Page 194 - A Practical Companion to Reservoir Stimulation
P. 194

PRACTICAL CONSIDERATIONS FOR FRACTURE TREATMENT DESIGN




            P-3.5: Viscosity Reduction from Breakers
            Breakers are added to fracturing fluids for two reasons. First,   100
            the viscosity of the fluid must be reduced so that the fluid can
            be  cleaned  up  quickly  following  a  treatment.  Second,  as   90
            demonstrated in  Section P-3.4,  the breaker should also de-    80
            grade the fluid and thus reduce proppant-conductivity dam-
            age. All common breakers perform both these tasks by attack-    70
            ing the backbone of the polymer and reducing its size.  As the
            molecular  weight  of  the  polymers  decreases,  so does  the   60
            fluid's  viscosity.                                             50
              Several systems are currently used  to break  water-base
            fracturing fluids. Table P-8 shows the concentration of con-    40
            ventional breaker systems needed to break linear fluids when    30
            the  well  can  be  shut in for 24 hr.  Enzyme breakys can be
            effective over a relatively  wide temperature range (70°F to    20
            150°F) but are limited to a pH range between 3.5 and 8. The
            optimum pH for most enzyme breakers is 5. Oxidizing breakers    10
            are  used  in  applications  where  the  fluid  is  exposed  to   0
            bottomhole temperatures between  125°F and  225°F. These             Persulfate/  Enzyme
            breakers can be expanded into lower temperature applications           Amine     Breaker
            (60°F to 125°F) if an amine is concurrently added to catalyze          Breaker
            the reaction. These breakers are effective over a wide pH
            range (3 to 14) and demonstrate superior breaking properties
            based on observed proppant-permeability reduction.  This is   Figure P-42-Retained  conductivity of a 40 Ib/lOOO gal
            especially true when the oxidative breaker reaction is catalyzed   borate-crosslinked fluid with two types of breakers (from
            by the amine (see Fig. P-42).                        STIMLAB, 1988).





















                          1          I          I          I          I         I          I          I
            I    140      I   0.06   I   0.175  I   0.1    I   0.375  I   0.15   I   0.375  I   0.2   I   0.55   I
                 160          0.06      0.08        0.1       0.2        0.15       0.375      0.2       0.55

                 180                    0.075                 0.1 5                 0.275                0.425
                 200                    0.075                 0.15                  0.2                  0.3




            Table P-8-Breaker  concentrations (Ib/l000 gal of fluid) for breaking a linear fluid in 24 hr. Data applicable for guar, HPG,
            HEC, CMC and CMHEC for the polymer loadings shown (from Gidley et al., RecentAdvances in Hydraulic Fracturing, SPE
            Monograph Vol.  12, 1990).


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