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Wastewaters ozonization decolorization

The main estimation results are values of ratio mineralization extent/process operating costs (ME/POC). Besides costs estimation on the basis of mineralized organic content, the cost for decolorization below visibility limit, <1 mgL that corresponds to decolorization below 1.25 % in our case, are also showed. From the point of view of the most suitable processes for decolorization of RB137 model wastewater below visibility limit, it can be seen that processes combining ozone and UV irradiation, UV/O3 and UV/O3/H2O2, are double cheaper than... [Pg.62]

Carriere J., Jones J. P. and Broadbent A.D., Decolorization of textile wastewaters by ozonation . AATCC Book of paper, 232 (1991). [Pg.171]

Hydrophobic nature, especially suitable to bind nonpolar substances, flue gas cleaning, gas cleaning, solvent recovery, deodorization, respiration filter, catalyst carrier, separation of gas mixtures, deoiling, degreasing, liquid decoloration organic substance removal from drinking water, feed water, and wastewater chlorine and ozone removal from water. [Pg.294]

Shu, H. and Chang, M. (2005). Pre-ozonation Coupled with UV/H2O2 Process for the Decoloration and Mineralization of Cotton Dyeing Effluent and Synthesized C. I. Direct Black 22 Wastewater, J. Hazardous Materials, 121, pp. 127-133. [Pg.285]


See other pages where Wastewaters ozonization decolorization is mentioned: [Pg.30]    [Pg.666]    [Pg.13]    [Pg.32]    [Pg.54]    [Pg.55]    [Pg.608]    [Pg.608]    [Pg.241]    [Pg.565]    [Pg.1997]    [Pg.454]    [Pg.516]    [Pg.587]   
See also in sourсe #XX -- [ Pg.608 ]




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