US2014044967A1PendingUtilityA1

System for processing and producing an aggregate

Assignee: AYERS REBECCAPriority: Jun 29, 2012Filed: Mar 15, 2013Published: Feb 13, 2014
Est. expiryJun 29, 2032(~5.9 yrs left)· nominal 20-yr term from priority
Inventors:Rebecca Ayers
Y10T428/2982B07B 13/11E21B 43/04E21B 43/267C09K 8/80E02D 3/12B07B 13/003
45
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Claims

Abstract

An aggregate processing assembly is provided. The processing assembly includes a separator assembly having a central member extending from a first end to a second end, the central member supporting at least one helical flight provided between the first and second ends, the helical flight having a width provided between a proximal end and a distal end. An assembly housing is provided around a portion of the separator assembly, the assembly housing includes a collection portion for receiving processed feed stock which exits the separator assembly radially away from the central member outward past the distal end, and the collection portion includes a first outlet. A second outlet is coupled to the separator assembly for receiving processed feed stock which exits the separator assembly at the second end of the at least one helical flight. A proppant, an aggregate, a system for processing feed stock to produce a proppant or aggregate, and a method of producing a proppant or aggregate is also provided.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A proppant resulting from a separator means comprising a plurality of particles, the particles have an average Krumbein and Sloss Sphericity Value of 0.6 or above, and an average Krumbein and Sloss Roundness Value of 0.6 or above. 
     
     
         2 . The proppant of  claim 1 , wherein the particles have an average Krumbein and Sloss Sphericity Value of 0.8 or above, and an average Krumbein and Sloss Roundness Value of 0.8 or above. 
     
     
         3 . The proppant of  claim 1 , wherein the particles have an average Krumbein and Sloss Sphericity Value of between 0.8 and 0.9, and an average Krumbein and Sloss Roundness Value of between 0.8 and 0.9. 
     
     
         4 . The proppant of  claim 1 , wherein the particles have an average Krumbein and Sloss Sphericity Value of at least 0.9, and an average Krumbein and Sloss Roundness Value of at least 0.9. 
     
     
         5 . The proppant of  claim 1 , wherein the particles include sand particles. 
     
     
         6 . The proppant of  claim 1 , wherein the particles include silica sand particles. 
     
     
         7 . The proppant of  claim 1 , wherein the proppant is greater than or equal to 0.1% by weight of a total weight of feed stock prior to processing by the separator means. 
     
     
         8 . The proppant of  claim 1 , wherein the proppant is greater than or equal to 5% by weight of a total weight of feed stock prior to processing by the separator means. 
     
     
         9 . The proppant of  claim 1 , wherein the proppant is greater than or equal to 10% by weight of a total weight of feed stock prior to processing by the separator means. 
     
     
         10 . The proppant of  claim 1 , wherein the proppant has an average particle size of 100 to 4,000 microns. 
     
     
         11 . An aggregate resulting from a processing means which separates a feed stock, the aggregate comprises a plurality of particles, the particles have an average median particle diameter of at least 1 micron more than the average median particle diameter of the feed stock. 
     
     
         12 . The aggregate of  claim 11 , wherein the particles have an average median particle diameter of at least 10 microns more than the average median particle diameter of the feed stock. 
     
     
         13 . The aggregate of  claim 11 , wherein the particles have an average median particle diameter of at least 20 microns more than the average median particle diameter of the feed stock. 
     
     
         14 . A proppant processing assembly comprising:
 a separator assembly having a central member extending from a first end to a second end, the central member supporting at least one helical flight provided between the first and second ends, the helical flight having a width provided between a proximal end and a distal end;   an assembly housing provided around a portion of the separator assembly, the assembly housing includes a collection portion for receiving a first fraction of processed feed stock which exits the separator assembly radially away from the central member outward past the distal end, the collection portion includes a first outlet;   a second outlet coupled to the separator assembly for receiving a second fraction of processed feed stock which exits the separator assembly at the second end of the at least one helical flight; and   a fraction acquisition assembly being selected from the group consisting of:
 a radial slot provided in a portion of the at least one helical flight; 
 a radial rim provided on the distal end of the at least a portion of one helical flight; 
 a splitter assembly provided along the radius of the at least one helical flight; and 
 a collection assembly formed by a first collection member coupled to the central member at a first end, and a second collection member coupled to the first collection member at a second end, the second collection member being perpendicular to the first collection member, and the first collection member being approximately parallel to the at least one helical flight and having a second width which is greater than the width of the at least one helical flight. 
   
     
     
         15 . The proppant processing assembly of  claim 14 , wherein a plurality of nested helical flights are provided on the central member. 
     
     
         16 . The proppant processing assembly of  claim 14 , wherein a portion of the central member is hollow, the hollow portion being coupled to the second outlet, and a termination member is provided at the second end of the at least one helical flight in order to direct the second fraction of processed feed stock from the at least one helical flight, through the hollow portion, and to the second outlet. 
     
     
         17 . The proppant processing assembly of  claim 14 , further comprising a feed stock delivery assembly including a feed stock supply line adapted to provide feed stock to the separator assembly. 
     
     
         18 . The proppant processing assembly of  claim 14 , wherein the first outlet is an outlet for a first fraction of processed material, and the second outlet is an outlet for a second fraction of processed material. 
     
     
         19 . A recombinant aggregate comprising:
 a first aggregate fraction resulting from a processing assembly, the first aggregate having a first particle size profile;   a second aggregate fraction resulting from a processing assembly, the second aggregate having a second particle size profile;   the first and second aggregate fractions are combined at a ratio such that the resulting mixture has a third particle size profile different from the first particle size profile and second particle size profile.   
     
     
         20 . The recombinant aggregate of  claim 19 , wherein the third particle size profile is different than a particle size profile of a feed stock provided to the processing assembly for generating the first aggregate fraction or second aggregate fraction.

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