Abstract:
Waste-to-bioenergy conversion from lignocellulosic materials like water hyacinth (WH) and
coffee husk (CH) can lead to multiple benefits such as freshwater body protection, eutrophication,
and renewable energy generation besides environmental protection. Water hyacinth is causing
significant damage to freshwater ecosystems disrupting ecosystem processes while coffee husks
are openly burnt, thus causing loss of energy, resources, and environmental harm contributing to
various diseases. However, determining how to convert it into biogas requires understanding the
material's chemical components, which are mostly complicated lignocellulosic materials. The
production of biogas can be restricted and its degradability is impacted by the intricate structure
of lignocellulosic materials. In addition, WH and CH have lower nitrogen content and moisture
levels compared to food waste. These factors can hinder microbial activity and slow down the
anaerobic digestion process. However, by introducing easily degradable waste such as food waste
into the co-digestion mixture, these limitations can be compensated. Moreover, food waste also
helps in balancing the carbon-to-nitrogen ratio, promoting faster hydrolysis rates, and improving
overall digestion efficiency. Furthermore, WH and CH were ground using a coffee grinder to
decrease cellulose crystallinity and reduce particle size in order to enhance the substrate's surface
area and improve enzymatic accessibility, thereby facilitating the efficient conversion of these
materials into biogas. Thus, this study examined the impacts of substrate mix proportions,
inoculum-substrate ratios (ISR), and initial pH levels on biodegradability and biogas production
for lignocellulosic materials digested with Food Waste (FW) under mono-and co-digestion modes.
To assess the potential of organic materials as biogas resources, an investigation was conducted to
characterize food waste, water hyacinth, and coffee husk in terms of their volatile matter, moisture
content, ash content, fiber content, carbon content, sulfur content, and nitrogen content, and then
three sets of batch experiments were performed under mesophilic conditions. The first group
included eight digesters that treated the FW/WH at varying mixing ratios (i.e., 100:0, 50:50, 40:60,
0:100) and varying ISR (0.5, 0.75, 1, and 2) at FW/WH of 50:50. Second, the effect of FW/CH
ratios (100:0, 60:40, 50:50, 40:60, 0:100) and initial pH levels (5, 6, 6.5, and 7.5) with a FW/CH
ratio of 60:40 were evaluated to get the initial optimal conditions that allows the maximum biogas
production. The third set involved seven digesters that tested the CH/WH/FW at different blend
proportions (i.e., 100:0:0, 0:100:0, 35:35:30, 30:30:40, 25:25:50, 20:20:60 and 0:0:100). The
modified logistic, modified Gompertz, and first-order kinetic models were used to simulate the
experimental results to portray the kinetics of the co-digestion. The volatile matter content in food
waste, water hyacinth, and coffee husk was found to be 90.25, 87.24, and 89.82% respectively.
The concentration for cellulose, hemicellulose, and lignin in WH were 41.39, 19.33, and 8.31%,
respectively compared to 24.88, 28.96, and 23.16% for CH. The characteristics of each material
indicated their potential for bioenergy recovery through anaerobic digestion. In addition, the
carbohydrate component of FW was higher than that of CH and WH, indicating the higher
biodegradability of FW, which improves the VFA quantities in the biodigester and facilitates the
microbial activities to degrade lignocellulose. In this study, the C/N ratio of WH is about 25.5,
which is within the optimum range for the methanation process. The C/N ratio of CH was 34.46,
which is comparatively high and indicates some nitrogen deficiency while that for FW was 19.9,
which signifies some carbon deficiency. The results specified the potential for nutrients
complementing in co-digestion of lignocellulosic materials with food waste, for better biogas
production. For the first test, maximum biogas production of 495.45 ml/gVS was observed at
WH/FW of 40:60% with a maximum biodegradability (BDfpc) of 89.3%. The modified Gompertz
equation fits accurately with experimental data. For the second set, peak biogas yield was 540.78
xv
ml/gVS with synergy of 1.46, as well as the highest BDfpc and organic biodegradation degree (ηBD)
of 85.64 and 56.80%, respectively, for FW/CH ratio of 60:40 and pH 7, representing 164% increase
over mono digestion of CH. The theoretical biogas production potential of the CH, WH, and FW
were 438.74 ml/gVS, 608.46 ml/gVS, and 759.92 ml/gVS, respectively. The findings showed that
without pretreatment, the mono-digestion of CH is not viable for biogas production due to its high
lignin content. Finally, for the third set, the maximum biogas yield of 572.60 ml/gVS, the highest
BDfpc of 89.22%, and ηBD of 57.82% was obtained at a blend ratio of 25:25:50, leading to 179.71%
increment compared to CH mono-digestion. The positive synergy reached in this experiment may
be due to multiple-factor couplings, including increased buffering capacity and improved nutrient
balance. Three substrates co-digestion comparatively enhanced biogas yield and its quality over
two substrates co-digestion. For the second and third sets, a modified logistic model outperformed
others with the best fit, and high correlation suggesting that it might well describe the kinetics of
co-digestion at different initial conditions. This study provided evidence that the biodegradability
and subsequent biogas yield can be positively influenced by the co-digestion of multiple substrates
and the introduction of inoculum. In order to enhance the biodegradation rate and biogas
production from lignocellulosic materials, the current study findings highlight the significance of
increasing easily biodegradable waste fractions in the co-digestion and inoculum-substrate ratios
under controlled initial conditions. Pretreating these substrates with alkali-assisted ultrasonication,
can significantly improve the accessibility of cellulose and hemicellulose, remove lignin barriers,
and reduce glucose crystallinity, eventually improving the overall performance of bioconversion
processes. Thus, it is recommended that future studies apply this pretreatment technology to
improve biogas production. Additionally, further research is necessary to examine the chemical
oxygen demand and biochemical oxygen demand of substrates, as well as the microbial
community, and understand the intermediate reactions occurring during co-digestion.