As a Process Engineer one can tackle pump cavitation problem by following methods:
1. Increasing the static height of the suction vessel
2. Increasing the LLLL in the suction vessel (LLLL is considered for calculating conservative value of NPSHa)
3. Increasing the system pressure
4. Decreasing the fluid temperature (i.e. decreasing the vapour pressure)
5. Increasing the suction piping diameter
6. Decreasing the suction piping length
Generally point 3 and 4 are difficult as those are generally fixed as per process requirement.
Cavitation can also be avoided by the following methods
A. Providing inducers (An Inducer is an axial flow impeller with blades that wrap in a helix around a central hub. An Inducer serves as a small booster pump for the main impeller. Usually inducers have between 2 and 4 vanes, although there may be more. The inducer imparts sufficient head to the liquid so that the NPSH requirement of the adjacent main impeller is satisfied)
B. Increasing the eye of the impeller
There can be more alternatives than A and B, but for that you need to contact the pump vendor, he is the right person to solve the issue