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Investigating role of abiotic side and finding optimum abiotic condition for improving gas biodesulfurization using Thioalkalivibrio versutus. Sci Rep 2022; 12:6260. [PMID: 35428823 PMCID: PMC9012822 DOI: 10.1038/s41598-022-10430-6] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 01/04/2022] [Accepted: 03/29/2022] [Indexed: 11/24/2022] Open
Abstract
Hydrogen sulfide (H2S) is a super toxic substance that produces SOx gases when combusted. Therefore, it should be removed from gas streams. Biodesulfurization is one of the developing methods for removing sulfide. Gas biodesulfurization must be accelerated to be competitive with chemical processes. This process has two sides: biotic and abiotic sides. To increase the rate of sulfide removal, this substance should be given to the bacteria in the maximum amount (Max. − RHS B). Therefore, it is necessary to minimize the rate of adverse abiotic reactions of sulfide (Min. − RHS A). Minimizing the sulfide reaction with biosulfur and oxygen and thiosulfate generation (Min. − RHS thio2) was assessed in de-microbized medium. It was concluded that the pH should be kept as low as possible. The kinetics of thiosulfate formation from sulfide oxidation (− RHS thio1) are strongly dependent on the sulfide concentration, and to minimize this reaction rate, sulfide should be gently injected into the culture. To minimize sulfide reduction to hydrogen sulfide (Min. − RHS rev), the pH should be kept as high as possible. Using the Design Expert v.13, a model was driven for the abiotic side to obtain optimum condition. The pH value was found to be 8.2 and the sulfide concentration to 2.5E−05 M. Thioalkalivibrio versutus cultivation under identified abiotic conditions resulted in biological removal of sulfide up to 1.5 g/h. The culture was not able to remove 2 g/h input sulfide, and to increase this, the biotic side should be studied.
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de Rink R, B Lavender M, Liu D, Klok JBM, Sorokin DY, Ter Heijne A, Buisman CJN. Continuous electron shuttling by sulfide oxidizing bacteria as a novel strategy to produce electric current. JOURNAL OF HAZARDOUS MATERIALS 2022; 424:127358. [PMID: 34879559 DOI: 10.1016/j.jhazmat.2021.127358] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/20/2021] [Revised: 08/30/2021] [Accepted: 09/24/2021] [Indexed: 06/13/2023]
Abstract
Sulfide oxidizing bacteria (SOB) are widely applied in industry to convert toxic H2S into elemental sulfur. Haloalkaliphilic planktonic SOB can remove sulfide from solution under anaerobic conditions (SOB are 'charged'), and release electrons at an electrode (discharge of SOB). The effect of this electron shuttling on product formation and biomass growth is not known. Here, we study and demonstrate a continuous process in which SOB remove sulfide from solution in an anaerobic 'uptake chamber', and shuttle these electrons to the anode of an electrochemical cell, in the absence of dissolved sulfide. Two experiments over 31 and 41 days were performed. At a sulfide loading rate of 1.1 mmolS/day, electricity was produced continuously (3 A/m2) without dissolved sulfide in the anolyte. The main end product was sulfate (56% in experiment 1% and 78% in experiment 2), and 87% and 77% of the electrons in sulfide were recovered as electricity. It was found that the current density was dependent on the sulfide loading rate and not on the anode potential. Biological growth occurred, mainly at the anode as biofilm, in which the deltaproteobacterial genus Desulfurivibrio was dominating. Our results demonstrate a novel strategy to produce electricity from sulfide in an electrochemical system.
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Affiliation(s)
- Rieks de Rink
- Environmental Technology, Wageningen University, P.O. Box 17, Wageningen, The Netherlands; Paqell B.V., Reactorweg 301, 3542 AD Utrecht, The Netherlands
| | - Micaela B Lavender
- Environmental Technology, Wageningen University, P.O. Box 17, Wageningen, The Netherlands
| | - Dandan Liu
- Paqell B.V., Reactorweg 301, 3542 AD Utrecht, The Netherlands
| | - Johannes B M Klok
- Environmental Technology, Wageningen University, P.O. Box 17, Wageningen, The Netherlands; Paqell B.V., Reactorweg 301, 3542 AD Utrecht, The Netherlands; Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, Leeuwarden, The Netherlands
| | - Dimitry Y Sorokin
- Winogradsky Institute of Microbiology, Research Centre of Biotechnology RAS, Leninskii Prospect, 33/2, 119071 Moscow, Russia; Department of Biotechnology, Delft University of Technology, Van der Maasweg 9, 2629HZ Delft, The Netherlands
| | - Annemiek Ter Heijne
- Environmental Technology, Wageningen University, P.O. Box 17, Wageningen, The Netherlands.
| | - Cees J N Buisman
- Environmental Technology, Wageningen University, P.O. Box 17, Wageningen, The Netherlands; Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, Leeuwarden, The Netherlands
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Li W, Zhang M, Kang D, Chen W, Yu T, Xu D, Zeng Z, Li Y, Zheng P. Mechanisms of sulfur selection and sulfur secretion in a biological sulfide removal (BISURE) system. ENVIRONMENT INTERNATIONAL 2020; 137:105549. [PMID: 32086075 DOI: 10.1016/j.envint.2020.105549] [Citation(s) in RCA: 20] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/20/2019] [Revised: 01/06/2020] [Accepted: 02/03/2020] [Indexed: 06/10/2023]
Abstract
Biological desulfurization technology is a sustainable process for the sulfide removal from biogas, which has multiple advantages. In this study, a biological sulfide removal (BISURE) system was established to investigate the working performances and process mechanisms. The results showed that the sulfide removal rate was 2.30 kg-S/(m3 d), the sulfide removal efficiency was higher than 98%, the sulfur production rate was 1.76 kg-S/(m3 d), the sulfur selectivity was 75.02 ± 3.63% and the main form of products (sulfur compounds) was Rosickyite-S and S8. The performance of BISURE system was supported by the dominant genus (abundance more than 60%) of sulfur-oxidizing bacteria (SOB) which shifted to Thiovirga at the high SLR. The sqr and dsrA genes could serve as the indicators for the pathway of two-step sulfide oxidation, i.e. "partial sulfide oxidation (PSO, sulfide → sulfur)" and "complete sulfide oxidation (CSO, sulfur → sulfate)". The sulfur selectivity was improved by enhancing PSO and inhibiting CSO with the indication of two genes. The cellular sulfur secretion was revealed, and the "outer-membrane vesicles (OMVs)-dependent" sulfur-secreting hypothesis was proposed to explain the transportation of elemental sulfur from inside to outside of SOB cells. The findings of this work provide a new perspective to understand the sulfur selection of sulfide bio-oxidation and the sulfur secretion of SOB cells so as to promote the development of biological desulfurization technology.
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Affiliation(s)
- Wenji Li
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Meng Zhang
- Advanced Environmental Biotechnology Centre, Nanyang Environment & Water Research Institute, Nanyang Technological University, Singapore
| | - Da Kang
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Wenda Chen
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Tao Yu
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Dongdong Xu
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Zhuo Zeng
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Yiyu Li
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China
| | - Ping Zheng
- Department of Environmental Engineering, College of Environmental & Resource Sciences, Zhejiang University, Hangzhou, Zhejiang 310058, China.
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Kiragosyan K, Klok JB, Keesman KJ, Roman P, Janssen AJ. Development and validation of a physiologically based kinetic model for starting up and operation of the biological gas desulfurization process under haloalkaline conditions. WATER RESEARCH X 2019; 4:100035. [PMID: 31334497 PMCID: PMC6614595 DOI: 10.1016/j.wroa.2019.100035] [Citation(s) in RCA: 15] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/04/2019] [Revised: 06/28/2019] [Accepted: 07/01/2019] [Indexed: 05/14/2023]
Abstract
Hydrogen sulfide is a toxic and corrosive gas that must be removed from gaseous hydrocarbon streams prior to combustion. This paper describes a gas biodesulfurization process where sulfur-oxidizing bacteria (SOB) facilitate sulfide conversion to both sulfur and sulfate. In order to optimize the formation of sulfur, it is crucial to understand the relations between the SOB microbial composition, kinetics of biological and abiotic sulfide oxidation and the effects on the biodesulfurization process efficiency. Hence, a physiologically based kinetic model was developed for four different inocula. The resulting model can be used as a tool to evaluate biodesulfurization process performance. The model relies on a ratio of two key enzymes involved in the sulfide oxidation process, i.e., flavocytochrome c and sulfide-quinone oxidoreductase (FCC and SQR). The model was calibrated by measuring biological sulfide oxidation rates for different inocula obtained from four full-scale biodesulfurization installations fed with gases from various industries. Experimentally obtained biological sulfide oxidation rates showed dissimilarities between the tested biomasses which could be explained by assuming distinctions in the key-enzyme ratios. Hence, we introduce a new model parameter α to whereby α describes the ratio between the relative expression levels of FCC and SQR enzymes. Our experiments show that sulfur production is the highest at low α values.
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Affiliation(s)
- Karine Kiragosyan
- Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911, MA, Leeuwarden, the Netherlands
- Environmental Technology, Wageningen University, P.O. Box 17, 6700, AA, Wageningen, the Netherlands
- Corresponding author. Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911, MA, Leeuwarden, the Netherlands.
| | - Johannes B.M. Klok
- Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911, MA, Leeuwarden, the Netherlands
- Environmental Technology, Wageningen University, P.O. Box 17, 6700, AA, Wageningen, the Netherlands
- Paqell B.V., Reactorweg 301, 3542, AD, Utrecht, the Netherlands
| | - Karel J. Keesman
- Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911, MA, Leeuwarden, the Netherlands
- Biobased Chemistry & Technology, Wageningen University, P.O. Box 17, 6700, AA, Wageningen, the Netherlands
| | - Pawel Roman
- Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911, MA, Leeuwarden, the Netherlands
| | - Albert J.H. Janssen
- Environmental Technology, Wageningen University, P.O. Box 17, 6700, AA, Wageningen, the Netherlands
- Shell, Oostduinlaan 2, 2596, M the Hague, the Netherlands
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Kalantari H, Nosrati M, Shojaosadati SA, Shavandi M. Investigation of transient forms of sulfur during biological treatment of spent caustic. ENVIRONMENTAL TECHNOLOGY 2018; 39:1597-1606. [PMID: 28554258 DOI: 10.1080/09593330.2017.1334707] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/11/2016] [Accepted: 05/20/2017] [Indexed: 06/07/2023]
Abstract
In the present study, the production of various transient forms of sulfur during biological oxidation of sulfidic spent caustics under haloalkaline conditions in a stirred tank bioreactor is investigated. Also, the effects of abiotic aeration (chemical oxidation), dissolved oxygen (DO) concentration and sodium concentration on forms of sulfur during biological treatment are demonstrated. Thioalkalivibrio versutus strain was used for sulfide oxidation in spent caustic (SC). The aeration had an important effect on sulfide oxidation and its final products. At DO concentrations above 2 mg l-1, majority of sulfide was oxidized to sulfate. Maximum sulfide removal efficiency (%R) and yield of sulfate production [Formula: see text] was obtained in Na+ concentration ranging from 0.6 to 2 M. Abiotic aeration, which is the most important factor of production of thiosulfate, resulted in the formation of an undesired product-polysulfide. However, abiotic aeration can be used as a pretreatment to biological treatment. In the bioreactor the removal efficiency was obtained as 82.7% and various forms of sulfur such as polysulfide, biosulfur, thiosulfate and sulfate was observed during biological treatment of SC.
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Affiliation(s)
- Hamed Kalantari
- a Biotechnology Group, Faculty of Chemical Engineering , Tarbiat Modares University , Tehran , Iran
| | - Mohsen Nosrati
- a Biotechnology Group, Faculty of Chemical Engineering , Tarbiat Modares University , Tehran , Iran
| | - Seyed Abbas Shojaosadati
- a Biotechnology Group, Faculty of Chemical Engineering , Tarbiat Modares University , Tehran , Iran
| | - Mahmoud Shavandi
- b Environment and Biotechnology Group , Research Institute of Petroleum Industry , Tehran , Iran
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Pokorna-Krayzelova L, Bartacek J, Vejmelkova D, Alvarez AA, Slukova P, Prochazka J, Volcke EI, Jenicek P. The use of a silicone-based biomembrane for microaerobic H2S removal from biogas. Sep Purif Technol 2017. [DOI: 10.1016/j.seppur.2017.07.077] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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Simple biogas desulfurization by microaeration – Full scale experience. Anaerobe 2017; 46:41-45. [DOI: 10.1016/j.anaerobe.2017.01.002] [Citation(s) in RCA: 35] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/23/2016] [Revised: 12/25/2016] [Accepted: 01/04/2017] [Indexed: 11/22/2022]
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de Sousa JT, Lima JDF, da Silva VC, Leite VD, Lopes WS. Recovery of elemental sulphur from anaerobic effluents through the biological oxidation of sulphides. ENVIRONMENTAL TECHNOLOGY 2017; 38:529-537. [PMID: 27350297 DOI: 10.1080/09593330.2016.1201148] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/08/2016] [Accepted: 06/05/2016] [Indexed: 06/06/2023]
Abstract
The aim of the present study was to evaluate the biological oxidation of sulphide in two different UASB reactors by assessing the occurrence of oxidized forms of sulphur in the effluents and the amount of S0 that could be recovered in the process. The bioreactors employed were an anaerobic hybrid (AH) reactor employing porous polyurethane foam as support media and a micro-aerated UASB reactor equipped with an aeration device above the digestion zone. The AH reactor produced a final effluent containing low concentrations of S2- (3.87% of total sulphur load). It was achieved due to a complete oxidation of 56.1% of total sulphur. The partial biological oxidation that occurred in the AH reactor allowed the recovery of 30% of the sulphur load as S0. The effluent from the micro-aerated UASB reactor contained 5% of the sulphur load in the form of S2-, while 20.9% was present as dissolved SO42- and 46% was precipitated as S0. It is concluded that the AH reactor or micro-aeration carried out above the digestion zone of the UASB reactor favoured the biological oxidation of S2- and the release of odourless effluents. Both technologies represent feasible and low-cost alternatives for the anaerobic treatment of domestic sewage.
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Affiliation(s)
- José Tavares de Sousa
- a Departamento de Engenharia Sanitária e Ambiental, Programa de Pós-Graduação em Ciência e Tecnologia Ambiental , Universidade Estadual da Paraiba , Campina Grande , Brazil
| | - Jéssyca de Freitas Lima
- a Departamento de Engenharia Sanitária e Ambiental, Programa de Pós-Graduação em Ciência e Tecnologia Ambiental , Universidade Estadual da Paraiba , Campina Grande , Brazil
| | - Valquíria Cordeiro da Silva
- a Departamento de Engenharia Sanitária e Ambiental, Programa de Pós-Graduação em Ciência e Tecnologia Ambiental , Universidade Estadual da Paraiba , Campina Grande , Brazil
| | - Valderi Duarte Leite
- a Departamento de Engenharia Sanitária e Ambiental, Programa de Pós-Graduação em Ciência e Tecnologia Ambiental , Universidade Estadual da Paraiba , Campina Grande , Brazil
| | - Wilton Silva Lopes
- a Departamento de Engenharia Sanitária e Ambiental, Programa de Pós-Graduação em Ciência e Tecnologia Ambiental , Universidade Estadual da Paraiba , Campina Grande , Brazil
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Sousa JAB, Bijmans MFM, Stams AJM, Plugge CM. Thiosulfate Conversion to Sulfide by a Haloalkaliphilic Microbial Community in a Bioreactor Fed with H 2 Gas. ENVIRONMENTAL SCIENCE & TECHNOLOGY 2017; 51:914-923. [PMID: 27997142 DOI: 10.1021/acs.est.6b04497] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 06/06/2023]
Abstract
In industrial gas biodesulfurization systems, where haloalkaline conditions prevail, a thiosulfate containing bleed stream is produced. This bleed stream can be treated in a separate bioreactor by reducing thiosulfate to sulfide and recycling it. By performing treatment and recycling of the bleed stream, its disposal decreases and less caustics are required to maintain the high pH. In this study, anaerobic microbial thiosulfate conversion to sulfide in a H2/CO2 fed bioreactor operated at haloalkaline conditions was investigated. Thiosulfate was converted by reduction to sulfide as well as disproportionation to sulfide and sulfate. Formate production from H2/CO2 was observed as an important reaction in the bioreactor. Formate, rather than H2, might have been used as the main electron donor by thiosulfate/sulfate-reducing bacteria. The microbial community was dominated by bacteria belonging to the family Clostridiaceae most closely related to Tindallia texcoconensis. Bacteria phylogenetically related to known haloalkaline sulfate and thiosulfate reducers, thiosulfate-disproportionating bacteria, and remarkably sulfur-oxidizing bacteria were also detected. On the basis of the results, two approaches to treat the biodesulfurization waste stream are proposed: (i) addition of electron donor to reduce thiosulfate to sulfide and (ii) thiosulfate disproportionation without the need for an electron donor. The concept of application of solely thiosulfate disproportionation is discussed.
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Affiliation(s)
- João A B Sousa
- Laboratory of Microbiology, Wageningen University , Stippeneng 4, 6708 WE Wageningen, The Netherlands
- Wetsus , European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands
| | - Martijn F M Bijmans
- Wetsus , European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands
| | - Alfons J M Stams
- Laboratory of Microbiology, Wageningen University , Stippeneng 4, 6708 WE Wageningen, The Netherlands
- CEB-Centre of Biological Engineering, University of Minho , Campus de Gualtar, 4710-057, Braga, Portugal
| | - Caroline M Plugge
- Laboratory of Microbiology, Wageningen University , Stippeneng 4, 6708 WE Wageningen, The Netherlands
- Wetsus , European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands
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Liu W, Liang C, Chen J, Zhu L. Effect of operating parameters on sulfide biotransformation to sulfur. J Environ Sci (China) 2013; 25:2417-2421. [PMID: 24649672 DOI: 10.1016/s1001-0742(12)60327-1] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 06/03/2023]
Abstract
A laboratory-scale bioreactor with polyethylene semi-soft packing was constructed and utilized to determine the efficiency of sulfide biotransformation to sulfur under various operating parameters. Sodium sulfide dissolved in tap water was pumped into the bioreactor as sulfide for biological desulfurization. The sulfide, sulfur and sulfate-S in the effluent and the sulfide purged as gas-phase H2S were determined to investigate the effects of operating parameters, such as pH, DO, hydraulic retention time (HRT), temperature and salinity, on the sulfide oxidation products. The activity of bacteria was highest at pH 7.8-8.2. The maximal sulfide removal load was 7.25 kg/(m3 x day), with a 322.07 mg/L influent sulfide concentration and 4.80 mg/L DO. The increase of DO value corresponds to a decrease in the sulfur yield. The reactor had the highest sulfide removal load and sulfur yield at 2.55 mg/L DO. HRT had little effect on desulfurization efficiency when the sulfide removal load was kept constant. The most effective desulfurization temperature was 33 degrees C. The sulfide removal load decreased from 2.85 to 0.51 kg/(m3 x day) with increasing salinity from 0.5% to 2.5% (m/m).
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Fortuny M, Gamisans X, Deshusses MA, Lafuente J, Casas C, Gabriel D. Operational aspects of the desulfurization process of energy gases mimics in biotrickling filters. WATER RESEARCH 2011; 45:5665-5674. [PMID: 21890165 DOI: 10.1016/j.watres.2011.08.029] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/29/2011] [Revised: 08/13/2011] [Accepted: 08/16/2011] [Indexed: 05/31/2023]
Abstract
Biological removal of reduced sulfur compounds in energy-rich gases is an increasingly adopted alternative to conventional physicochemical processes, because of economical and environmental benefits. A lab-scale biotrickling filter reactor for the treatment of high-H(2)S-loaded gases was developed and previously proven to effectively treat H(2)S concentrations up to 12,000 ppm(v) at gas contact times between 167 and 180 s. In the present work, a detailed study on selected operational aspects affecting this system was carried out with the objective to optimize performance. The start-up phase was studied at an inlet H(2)S concentration of 1000 ppm(v) (loading of 28 g H(2)S m(-3) h(-1)) and inoculation with sludge from a municipal wastewater treatment plant. After reactor startup, the inlet H(2)S concentration was doubled and the influence of different key process parameters was tested. Results showed that there was a significant reduction of the removal efficiency at gas contact times below 120 s. Also, mass transfer was found to be the main factor limiting H(2)S elimination, whereas performance was not influenced by the bacterial colonization of the packed column after the initial startup. The effect of gas supply shutdowns for up to 5 days was shown to be irrelevant on process performance if the trickling liquid recirculation was kept on. Also, the trickling liquid velocity was investigated and found to influence sulfate production through a better use of the supplied dissolved oxygen. Finally, short-term pH changes revealed that the system was quite insensitive to a pH drop, but was markedly affected by a pH increase, affecting both the biological activity and the removal of H(2)S. Altogether, the results presented and discussed herein provide new insight and operational data on H(2)S removal from energy gases in biotrickling filters.
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Affiliation(s)
- Marc Fortuny
- Department of Chemical Engineering, Universitat Autònoma de Barcelona, Bellaterra, Spain
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Sahinkaya E, Hasar H, Kaksonen AH, Rittmann BE. Performance of a sulfide-oxidizing, sulfur-producing membrane biofilm reactor treating sulfide-containing bioreactor effluent. ENVIRONMENTAL SCIENCE & TECHNOLOGY 2011; 45:4080-4087. [PMID: 21452867 DOI: 10.1021/es200140c] [Citation(s) in RCA: 51] [Impact Index Per Article: 3.9] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/30/2023]
Abstract
Sulfide-containing waste streams are generated in mining, petrochemical plants, tanneries, viscose rayon manufacture, and the gasification of coal. Colorless sulfur bacteria can oxidize sulfide to elemental sulfur (S°), which can be recovered, when oxygen is their electron acceptor. This study evaluated sulfide oxidation and S° recovery in an oxygen-based membrane biofilm reactor (MBfR) treating the effluent from a sulfidogenic anaerobic baffled reactor. Sulfide oxidation efficiency (37-99%) and S° recovery (64-89% of oxidized sulfide) could be controlled by manipulating the sulfide loading, oxygen pressure to the fibers, and hydraulic retention time (HRT). For example, too-low oxygen pressure decreased S° recovery due to decreased sulfide oxidation, but too-high oxygen pressure lowered S° recovery due to its oxidation to sulfate. Most importantly, high sulfide oxidation (>98%) and conversion to S° (>75%) could be achieved together when the sulfide loading was less than 1.7 mol/m²·d and the O₂ pressure was sufficient to give an O₂ flux of at least 1.5 mol/m²·d. However, higher sulfide loading could be compensated by a higher O₂ pressure, and the best performance occurred when the sulfide loading was high (2 molS/m²·d), the O₂ pressure was high (∼1 atm), and the HRT was short (1.9 h). Membrane fouling caused a low O₂ flux, which led to low sulfide-oxidation efficiency, but fouling could be reversed by mild acid washing.
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Affiliation(s)
- Erkan Sahinkaya
- Department of Environmental Engineering, Harran University , Osmanbey Campus, 63000 Sanliurfa, Turkey.
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Evaluation of haloalkaliphilic sulfur-oxidizing microorganisms with potential application in the effluent treatment of the petroleum industry. Biodegradation 2010; 22:83-93. [DOI: 10.1007/s10532-010-9378-4] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 12/18/2009] [Accepted: 06/15/2010] [Indexed: 11/26/2022]
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Rene ER, Jin Y, Veiga MC, Kennes C. Two-stage gas-phase bioreactor for the combined removal of hydrogen sulphide, methanol and alpha-pinene. ENVIRONMENTAL TECHNOLOGY 2009; 30:1261-1272. [PMID: 19950468 DOI: 10.1080/09593330903196868] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/28/2023]
Abstract
Biological treatment systems have emerged as cost-effective and eco-friendly techniques for treating waste gases from process industries at moderately high gas flow rates and low pollutant concentrations. In this study, we have assessed the performance of a two-stage bioreactor, namely a biotrickling filter packed with pall rings (BTF, 1st stage) and a perlite + pall ring mixed biofilter (BF, 2nd stage) operated in series, for handling a complex mixture of hydrogen sulphide (H2S), methanol (CH3OH) and alpha-pinene (C10H16). It has been reported that the presence of H2S can reduce the biofiltration efficiency of volatile organic compounds (VOCs) when both are present in the gas mixture. Hydrogen sulphide and methanol were removed in the first stage BTF, previously inoculated with H2S-adapted populations and a culture containing Candida boidinii, an acid-tolerant yeast, whereas, in the second stage, alpha-pinene was removed predominantly by the fungus Ophiostoma stenoceras. Experiments were conducted in five different phases, corresponding to inlet loading rates varying between 2.1 and 93.5 g m(-3) h(-1) for H2S, 55.3 and 1260.2 g m(-3) h(-1) for methanol, and 2.8 and 161.1 g m(-3) h(-1) for alpha-pinene. Empty bed residence times were varied between 83.4 and 10 s in the first stage and 146.4 and 17.6 s in the second stage. The BTF, working at a pH as low as 2.7 as a result of H2S degradation, removed most of the H2S and methanol but only very little alpha-pinene. On the other hand, the BF, at a pH around 6.0, removed the rest of the H2S, the non-degraded methanol and most of the alpha-pinene vapours. Attempts were originally made to remove the three pollutants in a single acidophilic bioreactor, but the Ophiostoma strain was hardly active at pH <4. The maximum elimination capacities (ECs) reached by the two-stage bioreactor for individual pollutants were 894.4 g m(-3) h(-1) for methanol, 45.1 g m(-3) h(-1) for H2S and 138.1 g m(-3) h(-1) for alpha-pinene. The results from this study showed the potential effectiveness of a two-stage bioreactor for treating H2S together with two hydrophilic and hydrophobic VOCs that are typically emitted from wood industries.
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Affiliation(s)
- Eldon R Rene
- Chemical Engineering Laboratory, Faculty ofSciences, University of La Coruña, Rúa Alejandro de la Sota, 1,15008-La Coruña, Spain
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Ravichandra P, Gopal M, Annapurna J. Biological sulfide oxidation using autotrophicThiobacillussp.: evaluation of different immobilization methods and bioreactors. J Appl Microbiol 2009; 106:1280-91. [DOI: 10.1111/j.1365-2672.2008.04095.x] [Citation(s) in RCA: 11] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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Sabumon PC. Development of enhanced sulphidogenesis process for the treatment of wastewater having low COD/SO(4)(2-) ratio. JOURNAL OF HAZARDOUS MATERIALS 2008; 159:616-625. [PMID: 18400386 DOI: 10.1016/j.jhazmat.2008.02.097] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/04/2007] [Revised: 02/22/2008] [Accepted: 02/22/2008] [Indexed: 05/26/2023]
Abstract
An upflow hybrid sulphidogenesis reactor of 1.75 L volume was developed (at oxidation-reduction potential (ORP)=-225+/-25 mV) using flocculent extended aeration process sludge (selected based on screening study at COD/SO(4)(2-) ratio=1) for enhanced sulphidogenesis and COD removal. The reactor was subjected to various loading rate studies at a hydraulic retention time (HRT) of 1 day with COD/SO(4)(2-) ratio of 1.3. At loading rate of 2.5 kg COD/(m(3)day), excellent performance with more than 97% removal of sulphate was achieved within bottom 40% volume of the reactor. At a higher loading rate of 3.75 kg COD/(m(3)day), there was a decrease in both sulphate (70-75%) and COD (50%) removal efficiencies. A controlled and continuous air injection (0.19 L/(L min)) given at 40% volume of the reactor affected sulphide oxidation inside the reactor and enhanced the sulphate reduction in the reactor. The specific sulphate reduction capacity of mixed culture drawn from the bottom part of the reactor was 0.35 kg SO(4)(2-)/(kg VSS day). The results of this study showed that enhanced sulphidogenesis with sulphide inhibition control can maintain sulphate-reducing bacteria (SRB) in anaerobic reactor at low COD/SO(4)(2-) ratios between 1 and 2, with efficient simultaneous removal of COD and SO(4)(2-). The sulphide generated in the system can be recovered as elemental sulphur and/or oxidized back to sulphate.
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Affiliation(s)
- P C Sabumon
- Environmental & Water Resources Engineering Division, Department of Civil Engineering, IIT Madras, Chennai 600036, India.
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González-Sánchez A, Meulepas R, Revah S. Sulfur formation and recovery in a thiosulfate-oxidizing bioreactor. ENVIRONMENTAL TECHNOLOGY 2008; 29:847-853. [PMID: 18724639 DOI: 10.1080/09593330801987657] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/26/2023]
Abstract
This work describes the design and performance of a thiosulfate-oxidizing bioreactor that allowed high elemental sulfur production and recovery efficiency. The reactor system, referred to as a Supernatant-Recycling Settler Bioreactor (SRSB), consisted of a cylindrical upflow reactor and a separate aeration vessel. The reactor was equipped with an internal settler and packing material (structured corrugated PVC sheets) to facilitate both cell retention and the settling of the formed elemental sulfur. The supernatant from the reactor was continuously recirculated through the aerator. An inlet thiosulfate concentration of 100 mmol l(-1) was used. The reactor system was fed with 89 mmol l(-1) d(-1) thiosulfate reaching 98 to 100% thiosulfate conversion with an elemental sulfur yield of 77%. Ninety-three percent of the produced sulfur was harvested from the bottom of the reactor as sulfur sludge. The dry sulfur sludge contained 87% elemental sulfur. The inclusion of an internal settler and packing material in the reactor system resulted in an effective retention of sulfur and biomass inside the bioreactor, preventing the oxidation of thiosulfate and elemental sulfur to sulfate in the aerator and, therefore, improving the efficiency of elemental sulfur formation and recovery.
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Affiliation(s)
- A González-Sánchez
- Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana, Iztapalapa, México DF, Mexico
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Fortuny M, Baeza JA, Gamisans X, Casas C, Lafuente J, Deshusses MA, Gabriel D. Biological sweetening of energy gases mimics in biotrickling filters. CHEMOSPHERE 2008; 71:10-17. [PMID: 18096204 DOI: 10.1016/j.chemosphere.2007.10.072] [Citation(s) in RCA: 31] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/25/2007] [Revised: 10/27/2007] [Accepted: 10/29/2007] [Indexed: 05/25/2023]
Abstract
Removal of hydrogen sulfide from waste and energy-rich gases is required, not only because of environmental health and safety reasons, but also because of operational reasons if such gases have to be used for energy generation. A biotrickling filter for the removal of ultra-high concentrations of H2S from oxygen-poor gases is proposed and studied in this work. Two laboratory-scale biotrickling filters were used to study the startup period and to determine the long-term performance of the gas sweetening process. The inlet H2S concentration ranged from 900 to 12000ppmv and two different packing materials were investigated. There was no toxicity effect observed even at a the highest H2S concentration, and maximum elimination capacities of 280 and 250g H2Sm(-3)h(-1) were obtained at gas contact times of 167 and 180s, respectively. Elemental sulfur and sulfate were found to be the most abundant end-products of the biological oxidation of sulfide when operated under microaerophilic conditions. The biotrickling filter was able to quickly recover its nominal performance after different load increases and system shutdowns simulating field operation. The results reported here show that biotreatment can be an interesting alternative to conventional gas sweetening systems normally used for such applications.
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Affiliation(s)
- Marc Fortuny
- Department of Chemical Engineering, Universitat Autònoma de Barcelona, Edifici Q, Campus de Bellaterra, 08193 Bellaterra, Barcelona, Spain
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Kim JH, Rene ER, Park HS. Biological oxidation of hydrogen sulfide under steady and transient state conditions in an immobilized cell biofilter. BIORESOURCE TECHNOLOGY 2008; 99:583-8. [PMID: 17360177 DOI: 10.1016/j.biortech.2006.12.028] [Citation(s) in RCA: 27] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 10/23/2006] [Revised: 12/22/2006] [Accepted: 12/23/2006] [Indexed: 05/14/2023]
Abstract
The removal of hydrogen sulfide (H(2)S) was investigated in a lab scale biofilter packed with biomedia, encapsulated by sodium alginate and polyvinyl alcohol (PVA). The main H(2)S oxidation products were SO(4)(2-), SO(3)(2-), S(2-) and S(0). The immobilized cell biofilter required no separate acclimatization period and showed high removal efficiencies (RE) within the first few days of experiments. The removal efficiencies in the biofilter were consistently greater than 99% even when H(2)S loading was 6 g m(-3)h(-1). The maximum elimination capacity achieved in this study is 8 g H(2)Sm(-3)h(-1) at a loading rate of 13 g H(2)Sm(-3) h(-1). The response of the immobilized cells to fluctuations in inlet concentration and flow rate was determined by subjecting the biofilter to inlet loads of up to 10 g H(2)Sm(-3)h(-1). The biofilter responded effectively to these shock loading conditions and convalesced rapidly within 4-8h. Pressure drop values were consistently less throughout the operational period. The results from this study suggest that an immobilized cell biofilter is effective in treating H(2)S under steady and transient operating conditions.
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Affiliation(s)
- Jung Hoon Kim
- Department of Civil and Environmental Engineering, University of Ulsan, P.O. Box 18, Ulsan 680-749, South Korea
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van den Bosch PLF, van Beusekom OC, Buisman CJN, Janssen AJH. Sulfide oxidation at halo-alkaline conditions in a fed-batch bioreactor. Biotechnol Bioeng 2007; 97:1053-63. [PMID: 17216660 DOI: 10.1002/bit.21326] [Citation(s) in RCA: 79] [Impact Index Per Article: 4.6] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Abstract
A biotechnological process is described to remove hydrogen sulfide (H(2)S) from high-pressure natural gas and sour gases produced in the petrochemical industry. The process operates at halo-alkaline conditions and combines an aerobic sulfide-oxidizing reactor with an anaerobic sulfate (SO(4) (2-)) and thiosulfate (S(2)O(3) (2-)) reducing reactor. The feasibility of biological H(2)S oxidation at pH around 10 and total sodium concentration of 2 mol L(-1) was studied in gas-lift bioreactors, using halo-alkaliphilic sulfur-oxidizing bacteria (HA-SOB). Reactor operation at different oxygen to sulfide (O(2):H(2)S) supply ratios resulted in a stable low redox potential that was directly related with the polysulfide (S(x) (2-)) and total sulfide concentration in the bioreactor. Selectivity for SO(4) (2-) formation decreased with increasing S(x) (2-) and total sulfide concentrations. At total sulfide concentrations above 0.25 mmol L(-1), selectivity for SO(4) (2-) formation approached zero and the end products of H(2)S oxidation were elemental sulfur (S(0)) and S(2)O(3) (2-). Maximum selectivity for S(0) formation (83.3+/-0.7%) during stable reactor operation was obtained at a molar O(2):H(2)S supply ratio of 0.65. Under these conditions, intermediary S(x) (2-) plays a major role in the process. Instead of dissolved sulfide (HS(-)), S(x) (2-) seemed to be the most important electron donor for HA-SOB under S(0) producing conditions. In addition, abiotic oxidation of S(x) (2-) was the main cause of undesirable formation of S(2)O(3) (2-). The observed biomass growth yield under SO(4) (2-) producing conditions was 0.86 g N mol(-1) H(2)S. When selectivity for SO(4) (2-) formation was below 5%, almost no biomass growth was observed.
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Affiliation(s)
- Pim L F van den Bosch
- Sub-Department of Environmental Technology, Wageningen University, Bomenweg 2, 6700 EV Wageningen, The Netherlands
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Qiu GL, Li YL, Zhao K. Thiobacillus thioparus immobilized by magnetic porous beads: Preparation and characteristic. Enzyme Microb Technol 2006. [DOI: 10.1016/j.enzmictec.2005.12.013] [Citation(s) in RCA: 13] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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Nielsen AH, Vollertsen J, Hvitved-Jacobsen T. Kinetics and stoichiometry of aerobic sulfide oxidation in wastewater from sewers-effects of pH and temperature. WATER ENVIRONMENT RESEARCH : A RESEARCH PUBLICATION OF THE WATER ENVIRONMENT FEDERATION 2006; 78:275-83. [PMID: 16629268 DOI: 10.2175/106143005x94367] [Citation(s) in RCA: 33] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/08/2023]
Abstract
Kinetics and stoichiometry of aerobic chemical and biological sulfide oxidation in wastewater from sewer networks were studied. In this respect, the effects of temperature and pH were investigated in the ranges 10 to 20 degrees C and 5 to 9, respectively. The temperature dependency of sulfide oxidation kinetics was described using an Arrhenius relationship. The effect of pH on the rate of chemical sulfide oxidation is related to the dissociation of hydrogen sulfide (H2S) to hydrogen sulfide ion (HS(-)), with HS(-) being more readily oxidized than H2S. Biological sulfide oxidation exhibited the highest rates at ambient wastewater pH, and the reaction was inhibited at both low and high pH values. Chemical sulfide oxidation was found to produce thiosulfate and sulfate, while elemental sulfur was the main product of biological sulfide oxidation. Based on the investigations, general rate equations and stoichiometric constants were determined, enabling the processes to be incorporated to conceptual sewer process models.
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González-Sánchez A, Alcántara S, Razo-Flores E, Revah S. Oxygen transfer and consumption in a thiosulfate oxidizing bioreactor with sulfur production. Lett Appl Microbiol 2005; 41:141-6. [PMID: 16033511 DOI: 10.1111/j.1472-765x.2005.01741.x] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
Abstract
AIMS To evaluate the contribution of oxygen transfer and consumption in a sulfoxidizing system to increase the elemental sulfur yield from thiosulfate oxidation. METHODS AND RESULTS A 10 l thiosulfate oxidizing bioreactor with suspended cells operating under microaerophilic conditions and a separated aerator with a variable volume of 0.8--1.7 l were operated with a consortium containing mainly Thiobacillus sp. that oxidizes several sulfide species to elemental sulfur and sulfate. From the gas-liquid oxygen balance, the k(L)a was estimated under different operation conditions. A k(L)a of around 200 h(-1) favoured elemental sulfur production and can serve as scale-up criterion. It was further shown that more than 50% of the oxygen fed to the system was consumed in the aerator. CONCLUSIONS The performance of the sulfoxidizing system can be improved by controlling oxygen transfer. SIGNIFICANCE AND IMPACT OF THE STUDY The proposed method for the k(L)a determination was based on the oxygen balance, which incorporates the oxygen concentrations measured in the liquid in steady state, reducing the interference of the response time in the traditional non-steady state methods. This approach can be used to optimize reactors where microaerophilic conditions are desirable.
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Affiliation(s)
- A González-Sánchez
- Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana Iztapalapa, México DF, México
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Krishnakumar B, Majumdar S, Manilal VB, Haridas A. Treatment of sulphide containing wastewater with sulphur recovery in a novel reverse fluidized loop reactor (RFLR). WATER RESEARCH 2005; 39:639-647. [PMID: 15707637 DOI: 10.1016/j.watres.2004.11.015] [Citation(s) in RCA: 54] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/24/2004] [Revised: 10/09/2004] [Accepted: 11/04/2004] [Indexed: 05/24/2023]
Abstract
A novel aerobic bioreactor, the reverse fluidized loop reactor (RFLR) was tested for recovering sulphur from aqueous sulphide in this study. The RFLR contained buoyant carrier particles on which chemolithotrophic sulphide oxidizing bacteria formed a biofilm, which oxidized sulphide to sulphur and separated from the aqueous phase. The redox potential of the RFLR was regulated to control the oxygenation of sulphide for sulphur production. The RFLR was operated without any pH control and under various controlled pHs. The sulphide removal and nature of products formed under various sulphide loading rates and pH were examined. Under pH uncontrolled state, 95% of sulphur was recovered up to 11 kg sulphide/m3 d. The maximum sulphide loading supplied to the reactor was 30 kg sulphide/m3 d at pH 8, of which 90% was completely oxidized and 65% recovered as sulphur. The decline in bacterial sulphide oxidation leads to chemical oxidation of sulphide and subsequent accumulation of intermediary products such as thiosulphate and polysulphide in the reactor.
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Affiliation(s)
- B Krishnakumar
- Environmental Technology Programme, Regional Research Laboratory (CSIR), Industrial Estate (PO), Trivandrum 695 019, India.
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Alcantara S, Velasco A, Muñoz A, Cid J, Revah S, Razo-Flores E. Hydrogen sulfide oxidation by a microbial consortium in a recirculation reactor system: sulfur formation under oxygen limitation and removal of phenols. ENVIRONMENTAL SCIENCE & TECHNOLOGY 2004; 38:918-23. [PMID: 14968883 DOI: 10.1021/es034527y] [Citation(s) in RCA: 47] [Impact Index Per Article: 2.4] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/23/2023]
Abstract
Wastewater from petroleum refining may contain a number of undesirable contaminants including sulfides, phenolic compounds, and ammonia. The concentrations of these compounds must be reduced to acceptable levels before discharge. Sulfur formation and the effect of selected phenolic compounds on the sulfide oxidation were studied in autotrophic aerobic cultures. A recirculation reactor system was implemented to improve the elemental sulfur recovery. The relation between oxygen and sulfide was determined calculating the O2/S2- loading rates (Q(O2)/Q(S)2- = Rmt), which adequately defined the operation conditions to control the sulfide oxidation. Sulfur-producing steady states were achieved at Rmt ranging from 0.5 to 1.5. The maximum sulfur formation occurred at Rmt of 0.5 where 85% of the total sulfur added to the reactor as sulfide was transformed to elemental sulfur and 90% of it was recovered from the bottom of the reactor. Sulfide was completely oxidized to sulfate (Rmt of 2) in a stirred tank reactor, even when a mixture of phenolic compounds was present in the medium. Microcosm experiments showed that carbon dioxide production increased in the presence of the phenols, suggesting that these compounds were oxidized and that they may have been used as carbon and energy source by heterotrophic microorganisms present in the consortium.
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Affiliation(s)
- Sergio Alcantara
- Programa de Biotecnología, Instituto Mexicano del Petróleo, Eje Central Lázaro Cárdenas 152, C.P. 07730, México D.F
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Boonstra J, van Lier R, Janssen G, Dijkman H, Buisman C. Biological treatment of acid mine drainage. BIOHYDROMETALLURGY AND THE ENVIRONMENT TOWARD THE MINING OF THE 21ST CENTURY - PROCEEDINGS OF THE INTERNATIONAL BIOHYDROMETALLURGY SYMPOSIUM 1999. [DOI: 10.1016/s1572-4409(99)80145-x] [Citation(s) in RCA: 24] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 12/13/2022]
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Surface characteristics and aggregation of microbiologically produced sulphur particles in relation to the process conditions. Colloids Surf B Biointerfaces 1996. [DOI: 10.1016/0927-7765(95)01246-x] [Citation(s) in RCA: 43] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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Steudel R. Mechanism for the Formation of Elemental Sulfur from Aqueous Sulfide in Chemical and Microbiological Desulfurization Processes. Ind Eng Chem Res 1996. [DOI: 10.1021/ie950558t] [Citation(s) in RCA: 206] [Impact Index Per Article: 7.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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Buisman CJN, Jspeert PI, Hof A, Janssen AJH, Hagen RT, Lettinga G. Kinetic parameters of a mixed culture oxidizing sulfide and sulfur with oxygen. Biotechnol Bioeng 1991; 38:813-20. [DOI: 10.1002/bit.260380803] [Citation(s) in RCA: 50] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/05/2022]
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