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IMPROVING THE EFFICIENCY OF WASTEWATER TREATMENT CONTAINING PETROLEUM PRODUCTS

Figure 1 - Dependence of membrane permeability on time at t=323 K, ΔР = 0.4 MPa, membrane material - fluoroplast: 

1 - ultrafiltration; 2 - ozonation with ultrafiltration

Dependence of membrane permeability on time at t=323 K, ΔР = 0.4 MPa, membrane material - fluoroplast: 1 - ultrafiltration; 2 - ozonation with ultrafiltration