Electrolytic cell and process for removal of bromide ions and disinfection of source waters using silver cathode and/or dimensionally stable anode (DSA): a process for the reduction of disinfectant/disinfection byproducts in drinking water

• US 7,384,564 B2
• Filed: 08/18/2006
• Issued: 06/10/2008
• Est. Priority Date: 02/16/2006
• Status: Expired due to Fees

• Current Assignee: Labisi Bo
• Original Assignee: Labisi Bo
• Inventors: Bo, Labisi
• Primary Examiner(s): Griffin; Walter D.
• Assistant Examiner(s): Allen; Cameron J
• Application Number:
  US11/465,542
• Publication Number:
  US 20070187337A1
• Time in Patent Office: 662 Days
• Field of Search: 210/748, 210/754, 210/764
• US Class Current: 210/748.2
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 1/461 by electrolysis
• CPC Class Codes: C02F 1/467 by electrochemical disinfection; by electrooxydation or by electroreduction
• CPC Class Codes: C02F 2001/46133 characterised by the material

Abstract

Electrolytic process combines disinfection with removal of bromide from raw water. Current is applied to the electrodes in an electrolytic cell with raw water that has some salinity as the electrolyte. The electrodes consist of silver or dimensionally stable anodes (DSA) as cathodes and dimensionally stable anodes (DSA) arranged in parallel baffling fashion. During electrolysis chloride is converted to chlorine. The chlorine immediately effects disinfection of the water and reduction of bromide ions to bromine gas which is liberated from the cell. Aqueous bromine will remain in solution as hypobromous acid. The extent of chlorine generation and bromide loss depend upon the chloride:bromide ratio, electrical energy supplied for electrolysis, ionic strength of the water, electrode distance, cell residence time and electrode material.

Claims

1. A process of water treatment in which bromide removal is accomplished in an electrolytic cell with silver cathode and DSA anode or DSA cathode and DSA anode powered with controlled and variable amount of current further comprising conventional water treatment and GAC filtration or other means of TOC removal so that the bromide and TOC concentrations are reduced to less than or equal to 100 ppb and less than or equal to 1.5 mg/L respectively before addition of chlorine thereby reducing TTHM, haloacetic acids and specifically other brominated disinfection byproducts in finished water.

2. The process of claim 1 in which the extent of bromide removal based on the chloride:

bromide ratio and the ionic strength of the solution can be adjusted by controlling the electrical energy supplied for the electrolysis, electrode distance or effective electrode area/cell volume, cell residence time and the choice of silver or DSA as cathode while using DSA as anode.

3. The process of claim 1 in which there is self generation of chlorine and bromine from chloride and bromide present in the source water so that disinfection of the water starts within the electrolytic cell without adding any disinfectant at that stage of the water treatment train resulting in a substantial reduction of the total coliform bacteria density in the cell effluent compared to the influent.