Source Jouranl of CSCD
Source Journal of Chinese Scientific and Technical Papers
Included as T2 Level in the High-Quality Science and Technology Journals in the Field of Environmental Science
Core Journal of RCCSE
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Indexed in World Journal Clout Index (WJCI) Report
Volume 38 Issue 5
Aug.  2020
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Article Contents
SU Chang, LI Ying-fen, YAN Xing, CHONG Yun-xiao. DIVERSITY OF IRON MINERALS AND THEIR ADSORPTION TO Cd IN FERROUS OXIDATION AND DENITRIFICATION BIOFILM REACTOR[J]. ENVIRONMENTAL ENGINEERING , 2020, 38(5): 76-83. doi: 10.13205/j.hjgc.202005014
Citation: SU Chang, LI Ying-fen, YAN Xing, CHONG Yun-xiao. DIVERSITY OF IRON MINERALS AND THEIR ADSORPTION TO Cd IN FERROUS OXIDATION AND DENITRIFICATION BIOFILM REACTOR[J]. ENVIRONMENTAL ENGINEERING , 2020, 38(5): 76-83. doi: 10.13205/j.hjgc.202005014

DIVERSITY OF IRON MINERALS AND THEIR ADSORPTION TO Cd IN FERROUS OXIDATION AND DENITRIFICATION BIOFILM REACTOR

doi: 10.13205/j.hjgc.202005014
  • Received Date: 2019-06-03
  • Nitrate-dependent anaerobic ferrous iron oxidation refers to the biomineralization process coupled with ferrous oxidation and nitrate nitrogen reduction, which not only has the effect of denitrification on sewage, but also can obtain a series of iron minerals with strong adsorption and removal ability for multi pollutants. In this study, we constructed a continuous flow biofilm reactor based on this process for wastewater denitrification treatment, and analyzed the characteristics of particulate matters generated internally after three months of operation and their adsorption effect on cadmium (Cd). The results showed that the granules in different positions of the reactor contain different iron minerals, the bottom and middle particles were dominated by siderite, and the top particles were dominated by goethite. These particles had a large specific surface area and a variety of organic functional groups for adsorption, and strong adsorption capacity for Cd2+ in water. The adsorption removal rate of different positions of the reactor was in sequence of effluent>top>middle>bottom, all above 84%. The kinetic and thermodynamic equations complied well with the pseudo second-order model and Freundlich isotherms model, respectively.
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