US8133587B2 - Proppant materials comprising a coating of thermoplastic material, and methods of making and using - Google Patents
Proppant materials comprising a coating of thermoplastic material, and methods of making and using Download PDFInfo
- Publication number
- US8133587B2 US8133587B2 US12/043,818 US4381808A US8133587B2 US 8133587 B2 US8133587 B2 US 8133587B2 US 4381808 A US4381808 A US 4381808A US 8133587 B2 US8133587 B2 US 8133587B2
- Authority
- US
- United States
- Prior art keywords
- hydrocarbons
- oligomer
- particle
- coated
- coating
- 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 - Fee Related, expires
Links
- 238000000034 method Methods 0.000 title claims abstract description 49
- 239000011248 coating agent Substances 0.000 title claims description 107
- 238000000576 coating method Methods 0.000 title claims description 107
- 239000012815 thermoplastic material Substances 0.000 title claims description 45
- 239000000463 material Substances 0.000 title description 27
- 229920001169 thermoplastic Polymers 0.000 claims abstract description 76
- 239000004416 thermosoftening plastic Substances 0.000 claims abstract description 76
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 36
- 239000002245 particle Substances 0.000 claims description 130
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 67
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 67
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 67
- 229930195733 hydrocarbon Natural products 0.000 claims description 42
- 150000002430 hydrocarbons Chemical class 0.000 claims description 42
- 229920001187 thermosetting polymer Polymers 0.000 claims description 32
- 150000002148 esters Chemical class 0.000 claims description 28
- 229920005989 resin Polymers 0.000 claims description 27
- 239000011347 resin Substances 0.000 claims description 27
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 20
- 150000003505 terpenes Chemical class 0.000 claims description 17
- 235000007586 terpenes Nutrition 0.000 claims description 17
- 230000010512 thermal transition Effects 0.000 claims description 16
- 229920003986 novolac Polymers 0.000 claims description 15
- 239000004576 sand Substances 0.000 claims description 15
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 14
- 235000008331 Pinus X rigitaeda Nutrition 0.000 claims description 14
- 235000011613 Pinus brutia Nutrition 0.000 claims description 14
- 241000018646 Pinus brutia Species 0.000 claims description 14
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 claims description 13
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 13
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 13
- 239000000919 ceramic Substances 0.000 claims description 12
- 239000007795 chemical reaction product Substances 0.000 claims description 12
- KPAPHODVWOVUJL-UHFFFAOYSA-N 1-benzofuran;1h-indene Chemical compound C1=CC=C2CC=CC2=C1.C1=CC=C2OC=CC2=C1 KPAPHODVWOVUJL-UHFFFAOYSA-N 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 11
- SLGWESQGEUXWJQ-UHFFFAOYSA-N formaldehyde;phenol Chemical compound O=C.OC1=CC=CC=C1 SLGWESQGEUXWJQ-UHFFFAOYSA-N 0.000 claims description 10
- 229920001568 phenolic resin Polymers 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 8
- 229920003987 resole Polymers 0.000 claims description 7
- 239000003431 cross linking reagent Substances 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 6
- 239000000725 suspension Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 5
- 229910001570 bauxite Inorganic materials 0.000 claims description 4
- 239000011246 composite particle Substances 0.000 claims description 4
- 238000000151 deposition Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 claims description 4
- 240000007049 Juglans regia Species 0.000 claims description 2
- 235000009496 Juglans regia Nutrition 0.000 claims description 2
- 239000011324 bead Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 239000002557 mineral fiber Substances 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 235000020234 walnut Nutrition 0.000 claims description 2
- 238000005755 formation reaction Methods 0.000 abstract description 25
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 22
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 15
- 235000013824 polyphenols Nutrition 0.000 description 14
- -1 polyethylene Polymers 0.000 description 9
- 238000002844 melting Methods 0.000 description 8
- 230000008018 melting Effects 0.000 description 8
- 239000003784 tall oil Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000010998 test method Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 239000004831 Hot glue Substances 0.000 description 4
- 239000004312 hexamethylene tetramine Substances 0.000 description 4
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 4
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 4
- 239000011236 particulate material Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- QLZJUIZVJLSNDD-UHFFFAOYSA-N 2-(2-methylidenebutanoyloxy)ethyl 2-methylidenebutanoate Chemical compound CCC(=C)C(=O)OCCOC(=O)C(=C)CC QLZJUIZVJLSNDD-UHFFFAOYSA-N 0.000 description 2
- VSKJLJHPAFKHBX-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 VSKJLJHPAFKHBX-UHFFFAOYSA-N 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 2
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 2
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000005042 ethylene-ethyl acrylate Substances 0.000 description 2
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 2
- 229920002313 fluoropolymer Polymers 0.000 description 2
- XMGQYMWWDOXHJM-UHFFFAOYSA-N limonene Chemical compound CC(=C)C1CCC(C)=CC1 XMGQYMWWDOXHJM-UHFFFAOYSA-N 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 229920000058 polyacrylate Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 229920001021 polysulfide Polymers 0.000 description 2
- 239000005077 polysulfide Substances 0.000 description 2
- 150000008117 polysulfides Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- SCUZVMOVTVSBLE-UHFFFAOYSA-N prop-2-enenitrile;styrene Chemical compound C=CC#N.C=CC1=CC=CC=C1 SCUZVMOVTVSBLE-UHFFFAOYSA-N 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 229920000638 styrene acrylonitrile Polymers 0.000 description 2
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 2
- GRWFGVWFFZKLTI-UHFFFAOYSA-N α-pinene Chemical compound CC1=CCC2C(C)(C)C1C2 GRWFGVWFFZKLTI-UHFFFAOYSA-N 0.000 description 2
- WTARULDDTDQWMU-RKDXNWHRSA-N (+)-β-pinene Chemical compound C1[C@H]2C(C)(C)[C@@H]1CCC2=C WTARULDDTDQWMU-RKDXNWHRSA-N 0.000 description 1
- WTARULDDTDQWMU-IUCAKERBSA-N (-)-Nopinene Natural products C1[C@@H]2C(C)(C)[C@H]1CCC2=C WTARULDDTDQWMU-IUCAKERBSA-N 0.000 description 1
- GRWFGVWFFZKLTI-IUCAKERBSA-N 1S,5S-(-)-alpha-Pinene Natural products CC1=CC[C@@H]2C(C)(C)[C@H]1C2 GRWFGVWFFZKLTI-IUCAKERBSA-N 0.000 description 1
- 239000004971 Cross linker Substances 0.000 description 1
- 238000005698 Diels-Alder reaction Methods 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- WTARULDDTDQWMU-UHFFFAOYSA-N Pseudopinene Natural products C1C2C(C)(C)C1CCC2=C WTARULDDTDQWMU-UHFFFAOYSA-N 0.000 description 1
- XCPQUQHBVVXMRQ-UHFFFAOYSA-N alpha-Fenchene Natural products C1CC2C(=C)CC1C2(C)C XCPQUQHBVVXMRQ-UHFFFAOYSA-N 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- MVNCAPSFBDBCGF-UHFFFAOYSA-N alpha-pinene Natural products CC1=CCC23C1CC2C3(C)C MVNCAPSFBDBCGF-UHFFFAOYSA-N 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229930006722 beta-pinene Natural products 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- LCWMKIHBLJLORW-UHFFFAOYSA-N gamma-carene Natural products C1CC(=C)CC2C(C)(C)C21 LCWMKIHBLJLORW-UHFFFAOYSA-N 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 235000001510 limonene Nutrition 0.000 description 1
- 229940087305 limonene Drugs 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003110 molding sand Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/80—Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
- C09K8/805—Coated proppants
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
- Y10T428/2998—Coated including synthetic resin or polymer
Definitions
- the present invention relates generally to improved proppant compositions and the methods for their use in hydraulic fracturing treatments, gravel packing for sand control, and in other well formation treatments.
- the present invention is directed generally to thermoplastic coated proppants, methods for preparing the thermoplastic coated proppants, and methods for using these proppants in, for example, subterranean well formations and hydraulic fracturing operations.
- Coated proppants of the present invention are free-flowing, and are not tacky at ambient conditions, yet exhibit latent tackiness at the elevated temperatures and pressures often encountered in subterranean formations.
- the coated proppant comprises (i) a particle, and (ii) a thermoplastic coating on the particle.
- the coated proppant can further comprise an outer thermoset coating surrounding the thermoplastic coating.
- thermoplastic coating onto a particle to obtain a coated proppant.
- an outer thermoset coating surrounding the thermoplastic coated proppant can be applied.
- the present invention also contemplates methods of using coated proppants in applications such as hydraulic fracturing, gravel packing, and well formation treatments.
- a method of treating a subterranean formation comprising (a) introducing a fluid suspension of coated proppants to the subterranean formation; (b) depositing the coated proppants in the subterranean formation; (c) subjecting the coated proppants to a temperature above the thermal transition point temperature of the thermoplastic coating on the particle; (d) agglomerating the thermoplastic coating of the coated proppants to form a stable framework of proppant particles.
- the coated proppant comprises (i) a particle, and (ii) a thermoplastic coating on the particle.
- a coated proppant comprises (i) a particle, and (ii) a thermoplastic coating on the particle, wherein the thermoplastic coating comprises a pine rosin, a modified rosin, a rosin ester, or any combination thereof.
- Methods of making and methods of using this coated proppant are also provided.
- the present invention is directed generally to thermoplastic coated proppants, methods for preparing the thermoplastic coated proppants, and methods for using these proppants in, for example, subterranean well formations and hydraulic fracturing operations.
- Coated proppants of the present invention are both free-flowing and not tacky at ambient conditions. This improves the ease in handling the proppants prior to and during their use. For example, these coated proppants do not need to be transported to a well site in slurry or suspension form, but can be distributed in bulk quantities as free-flowing solids.
- the coated proppants exhibit latent tackiness which results in the agglomeration of the coated proppants to form a stable framework of proppant particles.
- Such a stable framework or network of agglomerated proppant particles reduces both solid particle flow-back and the transport of formation fines from the subterranean formation.
- particle when unmodified, are used herein to indicate the base material which, when coated, forms a “proppant.”
- frac sand is a material that is often referred to in the art as a “proppant,” but in this disclosure, it is referred to as a “particle.”
- proppant is a material that is often referred to in the art as a “proppant,” but in this disclosure, it is referred to as a “particle.”
- proppant “proppant particle,” “coated proppant,” and the like, are reserved for thermoplastic coated particles in accordance with the teachings of this invention.
- free-flowing is used herein to mean that the proppant particles do not agglomerate appreciably, and generally remain as discrete, individual proppant particles.
- Proppants of the present invention are “free-flowing” at ambient conditions, i.e., at a temperature of about 20-25° C. and at atmospheric pressure.
- the flowability of the solid particles can be measured using a test method such as the American Foundrymen's Society Procedure 227-87-S, entitled “Moldability of Molding Sand Mixtures” as found in the Mold & Core Test Handbook, 2nd edition (1989), which is incorporated herein by reference.
- the test procedure involves placing a 200-gram sample of solid particles in a cylindrical 8-mesh screen of a rotary screen device driven by a 57 rpm motor. The screen is rotated for 10 seconds.
- the moldability index is equal to the weight of the product passing through the screen divided by the original weight charged to the screen chamber (i.e., 200 grams). If all of the material passes through the screen, the moldability index is 100%.
- free-flowing proppants have a moldability index of greater than about 80% at ambient conditions. For instance, the proppants disclosed herein can have a moldability index greater than about 85%, or greater than about 90%.
- the coated proppants have a moldability index of greater than about 95%, or alternatively, greater than about 98%.
- solid materials that are not free-flowing have a moldability index of less than about 50%.
- Such materials can, in some cases, have a moldability index of less than about 40%, or less than about 25%.
- tacky is used herein to refer to the property of being gummy to the touch, or sticky. Proppant particles which are tacky often stick together, agglomerate, and have either limited free-flow characteristics, or none at all. Force is generally needed to move or separate tacky proppant particles. Tackiness can be measured by placing 200 grams of the proppant material on a smooth, horizontal glass plate. The plate is then tilted to a 45 degree angle. This procedure is discussed in co-pending U.S. patent application Ser. No. 11/803,688, the disclosure of which is incorporated herein by reference in its entirety.
- non-tacky proppants of the present invention greater than about 80% of the initial 200-gram sample will run off the plate when positioned at a 45 degree angle, under ambient temperature and pressure. Often, for non-tacky proppants, greater than about 85%, greater than about 90%, or greater than about 95%, of the initial 200-gram charge will run off the plate when positioned at a 45 degree angle. Conversely, for tacky proppants, generally less than about 50% of the initial 200-gram sample will run off of the plate. For some tacky proppants, less than about 40%, less than about 30%, or less than about 20%, of the initial sample will run off the plate when positioned at a 45 degree angle.
- this test procedure can also be employed for determining the tackiness that develops as the coated proppants are heated close to or past their softening or melting point. Generally, about 10 minutes in the oven is sufficient to allow the glass plate and the proppant sample to reach the desired temperature for testing, at which point the horizontal glass plate is tilted to a 45 degree angle. As the coating on the proppant softens and tackiness develops, the coated proppant particles will show a reduced tendency to run off the plate.
- Applicants disclose or claim a range of any type Applicants' intent is to disclose or claim individually each possible number that such a range could reasonably encompass, including end points of the range as well as any sub-ranges and combinations of sub-ranges encompassed therein.
- Applicants disclose or claim a temperature range Applicants' intent is to disclose or claim individually every possible number that such a range could encompass, consistent with the disclosure herein.
- a thermal transition point temperature is in the range from about 30° C.
- the thermal transition point temperature can be selected from about 30° C., about 35° C., about 40° C., about 45° C., about 50° C., about 55° C., about 60° C., about 65° C., about 70° C., about 75° C., about 80° C., about 85° C., about 90° C., about 95° C., about 100° C., about 105° C., about 110° C., about 115° C., about 120° C., about 130° C., about 135° C., about 140° C., about 145° C., about 150° C., about 155° C., about 160° C., about 165° C., about 170° C., about 175° C., about 180° C., about 185° C., about 190° C., about 195° C., or about 200° C., as well as any range between about 30° C., about 35° C., about 40° C., about 45° C.
- the thermal transition point temperature is in a range from about 30° C. to about 175° C., or from about 60° C. to about 100° C.
- this also includes any combination of ranges between about 30° C. and about 200° C. (for example, about 60° C. to about 100° C., and about 125° C. to about 175° C.).
- thermoplastic coating based on the weight of the particle in a coated proppant provided in one aspect of this invention.
- the thermoplastic coating is from about 1% to about 8% by weight of the particle, Applicants intend to recite that the weight percent can be selected from about 1%, about 1.5%, about 2%, about 2.5%, about 3%, about 3.5%, about 4%, about 4.5%, about 5%, about 5.5%, about 6%, about 6.5%, about 7%, about 7.5%, or about 8%.
- the weight percent can be within any range from about 1% to about 8% (for example, the weight percent is in a range from about 2% to about 7%), and this also includes any combination of ranges between about 1% and about 8%. Likewise, all other ranges disclosed herein should be interpreted in a manner similar to these two examples.
- compositions and methods are described in terms of “comprising” various components or steps, the compositions and methods can also “consist essentially of” or “consist of” the various components or steps.
- a coated proppant in accordance with one aspect of the present invention comprises (i) a particle, and (ii) a thermoplastic coating on the particle.
- the present invention is not limited to any specific type of particulate material for use as the proppant substrate (before providing the particle or particulate with the coating containing thermoplastic material in accordance with the present invention), so long as the particle has sufficient strength to withstand the stresses, such as elevated temperature and pressure, often encountered in oil and gas recovery applications.
- the particle of the coated proppant is a sand, a naturally occurring mineral fiber, a ceramic, a bauxite, a glass, a metal bead, a walnut hull, a composite particle, and the like.
- the sand can be a graded sand or a resin-coated sand.
- Such resin-coated sands include sand particles coated with a curable thermosetting resin, for example, as described in U.S. Pat. No. 5,837,656, the disclosure of which is incorporated herein by reference in its entirety. These resin-coated sands can serve as particles in the present invention.
- a ceramic can include both porous and non-porous ceramic materials, while a bauxite can include sintered bauxite materials.
- Composite particles are an agglomeration of smaller, fine particles held together by a binder, and such composite particles can be the particulate material in the present invention.
- compositions containing coated proppants can employ mixtures or combinations of more than one type of particle, for instance, both a sand and a ceramic can be coated and then mixed to form a composition of coated proppants. It is contemplated that any particulate material suitable for use in proppant applications can be used in the present invention, regardless of the specific gravity of the particle, although it can be beneficial in certain applications to have a lower specific gravity to increase the distance that the proppants can be carried into a formation prior to settling.
- the particle is either a porous ceramic or porous polymer particle.
- porous ceramic or porous polymer particles are described in, for example, U.S. Patent Publication Nos. 2004/0040708 and 2004/0200617, the disclosures of which are incorporated herein by reference in their entirety.
- These porous ceramic or porous polymer materials can be of natural origin or can be produced synthetically. Although the use of such materials is not limited by specific gravity, the specific gravity of these materials is generally less than about 3 g/cc, or less than about 2.7 g/cc. In another aspect, the specific gravity of the porous particle is less than about 2.5 g/cc, for example, less than about 2.2 g/cc.
- the particle size of the particle used in the coated proppant of the present invention generally falls within a range from about 100 microns to about 3000 microns (about 3 mm). In another aspect, the particle size is from about 125 microns to about 2500 microns, from about 150 microns to about 2000 microns, or from about 175 microns to about 1500 microns. Yet, in another aspect, the particle of the coated proppant of the present invention has a particle size that falls within a narrower range of about 200 to about 1000 microns, for example, about 250 to about 800 microns, or from about 300 to about 700 microns.
- the particles generally have a mesh size from about 8 and about 100, based on the U.S. Standard Sieve Series.
- at least about 90% by weight of the particles have a particle size falling within the range from about 8 to about 100 mesh.
- at least about 95% by weight of the particles in a coated proppant composition have a size within the range from about 8 to about 100 mesh.
- 90% by weight or more (e.g., 95% or more) of the particles in a coated proppant composition can have a size within the 20 to 40 mesh range in another aspect of this invention.
- the particle in the coated proppant has a size in the range from about 8 to about 140 mesh, from 10 to about 120 mesh, from about 10 to about 100 mesh, or from about 14 to about 80 mesh. In other aspects of this invention, the particle is in a range from about 18 to about 60 mesh, or from about 20 mesh to about 40 mesh. In another aspect, there is less than about 10% by weight, for example, 5% by weight of less, of particles in a coated proppant composition having a size of less than about 20 mesh or greater than about 50 mesh.
- coated proppants of the present invention generally comprise particles which are not limited to any particular material or size.
- a coated proppant of the present invention also contains a thermoplastic coating on the particle.
- a coating provides the coated proppant with latent tackiness, in that the tackiness of the coating is not exhibited until the proppant is deposited in, for example, a subterranean formation at elevated temperature and pressure.
- the coated proppants, which exhibit latent tackiness are free-flowing and non-tacky.
- Suitable thermoplastic materials for use in providing the coating on the particle in accordance with the present invention can have a thermal transition point temperature (TTPT) in the range from about 30 to about 200° C.
- the thermal transition point temperature is measured by the melting point or the softening point of the thermoplastic coating, and reflects the temperature at which the material is able to soften, flow, become sticky or tacky, and/or exhibit adhesive characteristics.
- Temperatures in the range from about 30 to about 200° C. are often encountered by proppant materials in their use in subterranean formations.
- the softening point and melting point of potentially useful thermoplastic materials can be determined by any means and apparatus known to one of ordinary skill in the art.
- Two methods for determining the softening point of resins are the Mettler Cup and Ball test method (ASTM D 6090-99) and the Vicat Softening Point test method (ASTM D 1525).
- Two instruments for determining the melting point of a thermoplastic include a capillary melt point instrument and a Differential Scanning Calorimeter (abbreviated DSC, ASTM D 3418-03).
- DSC Differential Scanning Calorimeter
- the coated proppant At a temperature below the TTPT, such as ambient temperature conditions, the coated proppant is free-flowing and can be packaged, transported to and handled at the well head without the need for any specialized equipment or skilled labor. Since the coated proppants are not tacky at ambient conditions, the coated proppant particles do not have to be stored and/or transported as a slurry or suspension in a liquid diluent. The adhesive character of the thermoplastic coating is not exhibited until the coated proppants are deposited in the subterranean formation at elevated temperature and pressure (i.e., latent tackiness).
- the thermoplastic coating of the coated proppant has a thermal transition point temperature in the range from about 30 to about 200° C.
- the thermoplastic coating has a TTPT in the range from about 40 to about 180° C., from about 45 to about 160° C., or from about 50 to about 150° C.
- the thermoplastic coating has a TTPT in the range from about 55 to about 125° C., or from about 60 to about 100° C.
- the thermoplastic coating has a TTPT in the range from about 50 to about 175° C. such as, for example, from about 70 to about 140° C.
- Coated proppants of the present invention comprise a thermoplastic coating on the particle.
- This coating comprises at least one thermoplastic material, and thermoplastic materials suitable for use in accordance with the present invention include, but are not limited to, a polyethylene, a polypropylene, an ethylene vinyl acetate, an ethylene ethyl acrylate, a styrene-isoprene-styrene, an acrylonitrile-butadiene-styrene, a styrene-butadiene-styrene, a polystyrene, a polyurethane, an acrylic polymer, a polyvinyl chloride, a fluoroplastic, a pine rosin (e.g., tall oil rosin, wood rosin, and gum rosin), a modified rosin (e.g., disproportionated rosins, hydrogenated rosins, polymerized or oligomerized rosins, diels
- oligomers of C 5 hydrocarbons e.g., oligomers of cyclopentadiene
- oligomers of C 9 hydrocarbons e.g., oligomers of alpha-methylstyrene
- thermoplastic material for use in the coated proppants of the present invention will depend, in part, on the TTPT of the respective thermoplastic material (e.g., the softening point) and the anticipated thermal conditions of the particular end-use application.
- Phenolic novolac resins generally are produced with a formaldehyde to phenol molar ratio that is less than about 0.8:1. Phenolic novolacs have a shortage of formaldehyde and, therefore, are thermoplastic materials which will not cure in the absence of a crosslinking agent (e.g., hexamine). Rosin esters can be produced by condensing, for example, a tall oil rosin with a polyol. Similar ester products can be produced using other rosin sources, such as wood rosin and gum rosin, and these materials also fall within the scope of the present invention.
- a crosslinking agent e.g., hexamine
- the thermoplastic coating of the present invention comprises at least one thermoplastic material.
- This thermoplastic material in one aspect of the invention, can be a polyethylene, a polypropylene, an ethylene vinyl acetate, an ethylene ethyl acrylate, a styrene-isoprene-styrene, an acrylonitrile-butadiene-styrene, a styrene-butadiene-styrene, a polystyrene, a polyurethane, an acrylic polymer, a polyvinyl chloride, a fluoroplastic, a polysulfide, a styrene-acrylonitrile, a nylon, a phenol-formaldehyde novolac resin, or any combination thereof.
- the thermoplastic material is a pine rosin, a modified rosin, a rosin ester, or any combination thereof.
- the thermoplastic material is a terpene resin, a coumarone-indene resin, an oligomer of C 5 hydrocarbons, an oligomer of C 9 hydrocarbons, an oligomeric reaction product of a terpene and a phenolic, an oligomeric reaction product of a terpene and a styrenic, or combinations thereof.
- the number-average molecular weight of these oligomeric materials is less than about 10,000, and more often, less than about 5000.
- the number-average molecular weight of the terpene resin, the coumarone-indene resin, the oligomer of C 5 hydrocarbons, the oligomer of C 9 hydrocarbons, the oligomeric reaction product of a terpene and a phenolic, and the oligomeric reaction product of a terpene and a styrenic are all within a range from about 100 to about 4000.
- the number-average molecular weight of these materials can be in a range from about 125 to about 3000, from about 150 to about 2000, or from about 200 to about 1000, in other aspects of this invention.
- the thermoplastic material can be selected from among an ethylene vinyl acetate, a phenol-formaldehyde novolac resin, a pine rosin, a modified rosin, a rosin ester, a terpene resin, a coumarone-indene resin, an oligomer of C 5 hydrocarbons, an oligomer of C 9 hydrocarbons, an oligomeric reaction product of a terpene and a phenolic, and an oligomeric reaction product of a terpene and a styrenic, or any combination thereof.
- the thermoplastic coating comprises a thermoplastic material such as ethylene vinyl acetate.
- the thermoplastic coating can comprise a thermoplastic material which is selected from a pine rosin, a modified rosin, or a rosin ester, or a combination thereof.
- hot melt adhesive grades Opt-E-BondTM HL0033 manufactured by the HB Fuller Co.
- Cool-LokTM 34-250A manufactured by National Adhesives
- Opt-E-BondTM HL0033 is a hot melt adhesive containing polyethylene wax
- Cool-LokTM 34-250A is a hot melt adhesive containing ethylene vinyl acetate, paraffin wax, and an aromatic tackifier.
- pine rosins and modified rosins marketed by Georgia-Pacific as NOVARES® 1100 and NOVARES® 1182 are also suitable for use as thermoplastic materials in the present invention.
- a coated proppant according to one aspect of the present invention comprises (i) a particle, and (ii) a thermoplastic coating on the particle, wherein the thermoplastic coating comprises a pine rosin, a modified rosin, a rosin ester, or a combination thereof.
- the thermoplastic coating can comprise a glycerol rosin ester or a pentaerythritol rosin ester.
- the thermoplastic material is provided as at least a partial coating on the particle.
- the thermoplastic coating on the particle completely surrounds the particle.
- the thermoplastic coating is from about 0.5% to about 15% by weight of the particle.
- the weight percent of the thermoplastic coating, based on the weight of the particle can be from about 1% to about 12%, from about 1% to about 10%, or from about 1% to about 8%.
- the weight percent of the thermoplastic coating, based on the weight of the particle is from about 1.5% to about 8%, from about 2% to about 7%, or from about 2.5% to about 6% by weight.
- the weight percent of the thermoplastic coating, based on the weight of the particle is from about 5% to about 8% by weight.
- the coating thickness on an individual particle typically is within a range from about 0.1 to about 5 mils, for example, between about 0.2 and about 4 mils, or between about 0.3 and about 3 mils. In another aspect, the thickness of the thermoplastic coating on the particle is in a range from about 0.5 to about 2.8 mils, or from about 0.6 to about 2.5 mils. Further, the thickness of the thermoplastic coating on the particle can be from about 0.75 mils to about 2 mils in other aspects of this invention.
- thermoplastic coating onto a particle to obtain the coated proppant.
- the thermoplastic coating can be applied onto the particle using a warm or hot coat process in which the particle is first heated to a temperature above the melting point of the thermoplastic coating. The thermoplastic coating then is added to the hot particle, and mixed, causing the thermoplastic coating to coat and fuse to the particle, thereby forming the coated proppant. Sufficient time is provided to allow the thermoplastic coating to thoroughly coat the particle, while blending or mixing of the particle with the thermoplastic coating is employed.
- the resultant hot, coated proppants then are quenched to a temperature below the thermal transition point temperature of the thermoplastic coating to yield non-tacky, free-flowing solids.
- the coated proppants can be sieved to the desired particle size distribution.
- the thermoplastic coating Prior to the addition of the thermoplastic coating to the particle, optionally, the thermoplastic coating can be pre-heated to melt the coating by heating the coating material to a temperature in excess of its melting point.
- thermoplastic coating can be dissolved in a suitable solvent, or suspended or emulsified in a suitable solvent, and the thermoplastic-containing solvent then can be applied to the particulate.
- the coating can be, for example, blended or mixed with, or sprayed onto, the particles to be coated.
- Other methods known to those of skill in the art also can be used, and such methods may vary based on the particular thermoplastic coating employed.
- solvent is removed by suitable means (e.g., drying), resulting in free-flowing, coated proppants.
- suitable means e.g., drying
- the coated proppants of the present invention can be used to treat a subterranean formation.
- a method of treating a subterranean formation in accordance with this aspect of the present invention comprises (a) introducing a fluid suspension of coated proppants to the subterranean formation; (b) depositing the coated proppants in the subterranean formation; (c) subjecting the coated proppants to a temperature above the thermal transition point temperature of the thermoplastic coating on the particle; and (d) agglomerating the thermoplastic coating of the coated proppants to form a stable framework of proppant particles.
- the coated proppant comprises (i) a particle, and (ii) a thermoplastic coating on the particle.
- the agglomerated framework of proppant particles in the subterranean formation can reduce solid particle flow-back and/or the transport of formation fines from the subterranean formation.
- Other methods of using the coated proppants of the present invention are also provided in co-pending U.S. patent application Ser. No. 11/456,897, the disclosure of which is incorporated herein by reference in its entirety.
- a coated proppant which further comprises an outer thermoset coating surrounding the thermoplastic coating.
- This thermoset coating forms an outer shell of the coated proppant and is formulated to be non-tacky, resulting in free-flowing proppant particles.
- the thermoset coating breaks and exposes the thermoplastic coating (i.e., tacky thermoplastic coating), which can flow and cause agglomeration with adjacent coated proppants or other particulates.
- tacky thermoplastic coating i.e., tacky thermoplastic coating
- Such a structure has a latent tackiness because the outer thermoset shell provides free-flowing proppant particles at ambient temperature and pressure.
- thermoset coating comprises a thermoset material
- thermoset materials suitable for use in accordance with the present invention include, but are not limited to, phenol-formaldehyde resole resins (such as GP-2086 and 761D31, available from Georgia- Pacific), phenol-formaldehyde novolac resins mixed with a cross-linking agent such as hexamine (novolac resins such as GP-2110, GP-2202 and GP-298G87), epoxy resins, and other similar materials.
- GP-2086 is a liquid phenolic resole resin
- GP-761D31 is an ammonia-catalyzed liquid phenolic resole resin in methanol.
- GP-2110 is a liquid phenolic novolac resin in methanol
- GP-2202 is a flaked phenolic novolac resin
- GP-298G87 is a flaked phenolic novolac resin.
- Other curable thermosetting materials that can be employed in the present invention include, but are not limited to, unsaturated polyesters, vinyl esters, polyurethanes, melamine-formaldehyde resins, and the like, or combinations thereof.
- the thermoset coating is cured. Curing can be achieved, for example, by means of heat and/or by the addition of a crosslinking or curing agent.
- phenolic novolac resins generally are produced with a formaldehyde to phenol molar ratio that is less than about 0.8:1.
- Phenolic novolacs have a shortage of formaldehyde and, therefore, are thermoplastic materials and will not cure in the absence of a crosslinking agent (e.g., hexamine).
- Phenolic resole resins generally are produced with a formaldehyde to phenol ratio molar ratio that is about 1:1 or more. Resoles are thermosetting and crosslink in the absence of a crosslinking agent.
- the thermoset coating comprises a phenol-formaldehyde resole resin, a phenol-formaldehyde novolac resin and a crosslinking agent, or a combination thereof.
- the thermoset coating completely surrounds the thermoplastic coating.
- the thermoset coating is from about 0.5% to about 15% by weight of the thermoplastic coated proppant.
- the weight percent of the thermoset coating based on the weight of the coated proppant, can be from about 1% to about 12%, from about 1% to about 10%, from about 1% to about 8%, from about 1% to about 6%, or from about 1% to about 4% by weight.
- the thickness of the thermoset coating on an individual coated proppant typically falls within the range from about 0.2 to about 5 mils, for example, between about 0.3 and about 4 mils, or between about 0.5 and about 3 mils.
- the thickness of the thermoset coating on the thermoplastic coated particle is in a range from about 0.7 to about 2.8 mils, from about 0.8 to about 2.5 mils, or from about 1 mil to about 2 mils.
- thermoset coating to a thermoplastic coated proppant
- methods of using the coated proppant with the thermoset shell are provided in co-pending U.S. patent application Ser. No. 11/456,897, the disclosure of which is incorporated herein by reference in its entirety.
- a non-limiting example of the production of a thermoplastic coated proppant with a thermoset coating or shell is provided in Example 4 below.
- a particle (sand or porous ceramic) is added to a heated mixer (mill) and allowed to equilibrate at a temperature of about 232° C. (450° F.). Thereafter, a hot melt resin in an amount of about 6% by weight, based on the weight of the particle, is added to the mixer (mill) as a free-flowing powder. These materials are mixed for one minute and then cooling water is added to reduce the temperature. Mixing is continued until the temperature has been reduced sufficiently to provide a free-flowing coated proppant, which is removed and sized as desired.
- Cool-LokTM 34-250A a hot melt adhesive containing ethylene vinyl acetate, paraffin wax, and an aromatic tackifier
- the ceramic particle was placed into a preheated sand coating mill. When the temperature of the ceramic particles was about 450° F., as measured by an IR gun, the liquid Cool-LokTM 34-250A thermoplastic material was added to the ceramic particles and mixed for sixty seconds. Then, 100 grams of water were added to cool the coated proppant particles.
- the coated proppants were discharged from the coating mill, cooled to ambient temperature, and screened through an 18 mesh sieve, resulting in free-flowing and non-tacky proppant particles.
- the weight percent of the thermoplastic coating, based on the weight of the particle, for the proppants of Example 3 was about 4%.
- thermoset shell This coated proppant with thermoset shell was subjected to 8,000 psi pressure for several minutes at ambient temperature (20° C.), then the pressure was removed and material extracted, it was in the form of free-flowing grains. Under these conditions, the outer thermoset shell cracked, exposing the inner thermoplastic coating. However, at ambient temperature, the thermoplastic coating was not tacky.
- thermoset shell Another sample of the above-described coated proppant with thermoset shell was preheated in the crush cell at 105° C. and then was subjected to 8,000 psi for several minutes. Upon removing the pressure and extracting the proppant, the material came out in a solid rigid pellet. In this case, the cured outer layer cracked under the pressure and allowed the tacky thermoplastic coating underneath to exude out and bond to neighboring proppant particles.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Paints Or Removers (AREA)
Abstract
Description
Claims (36)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/043,818 US8133587B2 (en) | 2006-07-12 | 2008-03-06 | Proppant materials comprising a coating of thermoplastic material, and methods of making and using |
PCT/US2009/036326 WO2009111697A1 (en) | 2008-03-06 | 2009-03-06 | Proppant materials and methods |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/456,897 US8003214B2 (en) | 2006-07-12 | 2006-07-12 | Well treating materials comprising coated proppants, and methods |
US12/043,818 US8133587B2 (en) | 2006-07-12 | 2008-03-06 | Proppant materials comprising a coating of thermoplastic material, and methods of making and using |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/456,897 Continuation-In-Part US8003214B2 (en) | 2006-07-12 | 2006-07-12 | Well treating materials comprising coated proppants, and methods |
Publications (2)
Publication Number | Publication Date |
---|---|
US20080202750A1 US20080202750A1 (en) | 2008-08-28 |
US8133587B2 true US8133587B2 (en) | 2012-03-13 |
Family
ID=40732251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/043,818 Expired - Fee Related US8133587B2 (en) | 2006-07-12 | 2008-03-06 | Proppant materials comprising a coating of thermoplastic material, and methods of making and using |
Country Status (2)
Country | Link |
---|---|
US (1) | US8133587B2 (en) |
WO (1) | WO2009111697A1 (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9260651B2 (en) | 2014-03-28 | 2016-02-16 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
WO2016081220A1 (en) * | 2014-11-18 | 2016-05-26 | Powdermet, Inc. | Polymer coated proppant |
WO2016089599A1 (en) | 2014-12-05 | 2016-06-09 | Dow Global Technologies Llc | Proppant comprising an oil well treatment agent coating |
WO2016140813A1 (en) | 2015-03-04 | 2016-09-09 | Covestro Llc | Proppant sand coating for dust reduction |
US9518214B2 (en) | 2013-03-15 | 2016-12-13 | Preferred Technology, Llc | Proppant with polyurea-type coating |
US9562187B2 (en) | 2012-01-23 | 2017-02-07 | Preferred Technology, Llc | Manufacture of polymer coated proppants |
WO2017058762A1 (en) | 2015-09-29 | 2017-04-06 | Georgia-Pacific Chemicals Llc | Proppants coated with a resin containing a clay |
US9624421B2 (en) | 2011-09-02 | 2017-04-18 | Preferred Technology, Llc | Dual function proppants |
US9725645B2 (en) | 2011-05-03 | 2017-08-08 | Preferred Technology, Llc | Proppant with composite coating |
US9790422B2 (en) | 2014-04-30 | 2017-10-17 | Preferred Technology, Llc | Proppant mixtures |
US9862881B2 (en) | 2015-05-13 | 2018-01-09 | Preferred Technology, Llc | Hydrophobic coating of particulates for enhanced well productivity |
US10000691B2 (en) | 2015-06-08 | 2018-06-19 | Halliburton Energy Services, Inc. | Variably tacky proppants |
WO2018177619A1 (en) | 2017-03-30 | 2018-10-04 | Clariant International Ltd | Fluids for fracking of paraffinic oil bearing formations |
US10100247B2 (en) | 2013-05-17 | 2018-10-16 | Preferred Technology, Llc | Proppant with enhanced interparticle bonding |
US10281380B1 (en) | 2016-06-17 | 2019-05-07 | Matthew D. Bryant | Method for testing a proppant |
US10508231B2 (en) | 2014-03-28 | 2019-12-17 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US10544358B2 (en) | 2011-05-03 | 2020-01-28 | Preferred Technology, Llc | Coated and cured proppants |
US10590337B2 (en) | 2015-05-13 | 2020-03-17 | Preferred Technology, Llc | High performance proppants |
US10696896B2 (en) | 2016-11-28 | 2020-06-30 | Prefferred Technology, Llc | Durable coatings and uses thereof |
US11208591B2 (en) | 2016-11-16 | 2021-12-28 | Preferred Technology, Llc | Hydrophobic coating of particulates for enhanced well productivity |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8133587B2 (en) | 2006-07-12 | 2012-03-13 | Georgia-Pacific Chemicals Llc | Proppant materials comprising a coating of thermoplastic material, and methods of making and using |
US8003214B2 (en) * | 2006-07-12 | 2011-08-23 | Georgia-Pacific Chemicals Llc | Well treating materials comprising coated proppants, and methods |
US8058213B2 (en) * | 2007-05-11 | 2011-11-15 | Georgia-Pacific Chemicals Llc | Increasing buoyancy of well treating materials |
US7754659B2 (en) * | 2007-05-15 | 2010-07-13 | Georgia-Pacific Chemicals Llc | Reducing flow-back in well treating materials |
US20100139918A1 (en) * | 2008-09-30 | 2010-06-10 | Schlumberger Technology Corporation | Method to prevent well sanding using gravel packing |
WO2011005535A1 (en) * | 2009-06-22 | 2011-01-13 | Dow Global Technologies, Inc. | Ceramic-polymer composites |
US20110073309A1 (en) * | 2009-09-30 | 2011-03-31 | Schlumberger Technology Corporation | Method of proppant oil or gas formation fracture |
WO2011146186A2 (en) * | 2010-05-17 | 2011-11-24 | Georgia-Pacific Chemicals Llc | Proppants for use in hydraulic fracturing of subterranean formations |
US20120037368A1 (en) | 2010-08-12 | 2012-02-16 | Conocophillips Company | Controlled release proppant |
US8993489B2 (en) | 2011-05-03 | 2015-03-31 | Preferred Technology, Llc | Coated and cured proppants |
US9040467B2 (en) | 2011-05-03 | 2015-05-26 | Preferred Technology, Llc | Coated and cured proppants |
CN103031121A (en) * | 2011-09-30 | 2013-04-10 | 北京仁创科技集团有限公司 | Fracturing propping agent, preparation method thereof and deep wall fracturing method |
US20130196884A1 (en) * | 2012-02-01 | 2013-08-01 | Trican Well Service, Ltd. | Downhole Chemical Delivery For Oil And Gas Wells |
US8967263B2 (en) * | 2012-09-18 | 2015-03-03 | Halliburton Energy Services, Inc. | Methods of treating a subterranean formation with stress-activated resins |
US9279077B2 (en) * | 2012-11-09 | 2016-03-08 | Halliburton Energy Services, Inc. | Methods of forming and placing proppant pillars into a subterranean formation |
DK2925830T3 (en) | 2012-11-30 | 2019-03-11 | Total E&P Danmark As | PROCEDURE TO PROVIDE A BARRIER IN A FRACTURED SYSTEM |
US9797231B2 (en) * | 2013-04-25 | 2017-10-24 | Halliburton Energy Services, Inc. | Methods of coating proppant particulates for use in subterranean formation operations |
RU2527453C1 (en) | 2013-05-15 | 2014-08-27 | Открытое акционерное общество "Нефтяная компания "Роснефть" | Polymer proppant material and method for production thereof |
US10106729B2 (en) * | 2014-01-22 | 2018-10-23 | Durez Corporation | Resin composition, coated particles, injection material and method for injecting injection material into fracture |
US9867761B2 (en) * | 2014-04-30 | 2018-01-16 | L Star Softcoat, Llc | Colored lamellar compositions |
US9751192B2 (en) * | 2014-09-17 | 2017-09-05 | Saint-Gobain Abrasives, Inc. | Polymer impregnated backing material, abrasive articles incorporating same, and processes of making and using |
CN104357042B (en) * | 2014-10-23 | 2017-06-09 | 亿利资源集团有限公司 | A kind of overlay film proppant and preparation method thereof |
CA2988541A1 (en) * | 2015-08-31 | 2017-03-09 | Halliburton Energy Services, Inc. | Self-supporting proppant with improved proppant pack conductivity |
US20190112521A1 (en) * | 2017-10-18 | 2019-04-18 | Pfp Technology, Llc | Friction Reduction and Suspension in High TDS Brines |
CN110699062B (en) * | 2019-10-30 | 2021-09-28 | 大港油田集团有限责任公司 | Epoxy resin coating proppant and preparation method and construction process thereof |
CN111471446A (en) * | 2020-04-13 | 2020-07-31 | 北京大德广源石油技术服务有限公司 | Sand control agent for fracturing and application method thereof |
Citations (98)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3815680A (en) * | 1971-04-09 | 1974-06-11 | Continental Oil Co | Method for fracturing and propping unconsolidated and dilatant subterranean formations |
US3929191A (en) | 1974-08-15 | 1975-12-30 | Exxon Production Research Co | Method for treating subterranean formations |
US4073343A (en) | 1976-12-23 | 1978-02-14 | Texaco Inc. | Sand consolidation method |
CA1057649A (en) | 1977-06-20 | 1979-07-03 | Donald S. Black | Formation fracturing with foam having greater proppant concentration |
US4160483A (en) | 1978-07-21 | 1979-07-10 | The Dow Chemical Company | Method of treating a well using fluoboric acid to clean a propped fracture |
US4183813A (en) | 1978-11-15 | 1980-01-15 | Palmer Engineering Company Ltd. | Mixture concentrator |
US4222444A (en) | 1978-12-06 | 1980-09-16 | Hamilton Harold L | Method of well fluid leak prevention |
GB2050467A (en) | 1979-06-07 | 1981-01-07 | Perlman W | Fracturing Subterranean Formations |
US4336842A (en) | 1981-01-05 | 1982-06-29 | Graham John W | Method of treating wells using resin-coated particles |
US4439489A (en) | 1982-02-16 | 1984-03-27 | Acme Resin Corporation | Particles covered with a cured infusible thermoset film and process for their production |
US4493875A (en) | 1983-12-09 | 1985-01-15 | Minnesota Mining And Manufacturing Company | Proppant for well fractures and method of making same |
CA1185778A (en) | 1982-07-12 | 1985-04-23 | Brian R. Ainley | Stable foams and methods of use |
US4518040A (en) | 1983-06-29 | 1985-05-21 | Halliburton Company | Method of fracturing a subterranean formation |
US4527627A (en) | 1983-07-28 | 1985-07-09 | Santrol Products, Inc. | Method of acidizing propped fractures |
US4547468A (en) | 1981-08-10 | 1985-10-15 | Terra Tek, Inc. | Hollow proppants and a process for their manufacture |
EP0169412A1 (en) | 1984-07-05 | 1986-01-29 | Norton Company | Proppant for oil and gas wells |
US4569394A (en) | 1984-02-29 | 1986-02-11 | Hughes Tool Company | Method and apparatus for increasing the concentration of proppant in well stimulation techniques |
CA1202882A (en) | 1982-03-01 | 1986-04-08 | Owen Richmond | Method of removing gas from an underground seam |
US4585064A (en) | 1984-07-02 | 1986-04-29 | Graham John W | High strength particulates |
US4665990A (en) | 1984-07-17 | 1987-05-19 | William Perlman | Multiple-stage coal seam fracing method |
EP0308257A2 (en) | 1987-09-17 | 1989-03-22 | Minnesota Mining And Manufacturing Company | Novolac coated ceramic particulate |
US4852650A (en) | 1987-12-28 | 1989-08-01 | Mobil Oil Corporation | Hydraulic fracturing with a refractory proppant combined with salinity control |
US4888240A (en) | 1984-07-02 | 1989-12-19 | Graham John W | High strength particulates |
US4923714A (en) | 1987-09-17 | 1990-05-08 | Minnesota Mining And Manufacturing Company | Novolac coated ceramic particulate |
US5005641A (en) | 1990-07-02 | 1991-04-09 | Mohaupt Henry H | Gas generator with improved ignition assembly |
US5128390A (en) | 1991-01-22 | 1992-07-07 | Halliburton Company | Methods of forming consolidatable resin coated particulate materials in aqueous gels |
US5188175A (en) | 1989-08-14 | 1993-02-23 | Carbo Ceramics Inc. | Method of fracturing a subterranean formation with a lightweight propping agent |
US5217074A (en) | 1991-10-29 | 1993-06-08 | Exxon Chemical Patents Inc. | Method of fracturing formations |
US5311946A (en) | 1992-08-04 | 1994-05-17 | Benchmark Research And Technology, Inc. | Method and process for the stabilization of resin coated particulates |
US5318382A (en) | 1990-10-25 | 1994-06-07 | Cahill Calvin D | Method and apparatus for hydraulic embedment of waste in subterranean formations |
US5330005A (en) | 1993-04-05 | 1994-07-19 | Dowell Schlumberger Incorporated | Control of particulate flowback in subterranean wells |
US5411093A (en) | 1993-12-10 | 1995-05-02 | Mobil Oil Corporation | Method of enhancing stimulation load fluid recovery |
US5422183A (en) | 1993-06-01 | 1995-06-06 | Santrol, Inc. | Composite and reinforced coatings on proppants and particles |
US5492178A (en) | 1993-11-12 | 1996-02-20 | Halliburton Company | Well treating methods and devices using particulate blends |
US5500174A (en) | 1994-09-23 | 1996-03-19 | Scott; Gregory D. | Method of manufacture of a prepacked resin bonded well liner |
US5501275A (en) | 1993-04-05 | 1996-03-26 | Dowell, A Division Of Schlumberger Technology Corporation | Control of particulate flowback in subterranean wells |
US5501274A (en) | 1995-03-29 | 1996-03-26 | Halliburton Company | Control of particulate flowback in subterranean wells |
US5578371A (en) | 1995-08-25 | 1996-11-26 | Schuller International, Inc. | Phenol/formaldehyde fiberglass binder compositions exhibiting reduced emissions |
US5582249A (en) | 1995-08-02 | 1996-12-10 | Halliburton Company | Control of particulate flowback in subterranean wells |
US5639806A (en) | 1995-03-28 | 1997-06-17 | Borden Chemical, Inc. | Bisphenol-containing resin coating articles and methods of using same |
US5697440A (en) | 1996-01-04 | 1997-12-16 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5728302A (en) | 1992-04-09 | 1998-03-17 | Groundwater Services, Inc. | Methods for the removal of contaminants from subterranean fluids |
US5775425A (en) | 1995-03-29 | 1998-07-07 | Halliburton Energy Services, Inc. | Control of fine particulate flowback in subterranean wells |
US5787986A (en) | 1995-03-29 | 1998-08-04 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5833000A (en) | 1995-03-29 | 1998-11-10 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5837656A (en) | 1994-07-21 | 1998-11-17 | Santrol, Inc. | Well treatment fluid compatible self-consolidating particles |
US5839510A (en) | 1995-03-29 | 1998-11-24 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5929437A (en) | 1995-08-18 | 1999-07-27 | Protechnics International, Inc. | Encapsulated radioactive tracer |
US5964291A (en) | 1995-02-28 | 1999-10-12 | Aea Technology Plc | Well treatment |
US6017854A (en) | 1997-05-28 | 2000-01-25 | Union Oil Company Of California | Simplified mud systems |
US6047772A (en) | 1995-03-29 | 2000-04-11 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US6059034A (en) | 1996-11-27 | 2000-05-09 | Bj Services Company | Formation treatment method using deformable particles |
US6114410A (en) | 1998-07-17 | 2000-09-05 | Technisand, Inc. | Proppant containing bondable particles and removable particles |
US6116342A (en) | 1998-10-20 | 2000-09-12 | Halliburton Energy Services, Inc. | Methods of preventing well fracture proppant flow-back |
US6209643B1 (en) | 1995-03-29 | 2001-04-03 | Halliburton Energy Services, Inc. | Method of controlling particulate flowback in subterranean wells and introducing treatment chemicals |
US6330916B1 (en) | 1996-11-27 | 2001-12-18 | Bj Services Company | Formation treatment method using deformable particles |
US6364018B1 (en) | 1996-11-27 | 2002-04-02 | Bj Services Company | Lightweight methods and compositions for well treating |
US6406789B1 (en) | 1998-07-22 | 2002-06-18 | Borden Chemical, Inc. | Composite proppant, composite filtration media and methods for making and using same |
GB2370054A (en) | 2000-12-14 | 2002-06-19 | Halliburton Energy Serv Inc | Abrasive slurry delivery apparatus |
US6439309B1 (en) | 2000-12-13 | 2002-08-27 | Bj Services Company | Compositions and methods for controlling particulate movement in wellbores and subterranean formations |
US6528157B1 (en) | 1995-11-01 | 2003-03-04 | Borden Chemical, Inc. | Proppants with fiber reinforced resin coatings |
US6582819B2 (en) | 1998-07-22 | 2003-06-24 | Borden Chemical, Inc. | Low density composite proppant, filtration media, gravel packing media, and sports field media, and methods for making and using same |
US6626241B2 (en) | 2001-12-06 | 2003-09-30 | Halliburton Energy Services, Inc. | Method of frac packing through existing gravel packed screens |
US6632527B1 (en) | 1998-07-22 | 2003-10-14 | Borden Chemical, Inc. | Composite proppant, composite filtration media and methods for making and using same |
US20030205376A1 (en) | 2002-04-19 | 2003-11-06 | Schlumberger Technology Corporation | Means and Method for Assessing the Geometry of a Subterranean Fracture During or After a Hydraulic Fracturing Treatment |
US20030224165A1 (en) | 2002-06-03 | 2003-12-04 | Anderson Robert William | Particulate material having multiple curable coatings and methods for making and using same |
US20040040708A1 (en) | 2002-09-03 | 2004-03-04 | Stephenson Christopher John | Method of treating subterranean formations with porous ceramic particulate materials |
EP1400818A2 (en) | 2002-09-20 | 2004-03-24 | Halliburton Energy Services, Inc. | Fracture monitoring using pressure-frequency analysis |
US6732800B2 (en) | 2002-06-12 | 2004-05-11 | Schlumberger Technology Corporation | Method of completing a well in an unconsolidated formation |
US20040094300A1 (en) | 2002-08-26 | 2004-05-20 | Schlumberger Technology Corp. | Dissolving Filter Cake |
US6749025B1 (en) | 1996-11-27 | 2004-06-15 | Bj Services Company | Lightweight methods and compositions for sand control |
CN1508390A (en) | 2002-12-18 | 2004-06-30 | 宜兴东方石油支撑剂有限公司 | Solid propping agent for oil-gas well fractrue |
WO2004083600A1 (en) | 2003-03-18 | 2004-09-30 | Bj Services Company | Method of treating subterranean formations using mixed density proppants or sequential proppant stages |
US6817414B2 (en) | 2002-09-20 | 2004-11-16 | M-I Llc | Acid coated sand for gravel pack and filter cake clean-up |
US6832650B2 (en) | 2002-09-11 | 2004-12-21 | Halliburton Energy Services, Inc. | Methods of reducing or preventing particulate flow-back in wells |
WO2005000993A1 (en) | 2003-06-27 | 2005-01-06 | Halliburton Energy Services, Inc. | Compositions and methods for improving proppant pack permeability and fracture conductivity in a subterranean well |
US20050019574A1 (en) | 2003-04-15 | 2005-01-27 | Mccrary Avis Lloyd | Particulate material containing thermoplastics and methods for making and using the same |
US20050028979A1 (en) | 1996-11-27 | 2005-02-10 | Brannon Harold Dean | Methods and compositions of a storable relatively lightweight proppant slurry for hydraulic fracturing and gravel packing applications |
US20050059558A1 (en) | 2003-06-27 | 2005-03-17 | Blauch Matthew E. | Methods for improving proppant pack permeability and fracture conductivity in a subterranean well |
US20050096207A1 (en) | 2003-11-04 | 2005-05-05 | Global Synfrac Inc. | Proppants and their manufacture |
US6892813B2 (en) * | 2003-01-30 | 2005-05-17 | Halliburton Energy Services, Inc. | Methods for preventing fracture proppant flowback |
WO2005095202A1 (en) | 2004-03-22 | 2005-10-13 | Meissner Joerg | Swimming aid |
CN1730422A (en) | 2005-07-13 | 2006-02-08 | 攀枝花环业冶金渣开发有限责任公司 | High titanium type petroleum oil pressing crack propping agent and production method thereof |
US20060035790A1 (en) | 2004-08-16 | 2006-02-16 | Fairmount Minerals, Ltd. | Control of particulate flowback in subterranean formations using elastomeric resin coated proppants |
US20060037755A1 (en) | 2004-08-17 | 2006-02-23 | Knobloch Charles S | Solid state pump |
WO2006034298A2 (en) | 2004-09-20 | 2006-03-30 | Hexion Specialty Chemicals Inc. | Particles for use as proppants or in gravel packs, methods for making and using the same |
US20060146643A1 (en) | 2003-04-30 | 2006-07-06 | Allen Thomas E | Gel mixing system |
US7073581B2 (en) | 2004-06-15 | 2006-07-11 | Halliburton Energy Services, Inc. | Electroconductive proppant compositions and related methods |
GB2426023A (en) | 2005-05-12 | 2006-11-15 | Bj Services Co | Structured composite compositions for well treatment |
US20070054121A1 (en) | 2005-02-25 | 2007-03-08 | Weintritt Donald J | Graphite coating of particulate materials |
US7244492B2 (en) | 2004-03-04 | 2007-07-17 | Fairmount Minerals, Ltd. | Soluble fibers for use in resin coated proppant |
US20080011477A1 (en) | 2006-07-12 | 2008-01-17 | Richard Rediger | Well treating materials and methods |
WO2008033225A2 (en) | 2006-09-13 | 2008-03-20 | Hexion Specialty Chemicals Inc. | Logging device with down-hole transceiver for operation in extreme temperatures |
US20080202750A1 (en) | 2006-07-12 | 2008-08-28 | Georgia-Pacific Chemicals Llc | Proppant materials and methods |
US20080277115A1 (en) | 2007-05-11 | 2008-11-13 | Georgia-Pacific Chemicals Llc | Increasing buoyancy of well treating materials |
US20080283243A1 (en) | 2007-05-15 | 2008-11-20 | Georgia-Pacific Chemicals Llc | Reducing flow-back in well treating materials |
US7491444B2 (en) | 2005-02-04 | 2009-02-17 | Oxane Materials, Inc. | Composition and method for making a proppant |
US7624802B2 (en) * | 2007-03-22 | 2009-12-01 | Hexion Specialty Chemicals, Inc. | Low temperature coated particles for use as proppants or in gravel packs, methods for making and using the same |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6439789B1 (en) * | 2000-09-27 | 2002-08-27 | Closure Medical Corporation | Polymerizable 1, 1-disubstituted ethylene monomer formulation applicators, applicator tips, applicator kits and methods |
AU2001283114A1 (en) * | 2001-07-03 | 2003-02-17 | Scapa Tapes North America, Inc. | Heat-activated adhesive tape having an acrylic foam-like backing |
US7797400B2 (en) * | 2006-09-06 | 2010-09-14 | Oracle International Corporation | Computer-implemented methods and systems for testing the interoperability of web services |
-
2008
- 2008-03-06 US US12/043,818 patent/US8133587B2/en not_active Expired - Fee Related
-
2009
- 2009-03-06 WO PCT/US2009/036326 patent/WO2009111697A1/en active Application Filing
Patent Citations (118)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3815680A (en) * | 1971-04-09 | 1974-06-11 | Continental Oil Co | Method for fracturing and propping unconsolidated and dilatant subterranean formations |
US3929191A (en) | 1974-08-15 | 1975-12-30 | Exxon Production Research Co | Method for treating subterranean formations |
US4073343A (en) | 1976-12-23 | 1978-02-14 | Texaco Inc. | Sand consolidation method |
CA1057649A (en) | 1977-06-20 | 1979-07-03 | Donald S. Black | Formation fracturing with foam having greater proppant concentration |
US4160483A (en) | 1978-07-21 | 1979-07-10 | The Dow Chemical Company | Method of treating a well using fluoboric acid to clean a propped fracture |
US4183813A (en) | 1978-11-15 | 1980-01-15 | Palmer Engineering Company Ltd. | Mixture concentrator |
US4222444A (en) | 1978-12-06 | 1980-09-16 | Hamilton Harold L | Method of well fluid leak prevention |
GB2050467A (en) | 1979-06-07 | 1981-01-07 | Perlman W | Fracturing Subterranean Formations |
US4336842A (en) | 1981-01-05 | 1982-06-29 | Graham John W | Method of treating wells using resin-coated particles |
US4547468A (en) | 1981-08-10 | 1985-10-15 | Terra Tek, Inc. | Hollow proppants and a process for their manufacture |
US4439489A (en) | 1982-02-16 | 1984-03-27 | Acme Resin Corporation | Particles covered with a cured infusible thermoset film and process for their production |
CA1202882A (en) | 1982-03-01 | 1986-04-08 | Owen Richmond | Method of removing gas from an underground seam |
CA1185778A (en) | 1982-07-12 | 1985-04-23 | Brian R. Ainley | Stable foams and methods of use |
US4518040A (en) | 1983-06-29 | 1985-05-21 | Halliburton Company | Method of fracturing a subterranean formation |
US4527627A (en) | 1983-07-28 | 1985-07-09 | Santrol Products, Inc. | Method of acidizing propped fractures |
US4493875A (en) | 1983-12-09 | 1985-01-15 | Minnesota Mining And Manufacturing Company | Proppant for well fractures and method of making same |
US4569394A (en) | 1984-02-29 | 1986-02-11 | Hughes Tool Company | Method and apparatus for increasing the concentration of proppant in well stimulation techniques |
US4585064A (en) | 1984-07-02 | 1986-04-29 | Graham John W | High strength particulates |
US4888240A (en) | 1984-07-02 | 1989-12-19 | Graham John W | High strength particulates |
EP0169412A1 (en) | 1984-07-05 | 1986-01-29 | Norton Company | Proppant for oil and gas wells |
US4665990A (en) | 1984-07-17 | 1987-05-19 | William Perlman | Multiple-stage coal seam fracing method |
EP0308257A2 (en) | 1987-09-17 | 1989-03-22 | Minnesota Mining And Manufacturing Company | Novolac coated ceramic particulate |
US4923714A (en) | 1987-09-17 | 1990-05-08 | Minnesota Mining And Manufacturing Company | Novolac coated ceramic particulate |
US4869960A (en) | 1987-09-17 | 1989-09-26 | Minnesota Mining And Manufacturing Company | Epoxy novolac coated ceramic particulate |
US4852650A (en) | 1987-12-28 | 1989-08-01 | Mobil Oil Corporation | Hydraulic fracturing with a refractory proppant combined with salinity control |
US5188175A (en) | 1989-08-14 | 1993-02-23 | Carbo Ceramics Inc. | Method of fracturing a subterranean formation with a lightweight propping agent |
US5005641A (en) | 1990-07-02 | 1991-04-09 | Mohaupt Henry H | Gas generator with improved ignition assembly |
US5318382A (en) | 1990-10-25 | 1994-06-07 | Cahill Calvin D | Method and apparatus for hydraulic embedment of waste in subterranean formations |
US5128390A (en) | 1991-01-22 | 1992-07-07 | Halliburton Company | Methods of forming consolidatable resin coated particulate materials in aqueous gels |
US5217074A (en) | 1991-10-29 | 1993-06-08 | Exxon Chemical Patents Inc. | Method of fracturing formations |
US5370184A (en) | 1991-10-29 | 1994-12-06 | Exxon Chemical Patents Inc. | Method of treating formations |
US5728302A (en) | 1992-04-09 | 1998-03-17 | Groundwater Services, Inc. | Methods for the removal of contaminants from subterranean fluids |
US5311946A (en) | 1992-08-04 | 1994-05-17 | Benchmark Research And Technology, Inc. | Method and process for the stabilization of resin coated particulates |
US5316792A (en) | 1992-08-04 | 1994-05-31 | Benchmark Research And Technology, Inc. | Method and process for the stabilization of resin coated particulates |
US5425994A (en) | 1992-08-04 | 1995-06-20 | Technisand, Inc. | Resin coated particulates comprissing a formaldehyde source-metal compound (FS-MC) complex |
US5520250A (en) | 1992-08-04 | 1996-05-28 | Technisand, Inc. | Method and process for the stabilization of resin coated particulates |
US5330005A (en) | 1993-04-05 | 1994-07-19 | Dowell Schlumberger Incorporated | Control of particulate flowback in subterranean wells |
US5439055A (en) | 1993-04-05 | 1995-08-08 | Dowell, A Division Of Schlumberger Technology Corp. | Control of particulate flowback in subterranean wells |
US5501275A (en) | 1993-04-05 | 1996-03-26 | Dowell, A Division Of Schlumberger Technology Corporation | Control of particulate flowback in subterranean wells |
US5422183A (en) | 1993-06-01 | 1995-06-06 | Santrol, Inc. | Composite and reinforced coatings on proppants and particles |
US5492178A (en) | 1993-11-12 | 1996-02-20 | Halliburton Company | Well treating methods and devices using particulate blends |
US5411093A (en) | 1993-12-10 | 1995-05-02 | Mobil Oil Corporation | Method of enhancing stimulation load fluid recovery |
US5955144A (en) | 1994-07-21 | 1999-09-21 | Sanatrol, Inc. | Well treatment fluid compatible self-consolidation particles |
US5837656A (en) | 1994-07-21 | 1998-11-17 | Santrol, Inc. | Well treatment fluid compatible self-consolidating particles |
US5948734A (en) | 1994-07-21 | 1999-09-07 | Sanatrol, Inc. | Well treatment fluid compatible self-consolidating particles |
US5656176A (en) | 1994-09-23 | 1997-08-12 | Scott; Gregory D. | Method of filtering a subterranean fluid from a well bore using a resin bonded well liner |
US5500174A (en) | 1994-09-23 | 1996-03-19 | Scott; Gregory D. | Method of manufacture of a prepacked resin bonded well liner |
US5964291A (en) | 1995-02-28 | 1999-10-12 | Aea Technology Plc | Well treatment |
US5639806A (en) | 1995-03-28 | 1997-06-17 | Borden Chemical, Inc. | Bisphenol-containing resin coating articles and methods of using same |
US5916933A (en) | 1995-03-28 | 1999-06-29 | Borden Chemical, Inc. | Bisphenol-containing resin coating articles and methods of using same |
US6047772A (en) | 1995-03-29 | 2000-04-11 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US6209643B1 (en) | 1995-03-29 | 2001-04-03 | Halliburton Energy Services, Inc. | Method of controlling particulate flowback in subterranean wells and introducing treatment chemicals |
US5787986A (en) | 1995-03-29 | 1998-08-04 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5839510A (en) | 1995-03-29 | 1998-11-24 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5853048A (en) | 1995-03-29 | 1998-12-29 | Halliburton Energy Services, Inc. | Control of fine particulate flowback in subterranean wells |
US5775425A (en) | 1995-03-29 | 1998-07-07 | Halliburton Energy Services, Inc. | Control of fine particulate flowback in subterranean wells |
US5501274A (en) | 1995-03-29 | 1996-03-26 | Halliburton Company | Control of particulate flowback in subterranean wells |
US5833000A (en) | 1995-03-29 | 1998-11-10 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US5582249A (en) | 1995-08-02 | 1996-12-10 | Halliburton Company | Control of particulate flowback in subterranean wells |
US5929437A (en) | 1995-08-18 | 1999-07-27 | Protechnics International, Inc. | Encapsulated radioactive tracer |
US5578371A (en) | 1995-08-25 | 1996-11-26 | Schuller International, Inc. | Phenol/formaldehyde fiberglass binder compositions exhibiting reduced emissions |
US6528157B1 (en) | 1995-11-01 | 2003-03-04 | Borden Chemical, Inc. | Proppants with fiber reinforced resin coatings |
US5697440A (en) | 1996-01-04 | 1997-12-16 | Halliburton Energy Services, Inc. | Control of particulate flowback in subterranean wells |
US6749025B1 (en) | 1996-11-27 | 2004-06-15 | Bj Services Company | Lightweight methods and compositions for sand control |
US20050028979A1 (en) | 1996-11-27 | 2005-02-10 | Brannon Harold Dean | Methods and compositions of a storable relatively lightweight proppant slurry for hydraulic fracturing and gravel packing applications |
US6059034A (en) | 1996-11-27 | 2000-05-09 | Bj Services Company | Formation treatment method using deformable particles |
US6330916B1 (en) | 1996-11-27 | 2001-12-18 | Bj Services Company | Formation treatment method using deformable particles |
US6364018B1 (en) | 1996-11-27 | 2002-04-02 | Bj Services Company | Lightweight methods and compositions for well treating |
US6017854A (en) | 1997-05-28 | 2000-01-25 | Union Oil Company Of California | Simplified mud systems |
US6114410A (en) | 1998-07-17 | 2000-09-05 | Technisand, Inc. | Proppant containing bondable particles and removable particles |
US6406789B1 (en) | 1998-07-22 | 2002-06-18 | Borden Chemical, Inc. | Composite proppant, composite filtration media and methods for making and using same |
US6582819B2 (en) | 1998-07-22 | 2003-06-24 | Borden Chemical, Inc. | Low density composite proppant, filtration media, gravel packing media, and sports field media, and methods for making and using same |
US6632527B1 (en) | 1998-07-22 | 2003-10-14 | Borden Chemical, Inc. | Composite proppant, composite filtration media and methods for making and using same |
US6116342A (en) | 1998-10-20 | 2000-09-12 | Halliburton Energy Services, Inc. | Methods of preventing well fracture proppant flow-back |
US6439309B1 (en) | 2000-12-13 | 2002-08-27 | Bj Services Company | Compositions and methods for controlling particulate movement in wellbores and subterranean formations |
GB2370054A (en) | 2000-12-14 | 2002-06-19 | Halliburton Energy Serv Inc | Abrasive slurry delivery apparatus |
US6626241B2 (en) | 2001-12-06 | 2003-09-30 | Halliburton Energy Services, Inc. | Method of frac packing through existing gravel packed screens |
US20030205376A1 (en) | 2002-04-19 | 2003-11-06 | Schlumberger Technology Corporation | Means and Method for Assessing the Geometry of a Subterranean Fracture During or After a Hydraulic Fracturing Treatment |
US7153575B2 (en) | 2002-06-03 | 2006-12-26 | Borden Chemical, Inc. | Particulate material having multiple curable coatings and methods for making and using same |
US20030224165A1 (en) | 2002-06-03 | 2003-12-04 | Anderson Robert William | Particulate material having multiple curable coatings and methods for making and using same |
US6732800B2 (en) | 2002-06-12 | 2004-05-11 | Schlumberger Technology Corporation | Method of completing a well in an unconsolidated formation |
US20040094300A1 (en) | 2002-08-26 | 2004-05-20 | Schlumberger Technology Corp. | Dissolving Filter Cake |
US20040040708A1 (en) | 2002-09-03 | 2004-03-04 | Stephenson Christopher John | Method of treating subterranean formations with porous ceramic particulate materials |
US7426961B2 (en) | 2002-09-03 | 2008-09-23 | Bj Services Company | Method of treating subterranean formations with porous particulate materials |
US20040200617A1 (en) | 2002-09-03 | 2004-10-14 | Stephenson Christopher John | Method of treating subterranean formations with porous ceramic particulate materials |
US7713918B2 (en) * | 2002-09-03 | 2010-05-11 | Bj Services Company | Porous particulate materials and compositions thereof |
US6832650B2 (en) | 2002-09-11 | 2004-12-21 | Halliburton Energy Services, Inc. | Methods of reducing or preventing particulate flow-back in wells |
EP1400818A2 (en) | 2002-09-20 | 2004-03-24 | Halliburton Energy Services, Inc. | Fracture monitoring using pressure-frequency analysis |
US6817414B2 (en) | 2002-09-20 | 2004-11-16 | M-I Llc | Acid coated sand for gravel pack and filter cake clean-up |
CN1508390A (en) | 2002-12-18 | 2004-06-30 | 宜兴东方石油支撑剂有限公司 | Solid propping agent for oil-gas well fractrue |
US6892813B2 (en) * | 2003-01-30 | 2005-05-17 | Halliburton Energy Services, Inc. | Methods for preventing fracture proppant flowback |
US7210528B1 (en) | 2003-03-18 | 2007-05-01 | Bj Services Company | Method of treatment subterranean formations using multiple proppant stages or mixed proppants |
WO2004083600A1 (en) | 2003-03-18 | 2004-09-30 | Bj Services Company | Method of treating subterranean formations using mixed density proppants or sequential proppant stages |
US7270879B2 (en) | 2003-04-15 | 2007-09-18 | Hexion Specialty Chemicals, Inc. | Particulate material containing thermoplastics and methods for making and using the same |
US20050019574A1 (en) | 2003-04-15 | 2005-01-27 | Mccrary Avis Lloyd | Particulate material containing thermoplastics and methods for making and using the same |
US20060146643A1 (en) | 2003-04-30 | 2006-07-06 | Allen Thomas E | Gel mixing system |
US20050059558A1 (en) | 2003-06-27 | 2005-03-17 | Blauch Matthew E. | Methods for improving proppant pack permeability and fracture conductivity in a subterranean well |
WO2005000993A1 (en) | 2003-06-27 | 2005-01-06 | Halliburton Energy Services, Inc. | Compositions and methods for improving proppant pack permeability and fracture conductivity in a subterranean well |
US20050096207A1 (en) | 2003-11-04 | 2005-05-05 | Global Synfrac Inc. | Proppants and their manufacture |
US7244492B2 (en) | 2004-03-04 | 2007-07-17 | Fairmount Minerals, Ltd. | Soluble fibers for use in resin coated proppant |
WO2005095202A1 (en) | 2004-03-22 | 2005-10-13 | Meissner Joerg | Swimming aid |
US7073581B2 (en) | 2004-06-15 | 2006-07-11 | Halliburton Energy Services, Inc. | Electroconductive proppant compositions and related methods |
US20060035790A1 (en) | 2004-08-16 | 2006-02-16 | Fairmount Minerals, Ltd. | Control of particulate flowback in subterranean formations using elastomeric resin coated proppants |
US20060037755A1 (en) | 2004-08-17 | 2006-02-23 | Knobloch Charles S | Solid state pump |
US20060078682A1 (en) | 2004-09-20 | 2006-04-13 | Mcdaniel Robert R | Particles for use as proppants or in gravel packs, methods for making and using the same |
WO2006034298A2 (en) | 2004-09-20 | 2006-03-30 | Hexion Specialty Chemicals Inc. | Particles for use as proppants or in gravel packs, methods for making and using the same |
US7491444B2 (en) | 2005-02-04 | 2009-02-17 | Oxane Materials, Inc. | Composition and method for making a proppant |
US20070054121A1 (en) | 2005-02-25 | 2007-03-08 | Weintritt Donald J | Graphite coating of particulate materials |
GB2426023A (en) | 2005-05-12 | 2006-11-15 | Bj Services Co | Structured composite compositions for well treatment |
CN1730422A (en) | 2005-07-13 | 2006-02-08 | 攀枝花环业冶金渣开发有限责任公司 | High titanium type petroleum oil pressing crack propping agent and production method thereof |
US20080011477A1 (en) | 2006-07-12 | 2008-01-17 | Richard Rediger | Well treating materials and methods |
US20080202750A1 (en) | 2006-07-12 | 2008-08-28 | Georgia-Pacific Chemicals Llc | Proppant materials and methods |
US8003214B2 (en) * | 2006-07-12 | 2011-08-23 | Georgia-Pacific Chemicals Llc | Well treating materials comprising coated proppants, and methods |
WO2008033225A2 (en) | 2006-09-13 | 2008-03-20 | Hexion Specialty Chemicals Inc. | Logging device with down-hole transceiver for operation in extreme temperatures |
US7624802B2 (en) * | 2007-03-22 | 2009-12-01 | Hexion Specialty Chemicals, Inc. | Low temperature coated particles for use as proppants or in gravel packs, methods for making and using the same |
US20080277115A1 (en) | 2007-05-11 | 2008-11-13 | Georgia-Pacific Chemicals Llc | Increasing buoyancy of well treating materials |
US20080283243A1 (en) | 2007-05-15 | 2008-11-20 | Georgia-Pacific Chemicals Llc | Reducing flow-back in well treating materials |
US7754659B2 (en) * | 2007-05-15 | 2010-07-13 | Georgia-Pacific Chemicals Llc | Reducing flow-back in well treating materials |
Non-Patent Citations (11)
Title |
---|
"Density of Various solids", CRC Handbook of Chemistry and Physics, 90th edition, 2009-2010, section 15, p. 39. |
Advances in Coalbed Methane, Hart Energy Publications, Chemical Week Associates, May 2003. |
Conductivity Endurance Technology, Top Technology Solutions 2006, 2006 Halliburton, H04898, Apr. 2006. |
COOL-LOK 250F Hot Melt, National Starch & Chemicals, 2000. |
International Search Report and Written Opinion of the International Searching Authority for PCT/US08/62890, mailed Aug. 1, 2008, six pages, European Patent Office, Rijswijk, Netherlands. |
International Search Report and Written Opinion of the International Searching Authority for PCT/US08/63055, mailed Aug. 13, 2008, seven pages, European Patent Office, Rijswijk, Netherlands. |
International Search Report and Written Opinion of the International Searching Authority for PCT/US09/36326, mailed Jun. 26, 2009, nine pages, European Patent Office, Rijswijk, Netherlands. |
International Search Report for PCT/US2007/072212 mailed on Nov. 27, 2007. |
International Search Report for PCT/US2008/062890, mailed Sep. 1, 2008, European Patent Office, Rijswijk, Netherlands. |
International Search Report for PCT/US2008/063055, mailed Sep. 2, 2008, European Patent Office, Rijswijk, Netherlands. |
Written Opinion of the International Searching Authority for PCT/US07/72212, mailed Nov. 27, 2007, six pages, European Patent Office, Rijswijk, Netherlands. |
Cited By (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10544358B2 (en) | 2011-05-03 | 2020-01-28 | Preferred Technology, Llc | Coated and cured proppants |
US9725645B2 (en) | 2011-05-03 | 2017-08-08 | Preferred Technology, Llc | Proppant with composite coating |
US9624421B2 (en) | 2011-09-02 | 2017-04-18 | Preferred Technology, Llc | Dual function proppants |
US10087360B2 (en) | 2011-09-02 | 2018-10-02 | Preferred Technology, Llc | Dual function proppants |
US9562187B2 (en) | 2012-01-23 | 2017-02-07 | Preferred Technology, Llc | Manufacture of polymer coated proppants |
US10208242B2 (en) | 2013-03-15 | 2019-02-19 | Preferred Technology, Llc | Proppant with polyurea-type coating |
US9518214B2 (en) | 2013-03-15 | 2016-12-13 | Preferred Technology, Llc | Proppant with polyurea-type coating |
US10100247B2 (en) | 2013-05-17 | 2018-10-16 | Preferred Technology, Llc | Proppant with enhanced interparticle bonding |
US11760924B2 (en) | 2013-05-17 | 2023-09-19 | Preferred Technology, Llc | Proppant with enhanced interparticle bonding |
US11098242B2 (en) | 2013-05-17 | 2021-08-24 | Preferred Technology, Llc | Proppant with enhanced interparticle bonding |
US9260651B2 (en) | 2014-03-28 | 2016-02-16 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US10508231B2 (en) | 2014-03-28 | 2019-12-17 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US9969929B2 (en) | 2014-03-28 | 2018-05-15 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US10435624B2 (en) | 2014-03-28 | 2019-10-08 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US10731074B2 (en) | 2014-03-28 | 2020-08-04 | Arr-Maz Products, L.P. | Attrition resistant proppant composite and its composition matters |
US9790422B2 (en) | 2014-04-30 | 2017-10-17 | Preferred Technology, Llc | Proppant mixtures |
US11352553B2 (en) | 2014-11-18 | 2022-06-07 | Powdermet, Inc. | Polymer coated proppant |
WO2016081220A1 (en) * | 2014-11-18 | 2016-05-26 | Powdermet, Inc. | Polymer coated proppant |
US11149191B2 (en) | 2014-11-18 | 2021-10-19 | Terves, Llc | Polymer coated proppant |
US10138417B2 (en) | 2014-12-05 | 2018-11-27 | Dow Global Technologies Llc | Proppant comprising an oil well treatment agent coating |
WO2016089599A1 (en) | 2014-12-05 | 2016-06-09 | Dow Global Technologies Llc | Proppant comprising an oil well treatment agent coating |
WO2016140813A1 (en) | 2015-03-04 | 2016-09-09 | Covestro Llc | Proppant sand coating for dust reduction |
US9896620B2 (en) | 2015-03-04 | 2018-02-20 | Covestro Llc | Proppant sand coating for dust reduction |
US10590337B2 (en) | 2015-05-13 | 2020-03-17 | Preferred Technology, Llc | High performance proppants |
US9862881B2 (en) | 2015-05-13 | 2018-01-09 | Preferred Technology, Llc | Hydrophobic coating of particulates for enhanced well productivity |
US10000691B2 (en) | 2015-06-08 | 2018-06-19 | Halliburton Energy Services, Inc. | Variably tacky proppants |
WO2017058762A1 (en) | 2015-09-29 | 2017-04-06 | Georgia-Pacific Chemicals Llc | Proppants coated with a resin containing a clay |
US10281380B1 (en) | 2016-06-17 | 2019-05-07 | Matthew D. Bryant | Method for testing a proppant |
US10845281B1 (en) | 2016-06-17 | 2020-11-24 | Matthew D. Bryant | Method for testing a proppant |
US11686657B1 (en) | 2016-06-17 | 2023-06-27 | True Crush Testing, Llc | Method for testing a proppant |
US11208591B2 (en) | 2016-11-16 | 2021-12-28 | Preferred Technology, Llc | Hydrophobic coating of particulates for enhanced well productivity |
US10696896B2 (en) | 2016-11-28 | 2020-06-30 | Prefferred Technology, Llc | Durable coatings and uses thereof |
WO2018177619A1 (en) | 2017-03-30 | 2018-10-04 | Clariant International Ltd | Fluids for fracking of paraffinic oil bearing formations |
Also Published As
Publication number | Publication date |
---|---|
US20080202750A1 (en) | 2008-08-28 |
WO2009111697A1 (en) | 2009-09-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8133587B2 (en) | Proppant materials comprising a coating of thermoplastic material, and methods of making and using | |
US7244492B2 (en) | Soluble fibers for use in resin coated proppant | |
CA2685839C (en) | Increasing buoyancy of well treating materials | |
US6372678B1 (en) | Proppant composition for gas and oil well fracturing | |
US9845428B2 (en) | Proppants for hydraulic fracturing technologies | |
RU2344040C2 (en) | Material particles containing thermoplastic elastomer, methods of their obtainment and application | |
CA2685193C (en) | Reducing flow-back in well treating materials | |
AU2010245158B2 (en) | Methods for making and using UV/EB cured precured particles for use as proppants | |
US20060035790A1 (en) | Control of particulate flowback in subterranean formations using elastomeric resin coated proppants | |
US4518039A (en) | Method for treating subterranean formations | |
US8003214B2 (en) | Well treating materials comprising coated proppants, and methods | |
CN102167969A (en) | Low temperature coated particles for use as proppants or in gravel packs, methods for making and using the same. | |
CA2708166A1 (en) | Fracturing fluid compositions comprising solid epoxy particles and methods of use | |
CN101641211A (en) | Low temperature coated particles for use as proppants or in gravel packs, methods for making and using the same | |
WO2002026656A1 (en) | Proppant composition for gas and oil-well fracturing | |
RU2395474C1 (en) | Polymer-coated proppant | |
DK181044B1 (en) | Flowback resistant proppants | |
US8273406B1 (en) | Particulate solid coated with a curable resin | |
US4116708A (en) | Asphalt coating compositions | |
RU2388787C1 (en) | Proppant manufacturing method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: GEORGIA-PACIFIC CHEMICALS LLC, GEORGIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:REDIGER, RICHARD;ARON, MICHAEL J.;FENNELL, BEDFORD W.;AND OTHERS;REEL/FRAME:020933/0033;SIGNING DATES FROM 20080414 TO 20080430 Owner name: GEORGIA-PACIFIC CHEMICALS LLC,GEORGIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:REDIGER, RICHARD;ARON, MICHAEL J.;FENNELL, BEDFORD W.;AND OTHERS;SIGNING DATES FROM 20080414 TO 20080430;REEL/FRAME:020933/0033 Owner name: GEORGIA-PACIFIC CHEMICALS LLC, GEORGIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:REDIGER, RICHARD;ARON, MICHAEL J.;FENNELL, BEDFORD W.;AND OTHERS;SIGNING DATES FROM 20080414 TO 20080430;REEL/FRAME:020933/0033 |
|
STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
FPAY | Fee payment |
Year of fee payment: 4 |
|
FEPP | Fee payment procedure |
Free format text: MAINTENANCE FEE REMINDER MAILED (ORIGINAL EVENT CODE: REM.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
LAPS | Lapse for failure to pay maintenance fees |
Free format text: PATENT EXPIRED FOR FAILURE TO PAY MAINTENANCE FEES (ORIGINAL EVENT CODE: EXP.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
|
FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20200313 |