Open AccessEnhancing bioenergy production from food waste by in situ biomethanation: Effect of the hydrogen injection point
Author(s) -
OkoroShekwaga Cynthia Kusin,
Ross Andrew,
CamargoValero Miller Alonso
Publication year - 2021
Publication title -
food and energy security
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.253
H-Index - 25
ISSN - 2048-3694
DOI - 10.1002/fes3.288
Subject(s) - biogas , food waste , bioenergy , anaerobic digestion , carbon dioxide , resource recovery , chemistry , methane , pulp and paper industry , biofuel , valorisation , renewable resource , hydrogen , environmental science , renewable energy , waste management , environmental engineering , wastewater , biology , organic chemistry , ecology , engineering
The increasing rate of food waste (FW) generation around the world is a growing environmental concern, notwithstanding, its valorisation through anaerobic digestion (AD) makes it a potential resource. Moreover, there is a growing demand to optimise the biomethane from AD for gas‐to‐grid (GtG) and vehicular applications. This has spurred researches on hydrogen gas (H 2 ) injection into AD systems to enhance the biological conversion of H 2 and carbon dioxide (CO 2 ) to methane (CH 4 ), a process known as biomethanation. A simplistic approach for biomethanation is to add H 2 directly into working AD reactors (in situ biomethanation). However, a competition for the injected H 2 towards other biological reactions besides H 2 /CO 2 conversion to CH 4 could follow, thus, reducing the efficiency of the system. Hence, this study was conducted to understand how different H 2 injection points would affect H 2 /CO 2 conversion to CH 4 during FW in situ biomethanation, to identify an optimal injection point. Experiments were designed using H 2 equivalent to 5% of the head‐space of the AD reactor at three injection points representing different stages of AD: before volatile fatty acids (VFA) accumulation, during VFA accumulation and at depleted VFA intermediates. Lower potential for competitive H 2 consumption before the accumulation of VFA enabled a high H 2 /CO 2 conversion to CH 4 . However, enhanced competition for soluble substrates during VFA accumulation reduced the efficiency of H 2 /CO 2 conversion to CH 4 when H 2 was added at this stage. In general, 12%, 4% and 10% CH 4 increases as well as 39%, 25% and 34% CO 2 removal were obtained for H 2 added before VFA accumulation, during VFA accumulation and at depleted VFA intermediates, respectively. For immediate integration of biomethanation with existing AD facilities, it is suggested that the required H 2 be obtained biologically by dark fermentation.