340°F is the boiling point at 103 psig. What is the purpose here? To evaporate water and concentrate the slurry? Or to soak the solids at 340°F with little evaporation of the water?
For pumping at the boiling point, you have to ensure that you have sufficient NPSHA. I.e. the level control in the tank must be good or the tank must be high enough. It appears that at the inlet to the tank, you will have a three phase mixture (solids, liquid water and steam). That is an environment which favours erosion/corrosion. So, the heat exchanger, outlet piping, valves, tank inlet nozzle and impact areas on the tank walls should be designed for this. The heat exchanger will probably be designed for non-boiling operation. I.e. it will operate at a pressure above 103 psig. That means you would need a valve between it and the tank across which the mixture would flash.
In other words, it appears as if you have an interesting design problem on your hands. You have given us very little information to start off from. It is also not clear whether you are asking about the pump or also about the whole system including the pump.