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Zhan M, Zeng W, Liu H, Li J, Meng Q, Peng Y. Simultaneous nitrogen and sulfur removal through synergy of sulfammox, anammox and sulfur-driven autotrophic denitrification in a modified bioreactor enhanced by activated carbon. ENVIRONMENTAL RESEARCH 2023:116341. [PMID: 37290623 DOI: 10.1016/j.envres.2023.116341] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/26/2023] [Revised: 05/28/2023] [Accepted: 06/05/2023] [Indexed: 06/10/2023]
Abstract
Anaerobic ammonium (NH4+ - N) oxidation coupled with sulfate (SO42-) reduction (sulfammox) is a new pathway for the autotrophic removal of nitrogen and sulfur from wastewater. Sulfammox was achieved in a modified up-flow anaerobic bioreactor filled with granular activated carbon. After 70 days of operation, the NH4+ - N removal efficiency almost reached 70%, with activated carbon adsorption and biological reaction accounting for 26% and 74%, respectively. Ammonium hydrosulfide (NH4SH) was found in sulfammox by X-ray diffraction analysis for the first time, which confirmed that hydrogen sulfide (H2S) was one of the sulfammox products. Microbial results indicated that NH4+ - N oxidation and SO42- reduction in sulfammox were carried out by Crenothrix and Desulfobacterota, respectively, in which activated carbon may operate as electron shuttle. In the 15NH4+ labeled experiment, 30N2 were produced at a rate of 34.14 μmol/(g sludge·h) and no 30N2 was detected in the chemical control group, proving that sulfammox was present and could only be induced by microorganisms. The 15NO3- labeled group produced 30N2 at a rate of 88.77 μmol/(g sludge·h), demonstrating the presence of sulfur-driven autotrophic denitrification. In the adding 14NH4+ and 15NO3- group, it was confirmed that NH4+ - N was removed by the synergy of sulfammox, anammox and sulfur-driven autotrophic denitrification, where the main product of sulfammox was nitrite (NO2-) and anammox was the main cause of nitrogen loss. The findings showed that SO42- as a non-polluting species to environment may substitute NO2- to create a new "anammox" process.
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Affiliation(s)
- Mengjia Zhan
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China
| | - Wei Zeng
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China.
| | - Hong Liu
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China
| | - Jianmin Li
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China
| | - Qingan Meng
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China
| | - Yongzhen Peng
- National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing, 100124, China
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Yang N, Wang C, Han MF, Li YF, Hsi HC. Performance improvement of a biofilter by using gel-encapsulated microorganisms assembled in a 3D mesh material. CHEMOSPHERE 2020; 251:126618. [PMID: 32443246 DOI: 10.1016/j.chemosphere.2020.126618] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/21/2019] [Revised: 03/16/2020] [Accepted: 03/23/2020] [Indexed: 06/11/2023]
Affiliation(s)
- Nanyang Yang
- School of Environmental Science and Engineering, Tianjin University, Tianjin, 300072, China; Tianjin Key Lab of Indoor Air Environmental Quality Control, China
| | - Can Wang
- School of Environmental Science and Engineering, Tianjin University, Tianjin, 300072, China; Tianjin Key Lab of Indoor Air Environmental Quality Control, China.
| | - Meng-Fei Han
- School of Environmental Science and Engineering, Tianjin University, Tianjin, 300072, China; Tianjin Key Lab of Indoor Air Environmental Quality Control, China
| | - Yun-Fei Li
- School of Environmental Science and Engineering, Tianjin University, Tianjin, 300072, China; Tianjin Key Lab of Indoor Air Environmental Quality Control, China
| | - Hsing-Cheng Hsi
- Graduate Institute of Environmental Engineering, National Taiwan University, No. 71, Chou-Shan Rd., Taipei, 106, Taiwan
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Qiu X, Deshusses MA. Performance of a monolith biotrickling filter treating high concentrations of H 2S from mimic biogas and elemental sulfur plugging control using pigging. CHEMOSPHERE 2017; 186:790-797. [PMID: 28822257 DOI: 10.1016/j.chemosphere.2017.08.032] [Citation(s) in RCA: 30] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/13/2017] [Revised: 08/04/2017] [Accepted: 08/08/2017] [Indexed: 05/20/2023]
Abstract
A novel biotrickling filter using a 3D-printed honeycomb-monolith as its filter bed has been proposed and studied in this work and a solution to bed-clogging problems using pigging was demonstrated. The inlet H2S concentration in the mimic biogas was controlled around 1000 ppmv and the empty bed gas residence time (EBRT) was 41 s corresponding to a loading rate of 127 g S-H2S m-3 h-1. The influence of different H2S/O2 ratios on the removal performance and fate of sulfur end-products was investigated. The results indicated that at a H2S/O2 molar ratio of 1:2, an average removal efficiency of 95% and an elimination capacity of 122 g H2S m-3 h-1 was obtained. Under all conditions investigated, elemental sulfur (rather than sulfate) was the dominant end-product which mostly accumulated in the bed. However, the monolith bed design reduced the risk of clogging by elemental sulfur, while bed pigging was shown to be an effective means to remove excess biomass and elemental sulfur accumulated inside the bed and extend the life of the system indefinitely. Altogether, these findings could lead to significant process improvement for biological sweetening of biogas or for removing biomass in biotrickling filters at risk of plugging.
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Affiliation(s)
- Xintong Qiu
- Department of Civil and Environmental Engineering, 127C Hudson Hall, Box 90287, Duke University, Durham, NC, 27708-0287, USA
| | - Marc A Deshusses
- Department of Civil and Environmental Engineering, 127C Hudson Hall, Box 90287, Duke University, Durham, NC, 27708-0287, USA.
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Gerrity S, Kennelly C, Clifford E, Collins G. Hydrogen sulfide oxidation in novel Horizontal-Flow Biofilm Reactors dominated by an Acidithiobacillus and a Thiobacillus species. ENVIRONMENTAL TECHNOLOGY 2016; 37:2252-2264. [PMID: 26829048 DOI: 10.1080/09593330.2016.1147609] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 08/24/2015] [Accepted: 01/25/2016] [Indexed: 06/05/2023]
Abstract
Hydrogen Sulfide (H2S) is an odourous, highly toxic gas commonly encountered in various commercial and municipal sectors. Three novel, laboratory-scale, Horizontal-Flow Biofilm Reactors (HFBRs) were tested for the removal of H2S gas from air streams over a 178-day trial at 10°C. Removal rates of up to 15.1 g [H2S] m(-3) h(-1) were achieved, demonstrating the HFBRs as a feasible technology for the treatment of H2S-contaminated airstreams at low temperatures. Bio-oxidation of H2S in the reactors led to the production of H(+) and sulfate (SO(2-)4) ions, resulting in the acidification of the liquid phase. Reduced removal efficiency was observed at loading rates of 15.1 g [H2S] m(-3) h(-1). NaHCO3 addition to the liquid nutrient feed (synthetic wastewater (SWW)) resulted in improved H2S removal. Bacterial diversity, which was investigated by sequencing and fingerprinting 16S rRNA genes, was low, likely due to the harsh conditions prevailing in the systems. The HFBRs were dominated by two species from the genus Acidithiobacillus and Thiobacillus. Nonetheless, there were significant differences in microbial community structure between distinct HFBR zones due to the influence of alkalinity, pH and SO4 concentrations. Despite the low temperature, this study indicates HFBRs have an excellent potential to biologically treat H2S-contaminated airstreams.
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Affiliation(s)
- S Gerrity
- a Microbial Communities Laboratory, School of Natural Sciences , National University of Ireland Galway , Galway , Ireland
| | - C Kennelly
- b Civil Engineering, College of Engineering and Informatics , National University of Ireland Galway , Galway , Ireland
| | - E Clifford
- b Civil Engineering, College of Engineering and Informatics , National University of Ireland Galway , Galway , Ireland
- c Ryan Institute for Environmental, Marine and Energy Research , National University of Ireland Galway , Galway , Ireland
| | - G Collins
- a Microbial Communities Laboratory, School of Natural Sciences , National University of Ireland Galway , Galway , Ireland
- c Ryan Institute for Environmental, Marine and Energy Research , National University of Ireland Galway , Galway , Ireland
- d School of Engineering , University of Glasgow , Glasgow , UK
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Ramos I, Pérez R, Fdz-Polanco M. Microaerobic desulphurisation unit: a new biological system for the removal of H₂S from biogas. BIORESOURCE TECHNOLOGY 2013; 142:633-640. [PMID: 23774222 DOI: 10.1016/j.biortech.2013.05.084] [Citation(s) in RCA: 13] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/24/2013] [Revised: 05/20/2013] [Accepted: 05/21/2013] [Indexed: 06/02/2023]
Abstract
A new biotechnology for the removal of H2S from biogas was devised. The desulphurisation conditions present in microaerobic digesters were reproduced inside an external chamber called a microaerobic desulphurisation unit (MDU). A 10 L-unit was inoculated with 1L of digested sludge in order to treat the biogas produced in a pilot digester. During the 128 d of research under such conditions, the average removal efficiency was 94%. The MDU proved to be robust against fluctuations in biogas residence time (57-107 min), inlet H2S concentration (0.17-0.39% v/v), O2/H2S supplied ratio (17.3-1.4 v/v), and temperature (20-35°C). Microbiological analysis confirmed the presence of at least three genera of sulphide-oxidising bacteria. Approximately 60% of all the H2S oxidised was recovered from the bottom of the system in the form of large solid S(0) sheets with 98% w/w of purity. Therefore, this system could become a cost-effective alternative to the conventional biotechniques for biogas desulphurisation.
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Affiliation(s)
- I Ramos
- Department of Chemical Engineering and Environmental Technology, Escuela de Ingenierías Industriales, Sede Dr. Mergelina, University of Valladolid, Dr. Mergelina s/n, 47011 Valladolid, Spain
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Bacteria of the sulphur cycle: An overview of microbiology, biokinetics and their role in petroleum and mining industries. Biochem Eng J 2009. [DOI: 10.1016/j.bej.2008.12.011] [Citation(s) in RCA: 272] [Impact Index Per Article: 18.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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Rattanapan C, Boonsawang P, Kantachote D. Removal of H2S in down-flow GAC biofiltration using sulfide oxidizing bacteria from concentrated latex wastewater. BIORESOURCE TECHNOLOGY 2009; 100:125-130. [PMID: 18619836 DOI: 10.1016/j.biortech.2008.05.049] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/28/2008] [Revised: 05/21/2008] [Accepted: 05/22/2008] [Indexed: 05/26/2023]
Abstract
A biofiltration system with sulfur oxidizing bacteria immobilized on granular activated carbon (GAC) as packing materials had a good potential when used to eliminate H(2)S. The sulfur oxidizing bacteria were stimulated from concentrated latex wastewater with sulfur supplement under aerobic condition. Afterward, it was immobilized on GAC to test the performance of cell-immobilized GAC biofilter. In this study, the effect of inlet H(2)S concentration, H(2)S gas flow rate, air gas flow rate and long-term operation on the H(2)S removal efficiency was investigated. In addition, the comparative performance of sulfide oxidizing bacterium immobilized on GAC (biofilter A) and GAC without cell immobilization (biofilter B) systems was studied. It was found that the efficiency of the H(2)S removal was more than 98% even at high concentrations (200-4000 ppm) and the maximum elimination capacity was about 125 g H(2)S/m(3)of GAC/h in the biofilter A. However, the H(2)S flow rate of 15-35 l/h into both biofilters had little influence on the efficiency of H(2)S removal. Moreover, an air flow rate of 5.86 l/h gave complete removal of H(2)S (100%) in biofilter A. During the long-term operation, the complete H(2)S removal was achieved after 3-days operation in biofilter A and remained stable up to 60-days.
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Affiliation(s)
- Cheerawit Rattanapan
- Department of Industrial Biotechnology, Prince of Songkla University, Hat Yai, Songkhla, Thailand.
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Li Z, Sun T, Zhu N, Cao X, Jia J. Comparative study of using different materials as bacterial carriers to treat hydrogen sulfide. Appl Microbiol Biotechnol 2008; 81:579-88. [DOI: 10.1007/s00253-008-1745-2] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 07/02/2008] [Revised: 10/02/2008] [Accepted: 10/02/2008] [Indexed: 10/21/2022]
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Jiang X, Yan R, Jay JH. Reusing H2S-exhausted carbon as packing material for odor biofiltration. CHEMOSPHERE 2008; 73:698-704. [PMID: 18700176 DOI: 10.1016/j.chemosphere.2008.07.004] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 03/04/2008] [Revised: 07/03/2008] [Accepted: 07/03/2008] [Indexed: 05/26/2023]
Abstract
Exhausted carbon coming from the H2S adsorption process is a big environmental problem in Wastewater Treatment Plants. In this study, reusing exhausted carbon as a carrier of sulfide-oxidizing bacteria in lab-scale biofilters was evaluated. The exhausted carbons from different heights of the adsorption bed have different exhaustion extents, i.e. characteristics in terms of sulfur content, pH and porosity. Therefore, four biofilters were packed separately with exhausted carbon from top, middle, bottom of H2S adsorption bed, and a mixture of the three, to investigate the suitability for further H2S biofiltration. The results showed a quick startup in these biofilters (approximately 80 h). The numbers of sulfide-oxidizing bacteria immobilized on activated carbon were approximately 4.8, 9.2 and 14 x 108 CFU g-1 top, middle and bottom carbon after the 240-h operation, respectively. In addition, the biofilters demonstrated a rapid recovery to the original removal efficiency (RE) within 2 h after the H2S spike loadings. After a 110-h shutdown, the RE was rapidly recovered for all the biofilters within 5 h, with a shorter time (1 h) observed for the bottom carbon biofilter. The H2S removal mechanism of these biofilters was studied through a full analysis of sulfur products in both liquid (recycling medium) and activated carbon, and variable characterization of activated carbon before and after biofiltration. This study shows that the exhausted carbon-based biofilter is a feasible and economical alternative to conventional odor biofiltration.
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Affiliation(s)
- Xia Jiang
- School of Civil and Environmental Engineering, Nanyang Technological University, Blk N1, 50 Nanyang Avenue, Singapore 639798, Singapore
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Duan H, Yan R, Koe LCC, Wang X. Combined effect of adsorption and biodegradation of biological activated carbon on H2S biotrickling filtration. CHEMOSPHERE 2007; 66:1684-91. [PMID: 16930670 DOI: 10.1016/j.chemosphere.2006.07.020] [Citation(s) in RCA: 19] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/16/2005] [Revised: 07/10/2006] [Accepted: 07/10/2006] [Indexed: 05/11/2023]
Abstract
In order to evaluate the combined effect of adsorption and biodegradation of H(2)S on activated carbon surface in biotrickling filtration, four laboratory-scale biofiltration columns were operated simultaneously for 120h to investigate the mechanisms involved in treating synthetic H(2)S streams using biological activated carbon (BAC). The first three columns (A, B, C) contained a mixture of activated carbon and glass beads, with the carbons (BAC or virgin activated carbon (VAC)) and conditions (with or without liquid medium recirculation) differentiated. The last column (D) used 100% glass beads with liquid medium recirculation. Air streams containing 45ppmv H(2)S were passed through the columns at 4s of gas retention time (GRT) and liquid flow rate was set at 0.71mlmin(-1). Column D got its breakthrough in 3min of operation, indicating a negligible contribution of glass beads to the adsorption of H(2)S. The removal efficiency (RE) of Columns B and C using VAC dropped quickly to 30% within the first 8h, and afterwards continued to drop further but slowly. Column A using BAC stayed at 25% of RE throughout the operation time. A thorough investigation of the H(2)S oxidation products, i.e., various S species in both aqueous (recirculation media) and solid phases (BAC and VAC), was conducted using ICP-OES, IC, XRF, and CHNS elemental analyzer. BAC demonstrated a better performance than columns with adsorption only. Water film was found to enhance H(2)S removal. The percentage of sulphate in the total sulphur of the BAC system improved to twice of that of VAC system, indicating sulphate is the main product of H(2)S biofiltration. The observed pH drop in BAC system double confirmed that the presence of biodegradation in the biofilm over carbon surface did profound effect on the oxidation of H(2)S, compare to the systems with adsorption only.
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Affiliation(s)
- Huiqi Duan
- School of Civil and Environmental Engineering, Nanyang Technological University, Blk N1-B3b-18, 50 Nanyang Avenue, Singapore 639798, Singapore
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