OXIDATIVE BREAKERS IN A SILICONE BASED SUSPENSION
An oxidative breaker system for use in reducing the viscosity of a guar-based suspension includes a silicone oil carrier fluid, an oxidizer and a suspension aid. The suspension aid is preferably fumed silica. The oxidizer may be selected from the group consisting of alkali metal peroxide, transition metal peroxide, persulfate, bromide and bromate. In highly preferred embodiments, the oxidizer is magnesium peroxide or calcium peroxide. Also disclosed is a method for breaking a guar-based suspension with the inventive oxidative breaker system.
1 . An oxidative breaker system for use in reducing the viscosity of a polysaccharide-based suspension, the oxidative breaker system comprising:
a carrier fluid, wherein the carrier fluid is a silicone oil; and
an oxidizer mixed within the carrier fluid.
2 . The oxidative breaker system of claim 1 , wherein the silicone oil is a polymerized siloxane with organic side chains.
3 . The oxidative breaker system of claim 2 , wherein the silicone oil is a polydimethylsiloxanes.
4 . The oxidative breaker system of claim 3 , wherein the silicone oil is a medium viscosity polydimethylsiloxanes having a base viscosity of between about 50 mm 2 /s to about 1000 mm 2 /s.
5 . The oxidative breaker system of claim 4 , wherein the silicone oil is a medium viscosity polydimethylsiloxanes having a base viscosity of between about 350 mm 2 /s.
6 . The oxidative breaker system of claim 1 , further comprising a suspension aid, wherein the suspension aid comprises fumed silica.
7 . The oxidative breaker system of claim 1 , wherein the oxidizer is selected from the group consisting of alkali metal peroxide, transition metal peroxide, persulfate, bromide and bromate.
8 . The oxidative breaker system of claim 7 , wherein the oxidizer is magnesium peroxide.
9 . The oxidative breaker system of claim 8 , further comprising:
about 50% to about 70% by weight silicone oil;
about 30% to about 45% by weight magnesium peroxide; and
about 0% to about 2% by weight fumed silica.
10 . The oxidative breaker system of claim 9 , further comprising:
about 54% by weight silicone oil;
about 45% by weight magnesium peroxide; and
about 1% by weight fumed silica.
11 . The oxidative breaker system of claim 7 , wherein the oxidizer is calcium peroxide.
12 . The oxidative breaker system of claim 11 , further comprising:
about 55% to about 70% by weight silicone oil;
about 25% to about 45% by weight calcium peroxide; and
about 0% to about 2% by weight fumed silica.
13 . The oxidative breaker system of claim 12 , further comprising:
about 64% by weight silicone oil;
about 36% by weight calcium peroxide; and
about 0.4% by weight fumed silica.
14 . A method for reducing the viscosity of a polysaccharide-based fluid in a downhole environment, the method comprising the steps:
providing an oxidative breaker system, wherein the step of providing an oxidative breaker system comprises the step of mixing an oxidizer with a suspension aid in a silicone oil carrier fluid;
placing the oxidative breaker system in contact with the polysaccharide-based fluid; and
oxidizing the polysaccharide-based fluid with the oxidative breaker system to reduce the viscosity of the polysaccharide-based fluid.
15 . The method of claim 14 , wherein the step of providing an oxidative breaker system comprises the step of mixing an oxidizer with a suspension aid in a polydimethylsiloxane carrier fluid.
16 . The method of claim 14 , wherein the step of providing an oxidative breaker system comprises the step of mixing an oxidizer with fumed silica in a silicone oil carrier fluid.
17 . The method of claim 14 , wherein the step of providing an oxidative breaker system comprises the step of mixing magnesium peroxide with a suspension aid in a silicone oil carrier fluid.
18 . The method of claim 14 , wherein the step of providing an oxidative breaker system comprises the step of mixing calcium peroxide with a suspension aid in a silicone oil carrier fluid.
19 . The method of claim 14 , wherein the step of placing the oxidative breaker system in contact with the polysaccharide-based fluid comprises placing between about 2 and 4 gallons of the oxidative breaker system to every thousand gallons of polysaccharide-based fluid.