Biohydrogen production from wheat straw hydrolysate using Caldicellulosiruptor saccharolyticus followed by biogas production in a two-step uncoupled process
(2013) In International Journal of Hydrogen Energy 38(22). p.9121-9130- Abstract
- A two-step, un-coupled process producing hydrogen (H2) from wheat straw using Caldicellulosiruptor
saccharolyticus in a ‘Continuously stirred tank reactor’ (CSTR) followed by
anaerobic digestion of its effluent to produce methane (CH4) was investigated. C. saccharolyticus
was able to convert wheat straw hydrolysate to hydrogen at maximum production
rate of approximately 5.2 L H2/L/Day. The organic compounds in the effluent collected from
the CSTR were successfully converted to CH4 through anaerobic digestion performed in an
‘Up-flow anaerobic sludge bioreactor’ (UASB) reactor at a maximum production rate of 2.6 L
CH4/L/day. The maximum energy output of the process (10.9 kJ/g of... (More) - A two-step, un-coupled process producing hydrogen (H2) from wheat straw using Caldicellulosiruptor
saccharolyticus in a ‘Continuously stirred tank reactor’ (CSTR) followed by
anaerobic digestion of its effluent to produce methane (CH4) was investigated. C. saccharolyticus
was able to convert wheat straw hydrolysate to hydrogen at maximum production
rate of approximately 5.2 L H2/L/Day. The organic compounds in the effluent collected from
the CSTR were successfully converted to CH4 through anaerobic digestion performed in an
‘Up-flow anaerobic sludge bioreactor’ (UASB) reactor at a maximum production rate of 2.6 L
CH4/L/day. The maximum energy output of the process (10.9 kJ/g of straw) was about 57%
of the total energy, and 67% of the energy contributed by the sugar fraction, contained in
the wheat straw. Sparging the hydrogenogenic CSTR with the flue gas of the UASB reactor
((60% v/v) CH4 and (40% v/v) CO2) decreased the H2 production rate by 44%, which was due
to the significant presence of CO2. The presence of CH4 alone, like N2, was indifferent to
growth and H2 production by C. saccharolyticus. Hence, sparging with upgraded CH4 would
guarantee successful hydrogen production from lignocellulosic biomass prior to anaerobic
digestion and thus, reasonably high conversion efficiency can be achieved. (Less)
Please use this url to cite or link to this publication:
https://lup.lub.lu.se/record/3954432
- author
- Pawar, Sudhanshu LU ; Nkemka, Valentine LU ; Zeidan, Ahmad LU ; Murto, Marika LU and van Niel, Ed LU
- organization
- publishing date
- 2013
- type
- Contribution to journal
- publication status
- published
- subject
- keywords
- Caldicellulosiruptor saccharolyticus Hydrogen CSTR Methane UASB Lignocellulosic biomass
- in
- International Journal of Hydrogen Energy
- volume
- 38
- issue
- 22
- pages
- 9121 - 9130
- publisher
- Elsevier
- external identifiers
-
- wos:000322562800008
- scopus:84879939329
- ISSN
- 1879-3487
- DOI
- 10.1016/j.ijhydene.2013.05.075
- language
- English
- LU publication?
- yes
- id
- 2e5cebe4-cf23-46c4-82fa-71f2813f2ce0 (old id 3954432)
- date added to LUP
- 2016-04-01 10:38:43
- date last changed
- 2022-02-02 19:42:46
@article{2e5cebe4-cf23-46c4-82fa-71f2813f2ce0,
abstract = {{A two-step, un-coupled process producing hydrogen (H2) from wheat straw using Caldicellulosiruptor<br/><br>
saccharolyticus in a ‘Continuously stirred tank reactor’ (CSTR) followed by<br/><br>
anaerobic digestion of its effluent to produce methane (CH4) was investigated. C. saccharolyticus<br/><br>
was able to convert wheat straw hydrolysate to hydrogen at maximum production<br/><br>
rate of approximately 5.2 L H2/L/Day. The organic compounds in the effluent collected from<br/><br>
the CSTR were successfully converted to CH4 through anaerobic digestion performed in an<br/><br>
‘Up-flow anaerobic sludge bioreactor’ (UASB) reactor at a maximum production rate of 2.6 L<br/><br>
CH4/L/day. The maximum energy output of the process (10.9 kJ/g of straw) was about 57%<br/><br>
of the total energy, and 67% of the energy contributed by the sugar fraction, contained in<br/><br>
the wheat straw. Sparging the hydrogenogenic CSTR with the flue gas of the UASB reactor<br/><br>
((60% v/v) CH4 and (40% v/v) CO2) decreased the H2 production rate by 44%, which was due<br/><br>
to the significant presence of CO2. The presence of CH4 alone, like N2, was indifferent to<br/><br>
growth and H2 production by C. saccharolyticus. Hence, sparging with upgraded CH4 would<br/><br>
guarantee successful hydrogen production from lignocellulosic biomass prior to anaerobic<br/><br>
digestion and thus, reasonably high conversion efficiency can be achieved.}},
author = {{Pawar, Sudhanshu and Nkemka, Valentine and Zeidan, Ahmad and Murto, Marika and van Niel, Ed}},
issn = {{1879-3487}},
keywords = {{Caldicellulosiruptor saccharolyticus Hydrogen CSTR Methane UASB Lignocellulosic biomass}},
language = {{eng}},
number = {{22}},
pages = {{9121--9130}},
publisher = {{Elsevier}},
series = {{International Journal of Hydrogen Energy}},
title = {{Biohydrogen production from wheat straw hydrolysate using Caldicellulosiruptor saccharolyticus followed by biogas production in a two-step uncoupled process}},
url = {{https://lup.lub.lu.se/search/files/2018224/3954433.pdf}},
doi = {{10.1016/j.ijhydene.2013.05.075}},
volume = {{38}},
year = {{2013}},
}