Proppant bead forming methods

Patent metadata

Field	Value
Publication number	US-2017066962-A1
Application number	US-201615261764-A
Country	US
Kind code	A1
Filing date	Sep 9, 2016
Priority date	May 14, 2014
Publication date	Mar 9, 2017
Grant date	—

Abstract

The disclosure herein includes methods of preparing ceramic beads, useful as proppant materials, by mixing ceramic precursors, such as slag, fly ash, or aluminum dross, forming bead precursors from the mixture, and heating the bead precursors to drive a chemical reaction between the ceramic precursors to form the ceramic beads. The resultant ceramic beads may be generally spherical particles that are characterized by diameters of about 0.1 to 2 mm, a diametral strength of at least about 100 MPa, and a specific gravity of about 1.0 to 3.0. A coating process may optionally be used to increase a diametral strength of a proppant material. A sieving process may optionally be used to obtain a smaller range of sizes of proppant materials.

First claim

What is claimed is:

1 . A method of preparing a plurality of ceramics bead comprising:
mixing a plurality of ceramic precursors to form a mixture comprising particles of the ceramic precursors having sizes of about 30 μm to about 500 wherein the ceramic precursors include two or more of fly ash, slag, carbon black, pumice, and aluminum dross; forming a plurality of bead precursors each comprising the mixture, wherein the bead precursors each have cross-sectional dimensions of about 0.1 mm to about 2.5 mm; and heating the bead precursors to a temperature of greater than about 1200° C. to initiate a chemical reaction between the ceramic precursors, wherein the chemical reaction transforms the bead precursors into ceramic beads, wherein the ceramic beads are each characterized by one or more of a diameter of about 0.03 mm to about 2.0 mm, diametral strengths greater than about 100 MPa, and a specific gravity of about 1.0 to about 3.0.

2 . The method of claim 1 , wherein the mixture comprises one or more of:
a suspension, an emulsion, or a slurry comprising the plurality of ceramic precursors suspended in a solvent; homogenized ceramic precursors; or ground or milled ceramic precursors.

3 . The method of claim 1 , wherein the mixture comprises slag and fly ash, wherein the slag comprises about 20% to about 99% of the mixture by weight, wherein the fly ash comprises 1-80% of the mixture by weight, wherein carbon black comprises 0% to about 30% of the mixture by weight, wherein pumice comprises 0% to about 50% of the mixture by weight, and wherein aluminum dross comprises 0% to about 30% of the mixture by weight.

4 . The method of claim 1 , wherein the mixture further comprises one or more of:
a binder, wherein the binder comprises one or more of a silicate binder or a polyvinyl alcohol (PVA) binder; a reactive additive, wherein the reactive additive comprises one or more of AlN, Si 3 N 4 , or SiO 2 ; cellulose; a polymer; or a solvent, wherein the solvent comprises one or more of water, methanol, or ethanol.

5 . The method of claim 1 , wherein forming the plurality of bead precursors comprises one or more of:
forming the particles of ceramic precursors in the mixture into aggregated particles by a granulation process, wherein the aggregated particles correspond to the bead precursors; coating a plurality of organic scaffold beads with the mixture, wherein the organic scaffold beads comprise walnut shell or polystyrene beads; depositing the mixture into a plurality of mold forms, wherein the mold forms comprise graphite, molybdenum, a non-reactive metal, or a non-reactive ceramic; forming droplets from the mixture, wherein the mixture comprises a suspension, an emulsion, or a slurry comprising the ceramic precursors suspended in a solvent, and processing the droplets using a freeze drying process or a spray drying process, wherein freeze dried droplets or spray dried droplets correspond to the bead precursors; or forming aggregates of the mixture in a plasma source, wherein the aggregates of the mixture correspond to the bead precursors.

6 . The method of claim 1 , wherein the bead precursors comprise about 20% to about 99% slag by weight, wherein the bead precursors comprise about 1 to about 80% fly ash by weight, wherein the bead precursors comprise 0 to about 50% organic materials by weight, and wherein the organic materials comprise one or more of cellulose, walnut shells, or polystyrene.

7 . The method of claim 1 , wherein the bead precursors comprise green bodies of the ceramic precursors; and wherein the ceramic precursors in the green bodies chemically react during the heating to form a ceramic material.

8 . The method of claim 1 , wherein heating the bead precursors comprises heating the bead precursors in a reactive atmosphere, wherein the reactive atmosphere comprises one or more of N 2 , O 2 , or CO 2 , and wherein the chemical reaction forms one or more of a nitride-based ceramic, or an oxide-based ceramic from the ceramic precursors and the reactive atmosphere.

9 . The method of claim 1 , wherein heating the bead precursors includes:
heating the bead precursors to between about 1200° C. and about 1750° C.; heating the bead precursors to between about 250° C. and about 350° C. prior to heating the bead precursors to greater than about 1200° C.; sintering the bead precursors; annealing the bead precursors; melting the bead precursors; or exposing the bead precursors to a heated plasma.

10 . The method of claim 1 , wherein heating the bead precursors above a melting temperature of the mixture generates molten beads that exhibits a surface tension sufficient to cause the molten beads to form into or take on spherical shapes.

11 . The method of claim 1 , wherein heating the bead precursors includes:
heating the bead precursors using an inductive heating technique; heating the bead precursors using a conductive heating technique; or heating the bead precursors using a radiative heating technique.

12 . The method of claim 1 , wherein the ceramic beads are further characterized by one or more of:
porosities of about 1% to about 99%; hollow cores characterized by diameters of about 0.01 mm to about 1 mm; sphericities of about 0.5 to about 1.0; specific gravities of about 1.0 to about 1.5; specific gravities of about 1.0 to about 2.0; specific gravities of about 2.0 to about 2.5; specific gravities of about 2.5 to about 3.0; diametral strengths greater than about 150 MPa; diametral strengths greater than about 200 MPa; a uniform size distribution, wherein the uniform size distribution corresponds to a standard deviation of the diameters of the ceramic beads being less than 10% of an average or median diameter of the ceramic beads; or a non-uniform size distribution.

13 . The method of claim 1 , wherein the ceramic beads comprise one or more of a SiAlON ceramic, an oxide ceramic, a nitride ceramic, or an oxynitride ceramic.

14 . The method of claim 1 , further comprising coating the ceramic beads with an organic coating to form a plurality of coated ceramic beads.

15 . The method of claim 14 , wherein the organic coating comprises a phenolic polymer or a polyurethane polymer.

16 . The method of claim 14 , wherein the plurality of coated ceramic beads are characterized by diametral strengths greater than about 150 MPa.

17 . The method of claim 14 , wherein the plurality of coated ceramic beads are characterized by diametral strengths greater than about 300 MPa.

18 . The method of claim 1 , further comprising passing portions of the ceramic beads through one or more sieves each characterized by a different mesh size to sort the ceramic beads by diameter.

19 . The method of claim 18 , wherein a first sieve of the one or more sieves has a mesh size of about 10 to about 100.

20 . The method of claim 19 , wherein a second sieve of the one or more sieves has a mesh size of about 20 to about 140.

Assignees

• California Inst Of Techn
• Statoil Gulf Services LLC

Inventors

• Ravi Vilupanur A
• Firdosy Samad A
• Bux Sabah K
• Fleurial Jean-Pierre
• Yen Shiao-Pin S
• Kindler Andrew
• Chi Su C
• Homer Margie L
• Mcenerney Bryan W
• Kulkarni Pandurang
• Sundararajan Desikan

Classifications

• C04B35/587

  Fine ceramics · CPC title

• C04B35/62655

  Drying, e.g. freeze-drying, spray-drying, microwave or supercritical drying · CPC title

• C09K8/805

  Coated proppants · CPC title

• C04B2235/3208

  Calcium oxide or oxide-forming salts thereof, e.g. lime · CPC title

• C04B33/138

  from metallurgical processes, e.g. slag, furnace dust, galvanic waste · CPC title