Resin compositions and methods of using resin compositions to control proppant flow-back
a technology of resin composition and flow-back, which is applied in the direction of drilling composition, chemistry apparatus and processes, and well accessories, etc., can solve the problems of inability to hardenable resin composition, inability to control the flow-back of proppant or formation fluid, and inability to harden resin composition, etc., to achieve the effect of improving the conductivity of subterranean formations, improving resin compositions and resin-coated proppants, and improving the conductivity of subterran
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example 1
[0025] A resin of the present invention was prepared by mixing 0.75 mL of phenol, 6.1 mL of phenol formaldehyde, 2.55 mL of furfuryl alcohol, 0.1 mL of silane coupling agent n-beta-(aminoethyl)-gamma-aminopropyl trimethoxysilane, and 0.5 mL of an alkyl phosphonate surfactant. A volume of 7.5 mL of the resin mixture was then coated onto 250 grams of 20 / 40-mesh bauxite proppant. The coated proppant was then mixed with 300 mL of a fracturing fluid using carboxymethylhydroxypropyl guar as the gelling base. That gelled fluid was cross-linked with a zirconium cross-linker. The resulting viscous fracturing fluid comprising resin-coated proppant was stirred in a heated bath for 1 hour at 175° F. before being packed in brass flow cells. No closure stress was exerted on the cells and they were allowed to cure in an oven at various temperatures and for various lengths of time. Consolidated cores were obtained from the proppant packs to determine the unconsolidated compressive strength (UCS). T...
example 2
[0027] A modified API conductivity flow cell was used to perform proppant flowback testing to determine the effectiveness of the resin of the present invention in controlling proppant flowback. The conductivity flow cell was modified in that a 0.5-inch hole was installed a one end of the flow cell to simulate a perforation and a wire-mesh screen was initially inserted in the perforation to prevent production of the proppant. Ceramic proppant of 20 / 40-mesh was coated with 3% resin by weight of the proppant. The resin composition used was identical to that described in Example 1. The resin-coated proppant was then slurried into a viscous fracturing fluid as described in Example 1. The proppant slurry was packed into the modified conductivity cell to a loading of 2 lb / ft2 and set at an initial closure stress of 2,000 psi and a temperature of 150° F. After 2 hours, the temperature of the cell was increased to 300° F. and after 6 hours the closure stress was increased to 6,000 psi. The c...
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Abstract
Description
Claims
Application Information
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