The agitator in the source tank entrains gas in the bulk liquid so this gas has to be separated. The priming pot seems small - the suction line to the pumps should be continuously sloping down to the pumps, so that residual gas in the exit from the priming pot gets to escape back into the priming pot. Else you will still lose prime at pump suction. Agreed, a free venting arrangement of the inlet and exit nozzles on the pumps will also be necessary to keep the pump casing primed. Presume the vent line on the priming pot returns somewhere where the pressure is lower than that in the priming pot?
Submerged pump alternate may have been rejected on the grounds that solid salt granules could get into pump suction, eroding the impellers ?