Chemical characterization and hydrothermal pretreatment of Salicornia bigelovii straw for enhanced enzymatic hydrolysis and bioethanol potential
Introduction
Current energy needs and increasing crude oil prices are the driving force for exploring new energy resources. Lignocellulosic biomass is considered very attractive as a feedstock for generation of bioproducts (including bioethanol), due to its complex structure and natural abundance (Alvira et al., 2010). Traditional lignocellulosic feedstocks include mainly energy crops (e.g. prairie grasses) and agricultural residues (e.g. corn stover, wheat straw, sugar cane bagasse). However, even though being abundant and easily accessible in many regions of the world, these materials are not available in challenging climatic conditions, such as arid, salty soils of Middle East or Africa. An ongoing search for more attractive biofuel feedstocks for all climate regions has led researchers to examine new materials, such as halophytes. Halophytes are remarkable plant species that can survive high salinity environments (10–100 ppt); conditions which are not conducive to growth for 99% of other plants (Flowers and Colmer, 2008). Salicornia bigolovii is a halophyte that has attracted attention due to its oil seeds and it is a potential feedstock for biodiesel or bio-SPK (Synthetic Paraffinic Kerosene) production (Warshay et al., 2010). Lignocellulosic part of the plant (stems and seed spikes) is expected to have a similar composition to other halophytic shrubs (10–30% cellulose, 10–30% hemicellulose and 2–10% lignin) (Kraidees et al., 1998). This makes the biomass leftover after the seed separation a potentially attractive lignocellulosic feedstock for production of ethanol, biogas and other value-added by-products. S. bigelovii is a native plant for North America and the Caribbean (Zerai et al., 2010). The plant is currently grown in the Middle East for fodder for lamb, sheep and goats, which have the ability to tolerate high-sodium diet (Kraidees et al., 1998).
As 98% of water reserves are saline, and current fertile soils are getting salinized due to rising sea level, plants that can tolerate these conditions can become an attractive new feedstock for biofuel production, not competing with food crops for the fertile soil (Rozema and Flowers, 2008).
Lignocellulosic materials require physical–chemical pretreatment prior to biological processing to decrease the recalcitrance of the biomass by breaking the lignin–carbohydrate bonds and decreasing the crystalinity of cellulose (Alvira et al., 2010, Galbe and Zacchi, 2007). Hydrothermal pretreatment has been found to be an effective and cost efficient method for a wide range of lignocellulosic materials including poplar, olive tree residues, corn stover, wheat straw, prairie cordgrass and many more, producing highly digestible fiber fractions (60–100% glucan-to-glucose convertibility) (Cybulska et al., 2009, Petersen et al., 2009, Thomsen et al., 2008).
This method utilizes high-temperature water (having lower pH) to initiate hydrolysis of the acetyl bonds in the lignocellulosic structure, thus removing hemicellulosic oligomers to the solution. Hydrolysis of the acetyl bonds drops the pH further, inducing more acetyl bond cleavage, thus the alternate name of the process is autohydrolysis (Wyman et al., 2005). The effect of elevated temperature can be partially replaced with a catalyst (e.g. a mineral acid), which allows for the processing temperature and time to be lower. The most commonly used catalysts include sulfuric acid, sulfur dioxide or carbon dioxide (Luterbacher et al., 2010, Taherzadeh and Karimi, 2008). Alkaline catalysts have also been widely used (Thomsen et al., 2006). In general, temperature has been found to have major effect on the pretreatment effectiveness towards producing highly digestible fibers. Residence time has a much lower influence on the pretreatment efficiency, and is often found as non-significant factor in statistical modeling (Yu et al., 2010). These observations have been summarized in the severity theory, which generated an experimental severity factor that shows a greater significance of temperature for the pretreatment efficiency (Galbe and Zacchi, 2007, Hendriks and Zeeman, 2009). The optimal severity factor suggested by Aita and Kim (2010) should be between 3.0 and 4.5 for maximum digestibility of the produced fibers. This corresponds to 160–210 °C at processing times between 10 and 30 min (Yu et al., 2010). As the severity of the process increases, sugar degradation reactions become favorable (>170 °C for pentoses and >210–220 °C for hexoses) (Garrote et al., 1999, Zhang et al., 2011) and undesirable by-products are formed. These by-products (including mainly acetic acid, furfural and 5-hydroxymethyl furfural) are known for their inhibitory effect on the microorganisms even in very low concentrations (<1 g/L), which can result in low ethanol yields (Klinke et al., 2004, Thomsen et al., 2009). Furthermore, high pretreatment severity results in alteration of the lignin structure via melting, coagulation, and repolymerization on the cellulose fibers. Sugars released during the autohydrolysis are incorporated in the lignin structure in the process of condensation, leading to losses of carbohydrates and an increase in the acid insoluble residue measurements, giving artificially high values for lignin recovery (Garrote et al., 1999, Young, 1998).
This research study evaluates lignocellulosic biomass of S. bigelovii, a halophytic oil plant, as a potential lignocellulosic bioethanol feedstock. A hydrothermal process was chosen as a pretreatment method applied prior to enzymatic hydrolysis and fermentation in order to facilitate high efficiency of both. Optimization of the pretreatment temperature was performed as a screening test for future choice of the range of pretreatment conditions.
Section snippets
Raw material
S. bigelovii seeds were provided to Masdar Institute by International Center for Biosaline Agriculture (ICBA), Dubai as a part of the Masdar Institute Integrated Seawater Energy Agricultural System (ISEAS) project (ICBA, 2011). The plant was cultivated using 40 ppt NaCl water salinity and 1.0–2.0 gN/m2 fertilization. Seeds were separated from the plant after harvesting and the resulting biomass (stems, seedless inflorescences, and branches) was dried and used in this study. The seedless and dried
Raw feedstock characterization
Characterization of the seedless S. bigelovii revealed extremely high ash content (43.08 g/100 gDM). Other than that, the material shows typical lignocellulosic crop characteristics, containing cellulose, lignin and hemicellulose as dominant components. Results of the compositional analysis are as follows: 9.1 ± 1.5 g/100 gDM glucan, 7.7 ± 0.4 g/100 gDM xylan, 5.5 ± 2.1 g/100 gDM arabinan, 6.8 ± 1.4 g/100 gDM Klason lignin, 6.8 ± 0.1 g/100 gDM structural ash, and 53.7 ± 3.6 g/100 gDM total extractives (including
Conclusions
Seedless S. bigelovii examined as a bioethanol feedstock follows a typical trend for a lignocellulosic biomass. However, fresh water wash is required prior to any processing to remove the salt deposits. No significant difference was found among the enzymatic digestibility and fiber fermentability (both found to be high) in the severity range tested, suggesting that lower severities could be examined in the future, also since the content of lignin was found low in the feedstock. High
Acknowledgements
This work was supported by the Sustainable BioEnergy Research Consortium (SBRC), Masdar Institute of Science and Technology (Abu Dhabi, UAE). Ingelis Larsen and Tomas Fernqvist are acknowledged for their technical assistance.
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