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Producing desulfurized biogas through removal of sulfate in the first-stage of a two-stage anaerobic digestion.
Yun, Yeo-Myeong; Sung, Shihwu; Shin, Hang-Sik; Han, Jong-In; Kim, Hyun-Woo; Kim, Dong-Hoon.
Afiliación
  • Yun YM; College of Agriculture, Forestry and Natural Resource Management, University of Hawaii at Hilo, 200 W. Kawili Street, Hilo, Hawaii, 96720.
  • Sung S; College of Agriculture, Forestry and Natural Resource Management, University of Hawaii at Hilo, 200 W. Kawili Street, Hilo, Hawaii, 96720.
  • Shin HS; Department of Civil and Environmental Engineering, KAIST, 291 Daehak-ro, Yuseong-gu, Daejeon 305-701, Republic of Korea.
  • Han JI; Department of Civil and Environmental Engineering, KAIST, 291 Daehak-ro, Yuseong-gu, Daejeon 305-701, Republic of Korea.
  • Kim HW; Department of Environmental Engineering, Chonbuk National University, 567 Baekjedae-ro, Deokjin-gu, Jeonju, Jeonbuk 561-756, Republic of Korea.
  • Kim DH; Department of Civil Engineering, Inha University, 100 Inha-ro, Nam-gu, Incheon, Republic of Korea.
Biotechnol Bioeng ; 114(5): 970-979, 2017 05.
Article en En | MEDLINE | ID: mdl-27943246
ABSTRACT
In the present work, a two-stage anaerobic digestion system (TSADS) was newly designed to produce biogas with a greatly reduced H2 S content. The role of first (sulfidogenic)-stage digester was not only acidogenesis but also sulfidogenesis (sulfate reduction to H2 S), which would minimize the input of H2 S-producing source in the followed second (methanogenic)-stage digester. For the coexistence of acidogens and sulfate reducing bacteria (SRB) in the sulfidogenic-stage digester, it was found that pH played a crucial role. The acidogenic activity was not affected within a pH range of 4.5-6.0, while it was important to maintain a pH at 5.5 to achieve a sulfate removal efficiency over 70%. The highest sulfate removal attained was 78% at a hydraulic retention time (HRT) of 5 h at pH 5.5 ± 0.1. The H2 S content in the biogas produced in the conventional single-stage digester (SSAD), used as a control, reached 1,650 ± 25 ppmv . In contrast, the biogas produced in the methanogenic-stage digester of the developed process had an H2 S content of 200 ± 15 ppmv . Microbial analysis, done by the next generation sequencing technique, clearly showed the changes in community under different operating conditions. Desulfovibrio bastinii (4.9%) played a key role in sulfate removal in the sulfidogenic-stage of the TSADS owing to its characteristics of a short doubling time and growth in an acidic environment. Biotechnol. Bioeng. 2017;114 970-979. © 2016 Wiley Periodicals, Inc.
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Sulfatos / Reactores Biológicos / Biocombustibles Idioma: En Revista: Biotechnol Bioeng Año: 2017 Tipo del documento: Article

Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Sulfatos / Reactores Biológicos / Biocombustibles Idioma: En Revista: Biotechnol Bioeng Año: 2017 Tipo del documento: Article