Reuse of tannery wastewaters by combination of ultrafiltration and reverse osmosis after a conventional physical-chemical treatment

被引:49
作者
Fababuj-Roger, M. [1 ]
Mendoza-Roca, J. A. [1 ]
Galiana-Aleixandre, M. V. [1 ]
Bes-Pia, A. [1 ]
Cuartas-Uribe, B. [1 ]
Iborra-Clar, A. [1 ]
机构
[1] Univ Politecn Valencia, Dept Chem & Nucl Engn, E-46071 Valencia, Spain
关键词
ultrafiltration; wastewater reuse; reverse osmosis; tannery wastewater;
D O I
10.1016/j.desal.2006.02.032
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Due to the high conductivity of the global wastewater from a tannery industry, wastewater reuse is only possible if a reverse osmosis process is implemented in the wastewater treatment. The supernatant of a physical-chemical treatment is still very polluted, containing high COD values between 3000 mg/l and 4000 mg/l and conductivities of nearly 20 ms/cm. In this work, a combination of filtration, ultrafiltration and reverse osmosis is evaluated as treatment for the physical-chemically treated wastewater. Filtration was carried out using microfilters as a previous stage to ultrafiltration process. Ultrafiltration tests were performed in a laboratory plant. Organic membranes from Orelis with different cut-offs were tested to optimize the rejection and the permeate flux. Finally, the reverse osmosis step was carried out using an ESPA-1 membrane from Hydranautics. Results showed high COD values in ultrafiltration permeates (between 2000 and 3000 mg/l). A polyethersulfone membrane with cut-off of 30 kD was chosen for the pre-treatment of the reverse osmosis membrane. Permeate fluxes of the reverse osmosis membrane reached 40 1/(m(2)h) at 30 bar. Though membrane fouling was not observed during RO experiments, an industrial scale plant should pay special attention to a probable flux decrease due to the scaling if a high conversion is aimed.
引用
收藏
页码:219 / 226
页数:8
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