Fracpacks have become the completion of choice for deepwater wells due to concerns over loss of productivity associated with fines and sand production, limited rig availability and high intervention / sidetracking costs. Many deepwater reservoirs also require seawater injection in order to maintain reservoir pressure and increase the ultimate recovery of hydrocarbon reserves. This practice can significantly increase the potential for scaling, particularly the deposition of barium sulphate (BaSO 4 ) scale in reservoirs with high barium concentrations. Mechanical removal of sulphate scale at the reservoir level and / or from a damaged fracpack is not feasible. Chemical dissolution is not always practical, particularly in cases of high scale buildup. In these circumstances, little can be done to restore loss production except for pulling the completion or sidetracking the well. In either case, the consequences of sulphate scale build-up can be detrimental to the economics of the project, especially for high rate producer wells. For these reasons, preemptive scale management, most often in the form of scale squeezes, is a standard operating practice in high value wells susceptible to scaling. Deployment of a scale inhibitor concurrently with well completion operations is very attractive in that it delays the onset of scaling while providing a means for scale inhibition monitoring from the start of production. This not only provides adequate protection in case of early water breakthrough, but it also provides warning to plan and schedule routine well interventions, efficient utilization of resources (rig availability, workover crews, etc.), and better reservoir management. The addition of a phosphonate scale inhibitor into the pre-frac acid and overflush brine stages preceeding the frac operation was previously discussed in SPE 127768. As an extension of the previous work, a liquid pentaphosphonate scale inhibitor has been successfully incorporated into a seawater-based, borate-crosslinked frac fluid for fracpack operations in deepwater environments. Many challenges, including complex shear and temperature profiles, as well as potential incompatibilities arising from the interaction between the SI, crosslining agent / buffer package, and seawater were overcome by adjustments made to the crosslinking package, polymer loading, and fluid pH. The rigorous laboratory testing that led to the development of optimized fluid formulations, the assessment of scale inhibitor efficacy and formation damage potential is described herein.