Anawat Pinisakul

Application of electro-chemical process for treatment of arsenic-contaminated water - Bangkok : Asian Institute of Technology, 2002 - 134 p. - Dissertation ; no. EV-02-03 . - Asian Institute of Technology. Dissertation ; no. EV-02-3 .

A dissertation submitted in partial fulfil~ment of the reqqirements for the degree of Doctor of Technical Science, Inter-University Program on Environmental Toxicology, Technology and Management, Asian Institute of Technology; Chulabhorn Research Institute and Mahidol University

Thesis (Ph.D.) - Asian Institute of Technology, 2002

This research was conducted to investigate the efficiency, chemical reactions and mechanisms of arsenic (As) removal from a contaminated water by using the electrochemical treatment (ECT) process. For a synthetic As-contaminated water, within the following operating conditions : initial As-concentration of 0.5-5 mg/L, area of electrode plate/volume ofECT reactor of 0.02 cm2/cm3, 0.1 M KCl, electrical gradient of200 volt/m and initial pH higher than 3, the laboratory-scale ECT reactors operating in batch mode were able to reduce As to be within 0.01 mg/L in 15-20 min, making the treated water suitable for use in shrimp culture. For a contaminated groundwater containing As about 0.135-1.072 mg/L, the batch ECT reactors were effective in reducing the As to be within 0.01 mg/Lin 5 min. The Cr salt was found to yield better As removal efficiencies than the N03- salt because, chemically, N03- ions interfere with the production of OH- and Fe(OH)3, the compound mainly responsible for As removal. A first-order reaction model for As removal, incorporating parameters such as area of electrode plate/volume of ECT reactor, conductivity and electrical gradient, was developed which was found feasible in predicting As removal efficiency by the ECT process. The continuous ECT reactor was found to be equally effective in treating the Ascontaminated water, but due to the continuous As input, it required longer operation time than that of the batch operation. However; because of the continuous mixing condition, it required less power and electi'ode consumptions than those of the batch reactors in achieving the same As removal efficiency. The ECT sludge characteristics were analyzed by X-ray fluorescence (XRF) and X-ray diffractometric (XRD) methods. The results revealed maghemite (Fe203) and angellelite (Fe

Water--Pollution
Water--Purification