Lu Cai-Xia, Gu Ping
School of Environmental Science and Engineering, Tianjin University, Tianjin 300072, China.
Huan Jing Ke Xue. 2008 Mar;29(3):671-6.
Autotrophic denitrification with hydrogen as the electron donor for the removal of nitrate in drinking water was investigated by using a bench-scale sequencing batch reactor in an attached growth system. Gas permeable membrane was employed as the hydrogen diffuser to improve the hydrogen mass transfer and decrease the explosion risk. The results showed that nitrate could be removed efficiently with this technology. The removal rates of NO3(-)-N and TN could achieve 6.45 mg/(L h) and 4.89 mg/(L h) respectively, with the highest accumulation of NO2(-)-N 11.58 mg/L. pH increased to 10.56 and DOC increased 0.91 mg/L. A zero order kinetic model was proposed for NO3(-) and NO2(-) reduction, with the kinetic coefficients in the ranges of 0.33 - 0.60 g/(g d) and 0.37 - 0.45 g/(g d) respectively, The removal rates of NO3(-)-N and TN were not affected with the hydrogen pressure higher than 40 kPa, with the values (5.97 +/- 0.08) mg/(L h) and (4.25 +/- 0.04) mg/(L h) respectively, while decreased remarkably when the hydrogen pressure was 25 kPa. The denitrification reaction was inhibited at pH 6 with the removal rate of NO3(-)-N 1.83 mg/( L h); pH higher than 8 was the favorable condition for denitrification with the removal rate of NO3(-)-N 3.13 mg/(L h).
采用附着生长系统中的小型序批式反应器,研究了以氢气作为电子供体的自养反硝化作用去除饮用水中硝酸盐的效果。采用透气膜作为氢气扩散器,以改善氢气传质并降低爆炸风险。结果表明,该技术可有效去除硝酸盐。NO3(-)-N和TN的去除率分别可达6.45 mg/(L·h)和4.89 mg/(L·h),NO2(-)-N的最高积累量为11.58 mg/L。pH值升至10.56,溶解性有机碳增加0.91 mg/L。提出了用于NO3(-)和NO2(-)还原的零级动力学模型,动力学系数分别在0.33 - 0.60 g/(g·d)和0.37 - 0.45 g/(g·d)范围内。当氢气压力高于40 kPa时,NO3(-)-N和TN的去除率不受影响,其值分别为(5.97 ± 0.08) mg/(L·h)和(4.25 ± 0.04) mg/(L·h),而当氢气压力为25 kPa时,去除率显著下降。在pH值为6时反硝化反应受到抑制,NO3(-)-N的去除率为1.83 mg/(L·h);pH值高于8是反硝化的有利条件,NO3(-)-N的去除率为3.13 mg/(L·h)。