jul 1989 A
4994097 Brouwers Feb 1991 A
5039227 Leung et al. Aug 1991 A
5117983 Marrs Jun 1992 A
5124008 Rendall et al. Jun 1992 A
5143598 Graham et al. Sep 1992 A
5161744 Schoop et al. Nov 1992 A
5186820 Schultz et al. Feb 1993 A
5242580 Sury Sep 1993 A
5257699 Fricker et al. Nov 1993 A
5264118 Cymerman et al. Nov 1993 A
5362000 Schwelling Nov 1994 A
5441206 Schade et al. Aug 1995 A
5450966 Clark et al. Sep 1995 A
5480566 Strand Jan 1996 A
5503712 Brown Apr 1996 A
5589599 McMullen et al. Dec 1996 A
5645714 Strand et al. Jul 1997 A
5723042 Strand et al. Mar 1998 A
5772127 Maciejewski et al. Jun 1998 A
5954277 Maciejewski et al. Sep 1999 A
5960964 Austin et al. Oct 1999 A
6033187 Addie Mar 2000 A
6065607 Magnusson et al. May 2000 A
6076753 Maciejewski Jun 2000 A
6250476 Kroon et al. Jun 2001 B1
6318560 Davis Nov 2001 B2
6319099 Tanoue et al. Nov 2001 B1
6322845 Dunlow Nov 2001 B1
6371305 Austin et al. Apr 2002 B1
6390915 Brantley et al. May 2002 B2
6450775 Hutchinson et al. Sep 2002 B1
6460706 Davis Oct 2002 B1
6517733 Carlson Feb 2003 B1
6521079 Roy Feb 2003 B1
6585560 Tanoue et al. Jul 2003 B2
6648145 Davis et al. Nov 2003 B2
6800116 Stevens et al. Oct 2004 B2
6818058 Ronin Nov 2004 B2
6821060 McTurk et al. Nov 2004 B2
7008966 Degeorge et al. Mar 2006 B2
7013937 Potts Mar 2006 B2
7111738 Allen Sep 2006 B2
7207504 Willmot Apr 2007 B2
7399406 Mikula et al. Jul 2008 B2
7556715 Gaston et al. Jul 2009 B2
7588206 Hausman et al. Sep 2009 B2
7893378 Kenny Feb 2011 B2
20020018842 Dunlow Feb 2002 A1
20030089644 Hanks May 2003 A1
20040251731 Potts Dec 2004 A1
20040262980 Watson Dec 2004 A1
20050051500 Price et al. Mar 2005 A1
20050134102 Cymerman et al. Jun 2005 A1
20050161372 Colic Jul 2005 A1
20050173726 Potts Aug 2005 A1
20060091249 Potts May 2006 A1
20060226054 Bishop, Jr. Oct 2006 A1
20070014905 Chen et al. Jan 2007 A1
20070095032 Nilsen et al. May 2007 A1
20070180741 Bjornson et al. Aug 2007 A1
20070180951 Armstrong et al. Aug 2007 A1
20080047198 Mehlhose et al. Feb 2008 A1
20080121493 Bjornson et al. May 2008 A1
20080173572 Bjornson et al. Jul 2008 A1
20080197056 Kenny Aug 2008 A1
20100155305 Bjornson et al. Jun 2010 A1
20100181394 Bruggencate Jul 2010 A1
Foreign Referenced Citations (103)
Number Date Country
857305 Jan 1970 CA
841581 Dec 1970 CA
890903 Jan 1972 CA
917585 Dec 1972 CA
918588 Jan 1973 CA
922655 Mar 1973 CA
997300 Sep 1976 CA
1085762 Sep 1980 CA
1088883 Nov 1980 CA
1106789 Aug 1981 CA
1117353 Feb 1982 CA
1126187 Jun 1982 CA
1132511 Sep 1982 CA
1137906 Dec 1982 CA
1153347 Sep 1983 CA
1163257 Mar 1984 CA
1193586 Sep 1985 CA
1214421 Nov 1986 CA
1231692 Jan 1988 CA
1266261 Feb 1990 CA
1309050 Oct 1992 CA
2116243 Mar 1993 CA
2000984 Nov 1994 CA
2029795 Nov 1996 CA
2105176 May 1997 CA
2164925 Jun 1997 CA
2088227 Feb 1998 CA
2294860 Jun 1998 CA
2195604 Jan 1999 CA
2217623 Apr 1999 CA
2220821 May 1999 CA
2227667 Jul 1999 CA
2084375 Jul 2002 CA
2235938 Apr 2003 CA
2249679 Apr 2003 CA
2250623 Apr 2003 CA
2254048 May 2003 CA
2290029 Aug 2003 CA
2294860 Sep 2003 CA
2332207 Feb 2004 CA
2352274 Feb 2004 CA
2358805 Feb 2004 CA
2436818 Feb 2004 CA
2398026 Mar 2004 CA
2453697 Apr 2004 CA
2441969 May 2004 CA
2440311 Mar 2005 CA
2440312 Mar 2005 CA
2476194 Jan 2006 CA
2480122 Mar 2006 CA
2486137 Mar 2006 CA
2498862 Apr 2006 CA
2506398 May 2006 CA
2518040 May 2006 CA
2520821 May 2006 CA
2520943 May 2006 CA
2522514 May 2006 CA
2526336 May 2006 CA
2548370 Jun 2006 CA
2548371 Jun 2006 CA
2549895 Jun 2006 CA
2552031 Jun 2006 CA
2554725 Jun 2006 CA
2558059 Aug 2006 CA
2499840 Sep 2006 CA
2499846 Sep 2006 CA
2469326 May 2007 CA
2567643 May 2007 CA
2567644 May 2007 CA
2610124 May 2008 CA
2610169 May 2008 CA
2834987 Feb 1980 DE
3936681 May 1990 DE
0167178 Apr 1990 EP
0493858 Jun 1995 EP
2185027 May 1973 FR
1437605 Jun 1976 GB
2010777 Jul 1979 GB
04019331 Jan 2005 GB
04068029 Jan 2005 GB
005096492 Apr 1993 JP
8300318 Feb 1983 WO
8302071 Jun 1983 WO
8303062 Sep 1983 WO
8303444 Oct 1983 WO
8801201 Feb 1988 WO
9629149 Sep 1996 WO
9630629 Oct 1996 WO
9858739 Dec 1998 WO
9954049 Oct 1999 WO
0010896 Mar 2000 WO
0035585 Jun 2000 WO
0292231 Nov 2002 WO
0306165 Jan 2003 WO
03056134 Jul 2003 WO
03074394 Sep 2003 WO
2004005673 Jan 2004 WO
2004094061 Nov 2004 WO
2005000454 Jan 2005 WO
2005046874 May 2005 WO
2005046875 May 2005 WO
2005072877 Aug 2005 WO
2006035209 Apr 2006 WO
Non-Patent Literature Citations (32)
Entry
Keller et al.; “A Unique, Reagent-Based, Seperation Method for Tar Sands and Environmentallly Clean Ups”; Presented to AIChE 2001 Annual Meeting, Nov. 6, 2001, Reno, Nevada.
“The Fine Tailings Fundamentals Consortium”; Advances in Oil Sands Tailings Research, ISBN 0-7732-1691-X, Published by Alberta Department of Energy, Jun. 1995.
Stausz et al.; “The Chemistry of Alberta Oil Sands, Bitumens and Heavy Oils—Chapter 4—Composition and Structure of Alberta Oil Sands Carbonates”; Alberta Energy Research Institute, 2003, pp. 29-67.
Restriction Requirement dated Dec. 12, 2008 for U.S. Appl. No. 11/595,817.
Office Action dated May 23, 2008 for U.S. Appl. No. 11/595,817.
Office Action dated Mar. 2, 2009 for U.S. Appl. No. 11/595,817.
Restriction Requirement dated Dec. 2, 2008 for U.S. Appl. No. 11/558,340.
Office Action dated Apr. 29, 2009 for U.S. Appl. No. 11/558,340.
Restriction Requirement dated Aug. 28, 2008 for U.S. Appl. No. 11/558,303.
Office Action dated Jul. 21, 2009 for U.S. Appl. No. 11/595,817.
Natural Resources Canada, Treatment of Bitumen Froth and Oil Tailings, downloaded from www.nrcan.gc.ca/es/etb/cwrc/english/ast/researchareas/frothandslop/frothandslop.htm on Dec. 5, 2001.
National Energy Board, Canada's Oil Sands: A Supply and Market Outlook to 2015; An Energy Market Assessment, Oct. 2000.
Office Action dated Nov. 12, 2008 for U.S. Appl. No. 11/558,303.
Office Action dated Apr. 13, 2007 for CA Patent Application No. 2476194.
Office Action dated Jul. 29, 2008 for CA Patent Application No. 2476194.
Office Action dated Jun. 2, 2009 for CA Patent Application No. 2476194.
Printed publication namely Screen-printed (5 pages) electronic brochure from the website of Roxon Equipment. Date display “Jan. 27, 2004” (brochure screen printed Jan. 27, 2004) along with 23 screen-printed pages from the web site for www.roxongroup.com archived by the Web Archive (http://web.archive.org).
Office Action dated Jan. 26, 2007 for U.S. Appl. No. 10/825,230.
Office Action dated Oct. 3, 2007 for U.S. Appl. No. 10/825,230.
Office Action dated Jun. 20, 2008 for U.S. Appl. No. 10/825,230.
Notice of Allowability dated May 8, 2009 for U.S. Appl. No. 10/825,230.
Rimmer et al.; “Hydrocyclone-based Process for Rejecting Solids from Oil Sands at the Mine Site While Retaining Bitumen for Transportation to a Processing Plant”; Suncor Extraction 3rd edition, pp. 93-100, paper delivered on Monday Apr. 5, 1993 at a conference in Alberta, Canada entitled “Oil Petroleum Future”.
Excerpts from “Information Package for Mobile Crushing Plants (MCP)”, Krupp Canada, 1177 11 Ave. S.W., Suite #405, Calgary, Alberta, pp. 1-7 published Sep. 2004, Canada, pp. 8-46 published May 2003.
Protest to CA 2358805 Application filed Apr. 15, 2002, 217 pages.
“Oil Sands, Our Petroleum Future”; conference held at Edmonton Convention Centre, Edmonton, Alberta, Canada, Apr. 4-7, 1993.
Harding, John; “Cost-Saving Moves into High Gear” article in Financial Post, Apr. 4, 2006.
Johan, Ken; “Syncrude's Mine Production Planning”, Mine Planning and Equipment, Singhal (ed.), pp. 443-456, 1988, Balkema, Rottendam, ISBN 90 8191 8197.
Doucet et al.; “Drilling and Blasting in Tarsand”, Suncor Oil Sands Group, Nov. 7-8, 1985.
De Malherbe et al.; “Synthetic Crude from Oil Sands”; VDI-Verlag GmbH, Dusseldolf, 1983, vol. 3, No. 8, pp. 20-21.
Coward, Julian; seminar material used as class handout, University of Alberta, Mar. 20, 2000.
Restriction Requirement dated Aug. 4, 2011 for U.S. Appl. No. 12/562,785.
Office Action dated Oct. 21, 2011 for U.S. Appl. No. 12/562,785.
Related Publications (1)
Number Date Country
20120168542 A1 Jul 2012 US
Divisions (1)
Number Date Country
Parent 12646842 Dec 2009 US
Child 13416757 US
Continuations (1)
Number Date Country
Parent 11187977 Jul 2005 US
Child 12646842 US