Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6465208 | Chemical Engineering Journal | 2017 | 8 Pages |
â¢A two-stage hydrogenotrophic process to remove NO3â and ClO4â is presented.â¢NO3â is removed in a first unsaturated-flow pressurized reactor stage.â¢The residual H2 is coupled to ClO4â reduction in a second polishing stage.â¢Large presence of Dechloromonas was detected before and after ClO4â addition.â¢Effluent ClO4â concentration of 2 μg/L and â¼100% H2 utilization were achieved.
A novel pressurized hydrogenotrophic reactor operating at high rates was recently developed specifically for the removal of nitrate (NO3â) from drinking water. The reactor is characterized by safe and economical operation since hydrogen (H2) purging intrinsic to conventional H2-based denitrifying systems is not required and H2 loss occurs only through the effluent, resulting in H2 utilization efficiency above 90%. In this research, a new treatment scheme to remove NO3â and perchlorate (ClO4â) combining the pressurized reactor with a following open-to-atmosphere polishing unit is presented. In the pressurized reactor, NO3â and ClO4â are simultaneously removed. In the polishing unit, the residual dissolved H2 from the pressurized reactor serves to further reduce ClO4â to trace concentrations below recommended levels.First, ClO4â reduction together with denitrification was demonstrated in the pressurized reactor without special inoculation and a maximal ClO4â volumetric removal rate of 1.83 g/(Lreactor·d) was achieved. Microbial population analyses before and after the addition of ClO4â were similar with a large fraction of the genus Dechloromonas. Results show that the combined treatment scheme consisting of the pressurized reactor and the polishing unit allowed for the reduction of ClO4â concentration down to a minimal value of 2 µg/L with a simultaneous increase of the H2 utilization efficiency from 95% up to almost 100%.