Hi to all,
1. Which type of heat-exchanger will be used for cooling effluent with 25000mg/l of liquid specific gravity around 1. TSS - 100mg/l and pH 7-8.
Effluent should be cooled from 60 to 35 dec C. flow rate 133m3/hr with 2.5bar_g pressure.
2. If i use shell and tube heat exchanger (effluent in tube side due to corrosive in nature) in EDR, tube velocity is around 0.06-1.1m/s. is this velocity is enough to overcome the particle deposit/choke in the tube?