Biogas desulfurization and calorific value enhancement in compact H2S/CO2absorption units coupled to a photobioreactor

被引:11
|
作者
Rocher-Rivas R. [1 ]
González-Sánchez A. [2 ]
Ulloa-Mercado G. [3 ]
Muñoz R. [4 ]
Quijano G. [1 ]
机构
[1] Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro
[2] Instituto de Ingeniería, Universidad Nacional Autónoma de México, Circuito Escolar, Ciudad Universitaria, Mexico City
[3] Departamento de Biotecnología y Ciencias Alimentarias, Instituto Tecnológico de Sonora, Ciudad Obregón
[4] Institute of Sustainable Processes, University of Valladolid, Dr. Mergelina s/n., Valladolid
来源
关键词
Biogas; Calorific value; Desulfurization; Gas-liquid mass transfer; Microalgae-bacteria systems; Photobioreactor;
D O I
10.1016/j.jece.2022.108336
中图分类号
学科分类号
摘要
Biogas desulfurization is in many cases the main purification step required for energy generation. This is the case of wastewater treatment plants, waste management facilities or intensive livestock farms where the produced biogas is burned in situ to generate thermal and electrical power. The potential of compact H2S/CO2 absorption units coupled to a photobioreactor for biogas desulfurization was investigated in the present study. Two absorption unit configurations, bubble column and airlift, were evaluated in terms of H2S and CO2 removal at biogas retention times of 10 and 30 min, and liquid-to-biogas flowrate ratios of 1/1 and 4/1. Complete H2S removal was achieved in both absorption unit configurations regardless of the biogas retention time or liquid-to-biogas flowrate ratio applied. These results confirmed the feasibility of setting biogas retention times as short as 10 min, resulting in absorption units up to 49-fold smaller than that required for biogas upgrading up to biomethane. Biogas calorific value increases from 14.7 ± 4.0-19.3 ± 7.2 % were observed in the airlift configuration, while increases from 5.5 ± 2.2-25.2 ± 4.0 % were recorded in the bubble column. N-NO3- removal rates ranging from 16 ± 4-25 ± 5 g m-3 d-1 were recorded under the experimental conditions tested, no significant differences in nitrogen removal being observed between the airlift and bubble column configurations. The significant removal of CO2 that can be achieved at short biogas retention times certainly constitutes a motivation for implementing photobioreactors for biogas desulfurization, broadening the application niches of microalgae-bacteria systems in the context of renewable energy production. © 2022 Elsevier Ltd.
引用
收藏
相关论文
共 50 条
  • [1] Chemical absorption of H2S for biogas purification
    Horikawa, MS
    Rossi, F
    Gimenes, ML
    Costa, CMM
    da Silva, MGC
    [J]. BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2004, 21 (03) : 415 - 422
  • [2] Factors Influencing Chemical Absorption of CO2 and H2S in Biogas Purification: A Review
    Maile, O. I.
    Tesfagiorgis, H. B.
    Muzenda, E.
    [J]. WORLD CONGRESS ON ENGINEERING AND COMPUTER SCIENCE, WCECS 2015, VOL II, 2015, : 619 - 622
  • [3] Simultaneous absorption of CO2 and H2S from biogas by capillary membrane contactor
    Rongwong, Wichitpan
    Boributh, Somnuk
    Assabumrungrat, Suttichai
    Laosiripojana, Navadol
    Jiraratananon, Ratana
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2012, 392 : 38 - 47
  • [4] H2S oxidation coupled to nitrate reduction in a two-stage bioreactor: Targeting H2S-rich biogas desulfurization
    Flores-Cortes, Mauricio
    Perez-Trevilla, Jaime
    Cuervo-Lopez, Flor de Maria
    Buitron, German
    Quijano, Guillermo
    [J]. WASTE MANAGEMENT, 2021, 120 : 76 - 84
  • [5] H2S oxidation coupled to nitrate reduction in a two-stage bioreactor: Targeting H2S-rich biogas desulfurization
    Flores-Cortés, Mauricio
    Pérez-Trevilla, Jaime
    de María Cuervo-López, Flor
    Buitrón, Germán
    Quijano, Guillermo
    [J]. Waste Management, 2021, 120 : 76 - 84
  • [6] SOUND ABSORPTION AND VELOCITY IN H2S AND CO2/H2S MIXTURES
    SHIELDS, FD
    [J]. JOURNAL OF THE ACOUSTICAL SOCIETY OF AMERICA, 1969, 45 (02): : 481 - &
  • [7] Comparison of Various Alkaline Solutions for H2S/CO2-Selective Absorption Applied to Biogas Purification
    Dubois, Lionel
    Thomas, Diane
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2010, 33 (10) : 1601 - 1609
  • [8] Preliminary study on microbial desulfurization: Targeting h2s removal from biogas with a bioscrubber
    Prasetyo J.
    Senda S.P.
    Prasetyo D.H.
    Rahmawati N.
    Setyowati A.D.
    [J]. Industrial Biotechnology, 2020, 16 (03) : 182 - 186
  • [9] SELECTIVE ABSORPTION OF H2S FROM CO2 - FACTORS CONTROLLING SELECTIVITY TOWARD H2S
    SRINIVASAN, V
    AIKEN, RC
    [J]. FUEL PROCESSING TECHNOLOGY, 1988, 19 (02) : 141 - 152
  • [10] Investigations of H2S absorption rate and simultaneous H2S and CO2 absorption rate in mixtures of propylene carbonate and triethanoloamine
    Pohorecki, R.
    Mozenski, C.
    [J]. Inzynieria Chemiczna i Procesowa, 17 (02):