Industrial plant discharges 400 m³/day of wastewater (peak hour = 30 m³/h). TSS = 200 mg/L, particle density = 1.2 g/cm³, water at 20°C. Desired effluent TSS < 50 mg/L.
In the world of industrial wastewater treatment and potable water clarification, space is money, and efficiency is survival. Traditional sedimentation basins, while effective, consume vast footprints. Enter the (also known as an inclined plate settler or tube settler). By stacking settling surfaces at a 45- to 60-degree angle, this technology reduces the required footprint by up to 90% compared to conventional clarifiers. lamella clarifier design calculation pdf downloadl better
Using Stoke’s Law with dp = 60 µm (0.00006 m), ρp=1200 kg/m³, ρw=998, µ=0.001 Pa·s: Vs = (9.81 × (6e-5)² × (202)) / (18 × 0.001) = ~0.00396 m/s = 3.96 mm/s (or ~14.3 m/h) Industrial plant discharges 400 m³/day of wastewater (peak
[ V_s = \fracg (d_p)^2 (\rho_p - \rho_w)18 \mu ] In the world of industrial wastewater treatment and
HLR must be less than Vs · (a safety factor). A better PDF will show this comparison graphically. 2.4. Plate Spacing and Number of Plates Standard spacing: 25 to 75 mm. Closer spacing = more plates = higher efficiency but risk of bridging by solids.