Fresh banana pseudo-stems as a tropical lignocellulosic feedstock for methane production
© The Author(s). 2016
Received: 17 July 2016
Accepted: 12 September 2016
Published: 3 October 2016
The banana pseudo-stem is a low-lignin-content lignocellulosic biomass that can be used for methane production. In recent years, anaerobic digestion (AD) of dried banana stems for methane production has attracted considerable attention. However, there is limited information regarding methane production from the fresh banana pseudo-stem. The direct usability of fresh banana stems as a resource for renewable energy production through AD is a called upon prerequisite for an improved waste management system culminating in a sustainable as well as socioeconomic development of local banana-producing communities.
In this study, three series of experiments were performed simultaneously to investigate the methane production from fresh banana pseudo-stems for the first time. The tests included size reduction, enzyme addition, and co-digestion of banana stems with cow manure.
The achieved methane yields were 287, 340, to 347 mL g−1 volatile solids for the banana stem with particle sizes of 5, 10, and 20 mm, respectively. The highest yield was obtained at the particle size of 20 mm, showing a 21 % increase compared to the particle size of 5 mm. However, the particle size of 5 mm showed a high initial rate of hydrolysis evident by the highest hydrolysis rate constant of 0.152 d−1 as compared to 0.110 d−1 for the 20-mm particle size. The addition of enzyme and co-digestion improved the rate of hydrolysis evident by a high rate constant as compared to the control though there was no improvement in the ultimate methane production.
This study demonstrates the usability of the fresh banana stem for efficient and high methane production after simply applying a minimal size reduction. The implementation of such a study will benefit society especially rural banana-producing areas both toward renewable energy generation and sustainable waste management. These could lead to job creation and an improved standard of living.
Bananas are widely consumed fruits with over 140 metric tons produced annually. India and China are leading banana producers owning about half of the total production . Hainan is the largest tropical island in China, which had a population of 9,108,000 people at the end of 2015 and harbors abundant biomass resources. In the agricultural sector, banana trees are widely planted and the production has a primary economic importance. Annually, about 12.1 million tons of bananas are produced in China with 2.0 million tons coming from Hainan province. By using the residue/product ratio of 2.4 , 4.8 million tons of banana pseudo-stems, sheaths, central cylinders, and leaves is produced in Hainan province . The stem which is the major component is often abandoned in the plantation or processed into low-grade animal feed by local farmers. However, these treatments may cause serious environmental and ecological problems such as eutrophication. On the other hand, the banana stem contains a large amount of biodegradable biomass that can be a potential resource. Therefore, it is imperative to find environmentally friendly methods for both pollutant control and efficient utilization of the waste biomass from the banana stem.
The anaerobic digestion (AD) process, where biogas can be generated and upgraded to bio-methane which can be a substitute for natural gas, is widely recognized as a promising technique for the treatment of various organic wastes [4, 5]. However, low methane yield and poor substrate degradation rate are frequently reported when lignocellulosic biomasses are used as feedstock . The recalcitrant structure of lignocellulosic wastes often requires suitable treatment to change its chemical and physical property in order to improve the biodegradability for enhanced methane production and substrate utilization . In order to increase the rate of hydrolysis and optimize the biological conversion, physical, chemical, and biological pretreatments are often implemented, e.g., milling/grinding, acid or alkali treatment, and the addition of enzymes and microorganisms [6, 8–10]. Mechanical size reduction for banana stems could increase the rate of degradation and the methane yield by increasing the surface area of the substrates for an efficient enzymatic or microbial attack. Mild, environmentally friendly pretreatments using enzymes or cellulose-degrading microorganisms have provided another promising alternative for the enhancement of hydrolysis in the AD of lignocellulosic wastes [8, 9]. Although the cost of enzymatic treatment is relatively high and enzyme activity can be lost to some extent, compared to pretreatments with microorganisms, enzymes can act in the presence of different toxic and recalcitrant feedstock with a low requirement to environmental conditions such as pH, temperature, and salinity [8, 11]. The above research activities provide some potential strategies to enhance the AD of lignocellulosic waste; however, to date, the pretreatment methods for improving methane production of tropical and subtropical lignocellulosic waste such as banana stems are still limited.
Considering the economic factors, some large full-scale biogas plants have already evaluated the feasibility of co-digesting manure with the banana stem in Hainan Island . Banana stems and other tropical biomass can be used as supplementary substrates in the biogas plant for mitigating and optimizing both feedstock supply costs and environmental impact of livestock waste treatment. Moreover, the addition of suitable substrates can provide a better process stability by balancing the macro- and micronutrients and by avoiding the accumulation toxic by-products [13, 14]. Meanwhile, a wide range of nutrients and balanced C/N ratio among co-digestion might avoid ammonia through simple dilution.
Studies on the AD of banana waste most often reported the pre-dried banana stem used as a substrate for methane production [6, 15, 16]. Since the banana stem is bulky in nature, the main constraint in the value chain will be drying to reduce bulkiness and ease of transport. However, dry substrates are prone to floatation in an anaerobic digester  and hence poor contact with the microbial consortium. Also, studies on methane production from wet or fresh banana stem are scarcely reported in scientific literature. It is, therefore, worth investigating the production of methane from wet or fresh banana stems.
The current study aimed primarily at evaluating the feasibility of using the fresh banana stem as feedstock for methane production and to concomitantly investigate the effects of physical (size reduction ranging from 5 to 20 mm) and enzymatic treatment (Celluclast and MethaPlus) on the methane potential, biodegradability, and methane production rate. Co-digestion of the fresh banana stem with cow manure was also investigated to test the applicability of banana stem as a lignocellulosic co-substrate in methane production from animal manure. Such a study will therefore entail the transformation of waste into value-added products, thus addressing both the environmental pollution and inefficient utilization of resources. Generation of renewable energy from fresh banana stems could benefit rural communities which are often deprived of electrical energy. This may also reduce the dependence on firewood or charcoal which are known to provide for domestic energy requirements. Such a development could help save trees, lower emissions that cause climate change, and reduce the fumes from millions of tons of firewood that threaten the health of the improvised local communities.
Substrates and inoculum
The banana stem used in this study was collected from a banana farm in Yongzhuang village of Haikou city, Hainan province, China (19° 59′ 05.4″ N 110° 15′ 21.7″ E). The tough outer waxy layers and inflorescence centers were handily separated, thereby keeping only the tender intermediary succulent section. The samples were well packed in gas-tight containers and transported to the Department of Biotechnology at the University of Lund, Sweden, within 24 h. The substrate was stored in a refrigerator at 4 °C prior to use. The cow manure (CM) used as a co-substrate was obtained from an animal farm in Plönninge (Skåne, Sweden).
Characteristics of substrates and inoculum
5.53 ± 0.11
4.47 ± 0.05
5.00 ± 0.34
3.99 ± 0.34
4.82 ± 0.16
3.78 ± 0.23
6.86 ± 0.20
5.81 ± 0.21
1.98 ± 0.02
1.15 ± 0.02
Substrate pretreatments and co-digestion
Three parallel batch AD tests were performed in the present study to investigate the effect of size reduction, enzyme addition, and co-digestion of the banana stem with CM.
Only the B20 banana stem sample was investigated as per enzymatic treatment. The enzyme used in this study was a pure enzyme or mix enzyme. The first was a pure Celluclast (cellulase) 1.5 L, obtained from Novozyme Inc. (Denmark) which was derived from Trichoderma reesei. The optimum activity was 700 endoglucanase (EGU) g−1 or 70 filter paper units (FPU) g−1 at pH 4.5–6.0 and 50–60 °C. The second was MethaPlus® L100 obtained from DSM Biogas (Delft, Netherlands). MethaPlus® L100 is a complex enzyme mixture which is active in a pH range of 4.5 to 8.0. Under typical methane fermentation conditions, MethaPlus® L100 is active in a temperature range of 35–50 °C. The enzymes (Celluclast 1.5 L and MethaPlus® L100) were added into the reactors prior to the AD assay of B20 wherein 0.19 and 1.14 mL of Celluclast was added corresponding to an enzyme load of 10 and 60 FPU g−1 VS. For MethaPlus® L100, 2.2 mL was added which corresponded to an enzyme loading 10 FPU g−1 VS (Fig. 1).
Co-digestion with cow manure
The co-digestion test was performed with all three banana stem particle sizes (B5, B10, and B20). In order to investigate the performance of co-digestion by adding a small part of CM, two VS-based regimes were designed and tested, i.e., 15 % CM plus 85 % banana stems and the second contained a higher amount of CM, i.e., 35 % and a less fraction of the banana stem (65 %) (see Fig. 1).
Biochemical methane potential tests
Three series of biochemical methane potential (BMP) assays (Fig. 1), namely BMP of mechanical-pretreated samples (size reduction), BMP of enzyme-treated samples, and BMP of co-digested banana stem and CM, were performed in parallel with the aid of an automatic methane potential test system (AMPTS II) (Bioprocess Control AB, Sweden) under mesophilic conditions (37 ± 0.5 °C). The batch digestion trials were conducted in 15 reactors of 500 mL each. The substrates and inoculum were mixed at the ratio of 1:2 in terms of gram VS  to avoid potential substrate inhibition and low microbial density. All the reactors were sealed with rubber stoppers and connected to a mechanical agitator to provide complete mixing. During the test, only methane was measured as carbon dioxide was scrubbed off from the produced gas with the aid of concentrated NaOH. A detailed description of the AMPTS is found in and the experimental protocol was performed according to previous studies by Badshah et al. .
One blank and two sets of controls were included in the test. In the blank experiment, only the inoculum was used to measure the indigenous methane production from the inoculum, which was subtracted from the total methane produced from all test samples. The positive control with cellulose (Avicel PH-101, Sigma-Aldrich, St. Louis, MO, USA) was used to give an idea of the inoculum response toward “standard” substrates. The BMP of Celluclast/MethaPlus was also evaluated (third control) and subtracted from the enzyme-treated test samples. All tests were performed in triplicates and terminated after 34 days of incubation when the daily methane production was less than 1 % of the total methane production. The methane produced was automatically normalized to standard conditions, i.e., 0 °C and 1013 hPa by AMPTS software.
The content of TS and VS of all the samples including those of the different particle sizes and CM was determined in triplicates according to standard methods . The pH was measured by the automatic titrator TitroLine Easy (Schott Instrument, Germany). The content of hemicellulose, cellulose, and lignin were determined by analysis of neutral detergent fiber (NDF), acid detergent fiber (ADF), and acid detergent lignin (ADL) in ground samples as described in a previous study . The elements of C, H, and N of the banana stems were determined using a CE-440 elemental analyzer (EAI Co., USA), while S and O were determined by a 5E-8S II sulfur analyzer (Kaiyuan Co., China) and a PE 2400 II elemental analyzer (Perkin Elmer, USA), respectively. Chemical oxygen demand (COD) was determined with the aid of the Dr. Lange test kit LCK 914 (HACH LANGE GmbH, Germany).
where BMP(t) is the methane potential (N mL g−1 VS) at time t (days), BMP∞ is the maximum or ultimate methane potential (N mL g−1 VS) of the substrate, k is the rate constant or hydrolysis rate constant (d−1), and θ is the lag time constant (days).
Dixon’s test (P ≤ 0.05) was used to check for outliers in the replicate-BMP tests. One-way analysis of variance (ANOVA) was performed with the Statistical Package for the Social Science (SPSS), version 16, to assess statistical differences in methane yield between the various sample sizes, enzymatic treatments, and co-digestion at a 95 % confidence level to accept or reject the null hypothesis.
Results and discussion
Inoculum activity and substrate characterization
The inoculum showed a good methanogenic activity which was deduced from the positive control experiment using cellulose as the substrate. The BMP value of cellulose was 368 mL g−1 VS after 34 days of digestion, which represented 89 % of the theoretical yield of 415 mL g−1 VS [22, 23].
Compositional analysis of banana pseudo-stem
Contents (% TS)
30.08 ± 1.86
27.79 ± 0.88
6.08 ± 0.05
38.44 ± 0.42
5.03 ± 0.05
43.10 ± 0.32
1.24 ± 0.07
0.09 ± 0.01
Effect of particle sizes on methane production rate and BMP of banana stems
The simulation results of the anaerobic digestion process of banana stem with/without cow manure
BMP (mL g−1 VS)
k h (d−1)
289 ± 1.81
B5 + 15 % CM
287 ± 26.39
B5 + 35 % CM
311 ± 3.20
340 ± 18.18
B10 + 15 % CM
290 ± 16.39
B10 + 35 % CM
278 ± 8.34
347 ± 15.85
B20 + 15 % CM
296 ± 19.03
B20 + 35 % CM
322 ± 9.18
B20 + 10 FPU (C15L)
320 ± 20.60
B20 + 60 FPU (C15L)
343 ± 14.20
B20 + 10 FPU (Met100)
336 ± 31.10
The 34-day methane yields (mL g−1 VS) were 289 ± 1.81, 340 ± 18.18, and 347 ± 15.85 for B5, B10, and B20, respectively, wherein there was no significant difference (P ≤ 0.05) between B10 and B20. On the other hand, the B5 methane yield was significantly lower (P ≤ 0.05) than B10 and B20. The methane yields, therefore, showed a decreasing trend wherein B5 < B10 < B20 (Fig. 1), indicating an increase in methane yield with increasing particle size. The B20 and B10 showed a 20 and 18 % increase in methane yield, respectively, as compared to B5 which was significantly different (P ≤ 0.05). The results of decreasing BMP with decreasing particle size are in stark contrast with other studies where decreasing particle size has been reported to garner an improvement in methane yields [7, 26]. The explanation has liaised to morphological structures of the banana stem. The dermal tissues in the banana stem consist of well-defined epidermis with radial oblong, wide cells with thick cuticles . When the banana stem was reduced in size by cutting, the highly concentrated juice from the oblong cells could have been lost. That is, the smaller the particle size, the more organic juice was lost. In fact, the COD of the clear juice collected during chopping of samples showed an organic content value (dissolved COD) of 4401 mg L−1. It is plausible, therefore, to state that banana juice contains soluble organic compounds, easily convertible to methane that could have been lost during extreme size reduction. This may also occur during drying prior to AD. This hypothesis may explain why the methane yields in the present study, using wet/fresh banana stem, are significantly higher than those reported in studies wherein pre-dried samples are used. Another plausible explanation is the decrease in particle size increased the surface area of the banana stem that made it more accessible for the bacterial/enzymatic attack, thus leading to an accelerated hydrolysis evident by the increasing of the hydrolysis constant. It is probable that the accelerated hydrolysis may have led to the accumulation of volatile fatty acids which might have inhibited the biogas process and hence the poor BMP values [29, 30]. Results also showed that the larger particle size (B20) had the highest biodegradability.
Effect of enzyme addition on the BMP of B20 banana stem samples
Effect of co-digestion with different fractions of manures on AD of banana stem samples
The methane yields of B5 co-digested with 15 and 35 % of CM were 287 ± 26.39 and 311 ± 3.20 mL g−1 VS, respectively. The methane yields were 290 ± 16.39 and 278 ± 8.34 mL g−1 VS for B10 and 296 ± 19.03 and 322 ± 9.18 mL g−1 VS for B20, both co-digested with 15 and 35 % of CM addition, respectively. The results show that co-digestion did not lead to a significant (P ≤ 0.05) improvement in methane yield. In fact, for B10 and B20, mono-digestion showed significantly higher methane yields (P ≤ 0.05). Co-digestion may lead to either synergy wherein higher yields are achieved through the provision of vital nutrients and buffering or antagonism where lower yields are obtained . In the present study, it is probable that the inoculum was rich in buffering (partial alkalinity was 3600 mg L−1) and may have contained the necessary nutrients and cofactors needed for the biochemistry of methane production.
Though many studies have shown an improvement of anaerobic co-digestion compared to the mono-digestion [33, 34], this study showed that mono-digestion was a better option in terms of methane yields as compared to co-digestion. This might be because of the appropriate C/N of the banana stem for AD and the fact that the inoculum used in the present study showed a rather high partial alkalinity. The above conditions should have provided a conducive environment for the mono-AD of the banana stem.
The energy potential of fresh pseudo-banana stem
Many studies have reported the BMP of dried banana stem to range from 195 to 256 mL g−1 VS [35–38]; these yields are much lower than the value obtained in this study. This disparity can be attributed to the fresh or wet nature of the banana stem used in the present study. It is probable that high moisture aided the biodegradability or putrescibility through providing an initial richer medium for enzymatic attack and hence methanogenesis . Water is consumed during hydrolysis of macromolecules, and it has been reported that below a certain moisture content (<25 %), no biodegradation is known to take place . Pommier et al. also reported a linear correlation between methane production and moisture content. On the other hand, drying may lead to the floatation of biomass and constriction, shrinkage, and loss of porosity in the cells making it inaccessible to enzymatic attack through decreased surface area to volume ratio. As mentioned earlier, the sap or liquid fraction of the banana stem may be rich in soluble, easily convertible organics to methane, which are otherwise lost during drying. Bound water (water contained in substrate or moisture) is therefore essential for an effective and efficient AD process. Increase moisture therefore favors bacterial/methanogen-waste colonization. Increased moisture containment also leads to an increase in water activity which has been reported to positively correlate with bacterial/archaea growth and hence methane production . Water content may therefore positively impact methane production through increased microbial growth rate and bioavailability of solid banana waste . It must be mentioned that the use of wet banana stem in lieu of dry sample may present some logistic and conservation problems. Nonetheless, the fresh banana stem can be preserved via ensiling or co-ensiling with other fractions of the banana plant waste such as leaves and peels.
A full-scale, continuous stirred tank biogas plant can therefore be operated with the pseudo-banana stem as the sole substrate or co-digested with manure. Considering the 4.8 × 106 tons of wet banana stem produced in Hainan province and chopped to a particle size of 20 mm having a VS of 3.78 % w/w and a BMP of 347 m3 ton−1 VS, the yearly methane production could sum up to 6.29 × 107 m3 CH4. This corresponds to a calorific or lower heating value of 2.26 × 1011 kJ year−1 (1 m3 = 35,900 kJ) or 0.63 GWh year−1 (1 m3 = 9.97 kWh) . Paying cognizance of a conversion efficiency of 43 %, the yearly energy recovery from banana stem could amount to 0.27 GWh year−1. This can account for 1.46 % of the yearly power consumption in Hainan province. Thus, it is plausible to state that the banana stem contains a huge amount of energy that can be harnessed through AD.
This present study demonstrated that wet banana stems can be used as substrates in both mono- and co-digestion processes with cow manure. The methane production of the fresh banana stem as a mono-substrate could reach 347 mL g−1 VS, which is higher than the reported values from other lignocellulosic biomasses and especially dried banana stems. Mechanical cutting to a desirable size was deemed the most economically viable option due to a possibly less energy requirement and high achievable methane yield. The results of enzyme addition and the co-digestion with cow manure showed a limited improvement of methane production for the banana stem, while the hydrolysis rates were improved. In addition, in all the tests, 90 % of the total methane was produced within 2 weeks of incubation. Fresh banana stems can, therefore, become a cheap lignocellulosic substrate for methane production especially through co-ensiling with other morphological fractions for better storage or preservation.
The authors would like to thank the lab work support of Ms. Jinhua Chen. The authors wish to express their gratitude to the Agricultural Departments of the Hainan Provincial Government. The Open Fund of Key Laboratory of Development and Application of Rural Renewable Energy (2015014), Ministry of Agriculture in China, is gratefully acknowledged for the financial support.
CL conceived the study, initiated the collaboration with the partner, and handled both the collection of the data and the drafting of the manuscript. IAN and MN participated in the design of the study and took the lead in the collection and analysis of the literature material and the REEP House data; GL led the drafting of the manuscript. LD and JL contributed to the development of the literature review and the drafting of the manuscript. All authors read and approved the final manuscript.
The authors declare that they have no competing interests.
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- Padam BS, Tin HS, Chye FY, Abdullah MI (2014) Banana by-products: an under-utilized renewable food biomass with great potential. J Food Sci Technol 51(12):3527–3545View ArticleGoogle Scholar
- Yamaguchi J, Araki S (2004) Biomass production of banana plants in the indigenous farming system of the East African Highland: a case study on the Kamachumu Plateau in northwest Tanzania. Agric Ecosyst Environ 102(1):93–111View ArticleGoogle Scholar
- Mohapatra D, Mishra S, Sutar N (2010) Banana and its by-product utilization: an overview. J Sci Ind Res 69(5):323–329Google Scholar
- Neves LC M d, Converti A, Vessoni Penna TC (2009) Biogas production: new trends for alternative energy sources in rural and urban zones. Chem Eng Technol 32(8):1147–1153View ArticleGoogle Scholar
- Scholz M, Alders M, Lohaus T, Wessling M (2015) Structural optimization of membrane-based biogas upgrading processes. J Membr Sci 474:1–10View ArticleGoogle Scholar
- Zhang C, Li J, Liu C, Liu X, Wang J, Li S, Fan G, Zhang L (2013) Alkaline pretreatment for enhancement of biogas production from banana stem and swine manure by anaerobic codigestion. Bioresour Technol 149:353–358View ArticleGoogle Scholar
- Taherzadeh MJ, Karimi K (2008) Pretreatment of lignocellulosic wastes to improve ethanol and biogas production: a review. Int J Mol Sci 9(9):1621–1651View ArticleGoogle Scholar
- Parawira W (2012) Enzyme research and applications in biotechnological intensification of biogas production. Crit Rev Biotechnol 32(2):172–186View ArticleGoogle Scholar
- Herbel Z, Rákhely G, Bagi Z, Ivanova G, Ács N, Kovács E, Kovács KL (2010) Exploitation of the extremely thermophilic Caldicellulosiruptor saccharolyticus in hydrogen and biogas production from biomasses. Environ Technol 31(8-9):1017–1024View ArticleGoogle Scholar
- Wang H, Tao Y, Temudo M, Schooneveld M, Bijl H, Ren N, Wolf M, Heine C, Foerster A, Pelenc V (2015) An integrated approach for efficient biomethane production from solid bio-wastes in a compact system. Biotechnol for biofuels 8(1):1View ArticleGoogle Scholar
- Gianfreda L, Rao MA (2004) Potential of extra cellular enzymes in remediation of polluted soils: a review. Enzym Microb Technol 35(4):339–354View ArticleGoogle Scholar
- Pei P, Zhang C, Li J, Chang S, Li S, Wang J, Zhao M, Li J, Yu M, Chen X (2014) Optimization of NaOH pretreatment for enhancement of biogas production of banana pseudo-stem fiber using response surface methodology. Bio Resources 9(3):5073–5087Google Scholar
- Scano EA, Asquer C, Pistis A, Ortu L, Demontis V, Cocco D (2014) Biogas from anaerobic digestion of fruit and vegetable wastes: experimental results on pilot-scale and preliminary performance evaluation of a full-scale power plant. Energy Convers Manag 77:22–30View ArticleGoogle Scholar
- Nges IA, Escobar F, Fu X, Björnsson L (2012) Benefits of supplementing an industrial waste anaerobic digester with energy crops for increased biogas production. Waste Manage 32(1):53–59View ArticleGoogle Scholar
- Tock JY, Lai CL, Lee KT, Tan KT, Bhatia S (2010) Banana biomass as potential renewable energy resource: a Malaysian case study. Renew Sust Energ Rev 14(2):798–805View ArticleGoogle Scholar
- Kamdem I, Hiligsmann S, Vanderghem C, Bilik I, Paquot M, Thonart P (2013) Comparative biochemical analysis during the anaerobic digestion of lignocellulosic biomass from six morphological parts of Williams Cavendish banana (Triploid Musa AAA group) plants. World J Microbiol Biotechnol 29(12):2259–2270View ArticleGoogle Scholar
- Raposo F, De la Rubia M, Fernández-Cegrí V, Borja R (2012) Anaerobic digestion of solid organic substrates in batch mode: an overview relating to methane yields and experimental procedures. Renew Sust Energ Rev 16(1):861–877View ArticleGoogle Scholar
- Badshah M, Lam DM, Liu J, Mattiasson B (2012) Use of an automatic methane potential test system for evaluating the biomethane potential of sugarcane bagasse after different treatments. Bioresour Technol 114:262–269View ArticleGoogle Scholar
- APHA (2005) Total, fixed, and volatile solids in solid and semisolid samples. In: Eaton AD, Clesceri LS, Rice EW, Greenberg AE, Franson MA (eds) Standard methods for the examination of water and wastewater, 21st edn. American Public Health Association/American Water Works Association/Water Environment Federation, BaltimoreGoogle Scholar
- Van Soest PV, Robertson J, Lewis B (1991) Methods for dietary fiber, neutral detergent fiber, and nonstarch polysaccharides in relation to animal nutrition. J Dairy Sci 74(10):3583–3597View ArticleGoogle Scholar
- Angelidaki I, Alves M, Bolzonella D, Borzacconi L, Campos J, Guwy A, Kalyuzhnyi S, Jenicek P, Van Lier J (2009) Defining the biomethane potential (BMP) of solid organic wastes and energy crops: a proposed protocol for batch assays. Water Sci Technol 59(5):927–934View ArticleGoogle Scholar
- Kreuger E, Sipos B, Zacchi G, Svensson S-E, Björnsson L (2011) Bioconversion of industrial hemp to ethanol and methane: the benefits of steam pretreatment and co-production. Bioresour Technol 102(3):3457–3465View ArticleGoogle Scholar
- Raposo F, Fernández‐Cegrí V, De la Rubia M, Borja R, Béline F, Cavinato C, Demirer G, Fernández B, Fernández‐Polanco M, Frigon J (2011) Biochemical methane potential (BMP) of solid organic substrates: evaluation of anaerobic biodegradability using data from an international interlaboratory study. J Chem Technol Biotechnol 86(8):1088–1098View ArticleGoogle Scholar
- Oliveira L, Cordeiro N, Evtuguin D, Torres I, Silvestre A (2007) Chemical composition of different morphological parts from ‘Dwarf Cavendish’ banana plant and their potential as a non-wood renewable source of natural products. Ind Crop Prod 26(2):163–172View ArticleGoogle Scholar
- Angelidaki I, Ellegaard L (2003) Codigestion of manure and organic wastes in centralized biogas plants. Appl Biochem Biotechnol 109(1-3):95–105View ArticleGoogle Scholar
- Shen S, Nges IA, Yun J, Liu J (2014) Pre-treatments for enhanced biochemical methane potential of bamboo waste. Chem Eng J 240:253–259View ArticleGoogle Scholar
- Li M-F, Fan Y-M, Xu F, Sun R-C, Zhang X-L (2010) Cold sodium hydroxide/urea based pretreatment of bamboo for bioethanol production: characterization of the cellulose rich fraction. Ind Crop Prod 32(3):551–559View ArticleGoogle Scholar
- Cordeiro N, Belgacem M, Torres I, Moura J (2004) Chemical composition and pulping of banana pseudo-stems. Ind Crop Prod 19(2):147–154View ArticleGoogle Scholar
- Izumi K, Okishio Y-k, Nagao N, Niwa C, Yamamoto S, Toda T (2010) Effects of particle size on anaerobic digestion of food waste. Int Biodeter Biodegr 64(7):601–608View ArticleGoogle Scholar
- Tumutegyereize P, Muranga F, Kawongolo J, Nabugoomu F (2013) Optimization of biogas production from banana peels: effect of particle size on methane yield. Afr J Biotechnol 10(79):18243–18251Google Scholar
- Romano RT, Zhang R, Teter S, McGarvey JA (2009) The effect of enzyme addition on anaerobic digestion of JoseTall Wheat Grass. Bioresour Technol 100(20):4564–4571View ArticleGoogle Scholar
- Yang B, Dai Z, Ding S-Y, Wyman CE (2011) Enzymatic hydrolysis of cellulosic biomass. Biofuels 2(4):421–449View ArticleGoogle Scholar
- El-Mashad HM, Zhang R (2010) Biogas production from co-digestion of dairy manure and food waste. Bioresour Technol 101(11):4021–4028View ArticleGoogle Scholar
- Lehtomäki A, Huttunen S, Rintala J (2007) Laboratory investigations on co-digestion of energy crops and crop residues with cow manure for methane production: effect of crop to manure ratio. Resour Conserv Recycl 51(3):591–609View ArticleGoogle Scholar
- Kalia V, Sonakya V, Raizada N (2000) Anaerobic digestion of banana stem waste. Bioresour Technol 73(2):191–193View ArticleGoogle Scholar
- Cheng S, Li Z, Xu C, Yang L (2009) Experimental study on biochemical methane potential of banana tree wasteGoogle Scholar
- Khan MT, Maurer C, Argyropoulos D, Brule M, Mueller J (2009) Anaerobic digestion of banana waste, a potential source of energy in Uganda. In: Proceedings Tropentag (2009): International Research and Food SecurityGoogle Scholar
- Zainol N (2012) Kinetics of biogas production from banana stem waste. InTech, Biogas Europe, p 408Google Scholar
- Hernández-Berriel MC, Márquez-Benavides L, González-Pérez D, Buenrostro-Delgado O (2008) The effect of moisture regimes on the anaerobic degradation of municipal solid waste from Metepec (Mexico). Waste Manage 28:S14–S20View ArticleGoogle Scholar
- Pommier S, Chenu D, Quintard M, Lefebvre X (2007) A logistic model for the prediction of the influence of water on the solid waste methanization in landfills. Biotechnol Bioeng 97(3):473–482View ArticleGoogle Scholar
- Bourgeois C, Mescle J, Zucca J (1996) Microbiologie alimentaire. Lavoisier, Tome 1 Paris, p 672Google Scholar
- Pommier S, Chenu D, Quintard M, Lefebvre X (2007) A logistic model for the prediction of the influence of water on the solid waste methanization in landfills. Biotechnol Bioeng 97:473–482View ArticleGoogle Scholar