Simultaneous sulfide and acetate oxidation under denitrifying conditions using an inverse fluidized bed reactor

被引:34
作者
Beristain-Cardoso, Ricardo
Texier, Anne-Claire
Sierra-Alvarez, Reyes [2 ]
Field, Jim A. [2 ]
Razo-Flores, Elias [3 ]
Gomez, Jorge [1 ]
机构
[1] Univ Autonoma Metropolitana Iztapalapa, Div CBS, Dept Biotechnol, Mexico City 09340, DF, Mexico
[2] Univ Arizona, Tucson, AZ USA
[3] Inst Potosino Invest Cient & Tecnol, San Luis Potosi, Mexico
关键词
denitrification; elemental sulfur; inverse fluidized bed reactor; sulfide oxidation;
D O I
10.1002/jctb.1921
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
BACKGROUND: Simultaneous removal of sulfur, nitrogen and carbon compounds from wastewaters is a commercially important biological process. The objective was to evaluate the influence of the CH3COO-/NO3- molar ratio on the sulfide oxidation process using an inverse fluidized bed reactor (IFBR). RESULTS: Three molar ratios of CH3COO-/NO3- (0.85, 0.72 and 0.62) with a constant S2-/NO3- molar ratio of 0.13 were evaluated. At a CH3COO-/NO3- molar ratio of 0.85, the nitrate, acetate and sulfide removal efficiencies were approximately 100%. The N-2 yield (g N-2 g(-1) NO3--N consumed) was 0.81. Acetate was mineralized, resulting in a yield of 0.65 g inorganic-C g(-1) CH3COO--C Consumed. Sulfide was partially oxidized to S-0, and 71% of the S2- consumed was recovered as elemental sulfur by a settler installed in the IFBR. At a CH3COO-/NO3- molar ratio of 0.72, the efficiencies of nitrate, acetate and sulfide consumption were of 100%, with N-2 and inorganic-C yields of 0.84 and 0.69, respectively. The sulfide was recovered as sulfate instead of S-0, with a yield of 0.92 g SO42--S g(-1) S2- consumed. CONCLUSIONS: The CH3COO-/NO3- molar ratio was shown to be an important parameter that can be used to control the fate of sulfide oxidation to either S-0 or sulfate. In this study, the potential of denitrification for the simultaneous removal of organic matter, sulfide and nitrate from wastewaters was demonstrated, obtaining CO2, S-0 and N-2 as the major end products. (C) 2008 Society of Chemical Industry.
引用
收藏
页码:1197 / 1203
页数:7
相关论文
共 18 条
[11]   TREATMENT OF H2S-CONTAINING GASES - A REVIEW OF MICROBIOLOGICAL ALTERNATIVES [J].
JENSEN, AB ;
WEBB, C .
ENZYME AND MICROBIAL TECHNOLOGY, 1995, 17 (01) :2-10
[12]   Bacterial oxidation of sulphide under denitrifying conditions [J].
Krishnakumar, B ;
Manilal, VB .
BIOTECHNOLOGY LETTERS, 1999, 21 (05) :437-440
[13]   Treatment of sulphide containing wastewater with sulphur recovery in a novel reverse fluidized loop reactor (RFLR) [J].
Krishnakumar, B ;
Majumdar, S ;
Manilal, VB ;
Haridas, A .
WATER RESEARCH, 2005, 39 (04) :639-647
[14]  
LOWRY OH, 1951, J BIOL CHEM, V193, P265
[15]   Comparison of carbon storage under aerobic and anoxic conditions [J].
Majone, M ;
Massanisso, P ;
Ramadori, R .
WATER SCIENCE AND TECHNOLOGY, 1998, 38 (8-9) :77-84
[16]   EXPERIMENTAL-STUDY OF THE INVERSE FLUIDIZED-BED BIOFILM REACTOR [J].
NIKOLOV, L ;
KARAMANEV, D .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1987, 65 (02) :214-217
[17]   Simultaneous biological removal of nitrogen, carbon and sulfur by denitrification [J].
Reyes-Avila, JS ;
Razo-Flores, E ;
Gomez, J .
WATER RESEARCH, 2004, 38 (14-15) :3313-3321
[18]   An innovative process of simultaneous desulfurization and denitrification by Thiobacillus denitrificans [J].
Wang, AJ ;
Du, DZ ;
Ren, NQ ;
van Groenestijn, JW .
JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERING, 2005, 40 (10) :1939-1949