Bio-ethanol production through simultaneous saccharification and co-fermentation (SSCF) of a low-moisture anhydrous ammonia (LMAA)-pretreated napiegrass (Pennisetum purpureum Schumach)
© Yasuda et al.; licensee Springer. 2014
Received: 18 May 2014
Accepted: 23 June 2014
Published: 1 July 2014
Efficient bio-ethanol production from napiegrass (Pennisetum purpureum Schumach) was investigated. A low-moisture anhydrous ammonia (LMAA)-pretreated napiegrass was subjected to simultaneous saccharification and co-fermentation (SSCF), which was performed at 36°C using Escherichia coli KO11, Saccharomyces cerevisiae, cellulase, and xylanase. It was found that use of xylanase as well as the LMAA-pretreatment was effective for the SSCF. After the SSCF for 96 h, the ethanol yield reached 74% of the theoretical yield based on the glucan (397 mg g-1) and xylan (214 mg g-1) occurring in dry powdered LMAA-pretreated napiergrass.
Bioethanol from lignocellulosic biomass has been recognized as one of promising sustainable energy source alternative to petroleum-based fuels, since the lignocelluloses are not directly in competition with food sources (Galbe and Zacchi 2007; Taherzadeh and Karimi 2007). We are interested in ethanol production from herbaceous lignocellulosic napiergrass (Pennisetum purpureum Schumach) because of its low lignin content and high harvest amount per year and per area (Yasuda et al. 2012, 2013). In lignocellulosic ethanol production, pentose fermentation is an unavoidable process because of its high xylan content. In pentose fermentation process, however, ethanol concentration is usually too low (<10 g L-1) to distillate with low energy cost. Therefore, pentose fermentation has been performed as co-fermentation of hexose and pentose using a variety of recombinant strains such as Escherichia coli KO11 (Ohta et al. 1990, 1991; Underwood et al. 2002; Brandon et al. 2011), Saccharomyces cerevisiae 424A(LNH-ST) (Jin et al. 2012a, [b]), S. cerevisiae TMB3400 (Ohgren et al. 2006; Matsushika et al. 2009), and Zymomonas mobilis AX101 (Su et al. 2012). Simultaneous saccharification and co-fermentation (SSCF) is generally superior to the separate saccharification and co-fermentation since SSCF can achieve saccharification, hexose fermentation, and pentose fermentation in one-pot reaction. Here, we applied SSCF to ethanol production from napiergrass, which was treated by low-moisture anhydrous ammonia (LMAA) pretreatment.
Materials and methods
Napiergrass as lignocellulosic materials
As raw material, a dwarf type of napiergrass was cultivated in the Kibana Agricultural Science Station, at the University of Miyazaki. Leaf blades of the napiergrass were separated from the stem and then cut by a cutter and dried at 70°C for 72 h. The dried matter was ground until 70% of the particles were in a range of 32–150 μm in length.
Chemical components of napiergrass
The powdered napiergrass (30 g) was treated with a 1% aqueous solution of NaOH (400 mL) at 95°C for 1 h. The holocellulose was isolated as a pale yellow precipitate by centrifugation and filtration of the treated mixture. The supernatant solution was neutralized to pH 5.0 by a dilute HCl solution. The resulting dark brown precipitate identified as lignin was collected via centrifugation at 10,000 rpm for 10 min. Sugars in holocellolose were determined according to the methods published by the National Renewable Energy Laboratory as follows (Sluiter et al. 2010). Sulfuric acid (72 wt%, 3.0 mL) was added slowly to holocelulose (300 mg) and kept at 30°C for 1 h. The resulting solution was diluted by water (84 mL) until the concentration of sulfuric acid was 4 wt%. Acid hydrolysis was performed by autoclaving at 121°C for 1 h in an autoclave. After the neutralization by CaCO3, the solution was subjected to the centrifugation to give the supernatant solution (ca. 87 mL), which was concentrated to 30 mL by evaporation. The solution was analyzed by HPLC. The peaks of glucose and xylose appeared whereas the peaks of galactose and arabinose were very weak because of their low contents. The amounts of glucan and xylan were determined from the amounts of glucose and xylose determined by HPLC. It was confirmed that the sum amounts of glucan and xylan were equaled to the amounts of hollocellolose. The ash component in lignocellulose was obtained by the burning of the lignocellulose (2.0 g) in an electric furnace (KBF784N1, Koyo, Nara, Japan) for 2 h at 850°C.
Low-moisture anhydrous ammonia (LMAA) pretreatment
Water (100 g) was added dropwise to dry powdered napiergrass (100 g, volume 320 mL) in the flask (1 L). The resulting moist powdered napiergrass in the flask was evacuated with a pump under 20 mm Hg and then gaseous NH3 was introduced into the flask. This operation was performed three times until the atmosphere inside the flask was entirely replaced with NH3. The amount of NH3 presented in the flask was 1.1 g. The LMAA pretreatment was performed by modifying the Kim method where LMAA pretreatment was performed at 80°C for 86 h (Yoo et al. 2011). In our LMAA-pretreatment, the moist powdered napiergrass was kept under NH3 gas atmosphere at room temperature for four weeks (28 days). After the treatment, the NH3 was removed with an evaporator. The treated napiergrass was washed with water (2 L) three times to separate the brownish aqueous solution of the lignin. After pH was checked to be neutral, the pretreated napiergrass was dried at 60°C to weigh out the precise amount of napiergrass in the following biological treatment.
Hydrolytic enzyme for saccharification
A cellulase from Acremonium cellulolyticus (Acremozyme KM, Kyowa Kasei, Osaka, Japan) was selected by comparing its activity with other cellulases such as Meycellase (Meiji Seika), a cellulase from Trichoderma viride (Wako Chemicals, Osaka, Japan) and a cellulase from Aspergillus niger (Fluka Japan, Tokyo) (Yasuda et al. 2011). The cellulase activity of Acremozyme KM was determined to be 1,320 units mg–1 by the method of breaking down filter paper (Kitamikado and Toyama 1962). A xylanases from Trichoderma longibrachiatum (reesei) (Sumizyme X, Shin Nihon Chemicals, Anjyo, Japan, 5,000 u g-1) was selected from commercially available hemicellulase.
Saccharification was performed for the powdered napiergrass (10.0 g) using both cellulase and xylanase, whose total amount was 1.0 g, at 45°C in an acetate buffer (60 mL, pH 5.0).
Preparation of the inoculum culture of Escherichia coli KO11 and Saccharomyces cerevisiae
E. coli KO11 was grown in the LB medium (200 mL) consisting of tryptone (2.0 g L–1, Difco), yeast extract (1.0 g L–1), and NaCl (2.0 g L–1) under shaking at 150 rpm at 37°C for 24 h. The KO11 cell suspension contained a dry weight of 0.52 mg mL–1 of E. coli KO11. Saccharomyces cerevisiae NBRC 2044 was grown at 30°C for 24 h in a basal medium (initial pH 5.5) consisting of glucose (20.0 g L–1), polypeptone (1.0 g L–1), yeast extract (1.0 g L–1), KH2PO4 (1.0 g L–1), and MgSO4 (3.0 g L–1). After incubating for 24 h, the cell suspension of S. cerevisiae, whose grown culture of S. cerevisiae showed a cell density of 7.7 × 107 cells mL–1, was obtained (Yasuda et al. 2012).
Simultaneous saccharification and co-fermentation (SSCF)
Typical procedure of SSCF is as follows. The LMAA-pretreated napiergrass (3.0 g) was suspended in the acetate buffer (14.0 mL, pH 5.0) and then autoclaved at 121°C for 20 min. After cooling to room temperature under UV-irradiation, the cell suspension (0.36 mL) of S. cerevisiae, a portion (21 mL) of the inoculum culture E. coli KO11, and the cellulase (150 mg) and xylanase (150 mg) in an acetate buffer solution (5.0 mL, pH 5.0) were added to the suspension of the napiergrass. After pH was adjusted to 6.0, air was purged with N2. In the SSCF without S. cerevisiae, replacement by N2 gas was not performed. The SSCF was initiated by stirring the solution vigorously with a magnetic stirrer at 36°C which was an optimal fermentation temperature of E. coli KO11. The evolved CO2 was collected over water by a measuring cylinder, and the reaction was monitored by the volume of CO2. The SSCF reaction was continued for 96 h until CO2 evolution ceased.
Saccharides were analyzed on a high-performance liquid chromatography system (LC-20AD, Shimadzu, Kyoto, Japan) equipped with RI detector (RID-10A) using an anion exchange column (NH2P-50 4E; Shodex Asahipak, 250 mm in length and 4.6 mm in ID, Yokohama, Japan). Acetonitrile-water (8:2 v/v) was flowed at 1.0 mL min-1 as mobile phase. Ethanol was analyzed by gas-liquid chromatography using 2-propanol as an internal standard on a Shimadzu gas chromatograph GC-8A equipped with a glass column of 5% Thermon 1000 on Sunpak-A (Shimadzu).
Results and discussion
Ethanol production from lignocelluloses
In general, the cellulosic bio-ethanol production involves three steps such as saccharification of cellulosic components (SA), hexose fermentation (HF), and pentose fermentation (PF). These processes are combined each other to simplify the procedure and enhance the ethanol yield. Typical combinations are as follows: SSF is simultaneous process of SA and HF but does not take place PF. CF is co-fermentation of hexose and pentose. SSCF is simultaneous process of SA, HF, and PF. For efficient cellulosic bio-ethanol production, moreover, pretreatment to remove the lignin and/or promote an enzymatic digestibility of the cellulosic components are usually required.
Napiergrass as raw material
Napiergrass belongs to herbaceous tropical species, native to the east Africa and has high dry matter productivity with moderate forage quality in southern Kyushu (Ishii et al. 2005a, 2013). Napiergrass has wide variation of phenotypes, reflected by plant breeding due to the crossing of dwarf genotype and relative species such as pearl millet (Pennisetum americanum) (Ishii et al. 2005a; Hanna and Sollenburger 2007). A dwarf variety of late-heading type of napiergrass (dwarf napiergrass) originated from Florida, USA, via Thailand (Mukhtar et al. 2003) was assessed to be suitable for both grazing (Ishii et al. 2005b) and cut-and-carry systems among several sites of southern Kyushu, Japan (Utamy et al. 2011). Dwarf napiergrass meets the requirement of lignocellulose for the biofuel production because it has low lignin-content and a relatively high herbage mass per year and per area (Rengsirikul et al. 2011; Rengsirikul et al. 2013; Khairani et al. 2013). Therefore, we have continued to use this dwarf type of napiergrass for the bio-ethanol (Yasuda et al. 2011) and bio-hydrogen production (Shiragami et al. 2012).
As has been reported previously (Yasuda et al. 2013), the LMAA-pretreatment was useful for the simultaneous saccharification and fermentation (SSF) of napiergrass. In the present case, therefore, the powdered napiergrass was subjected to the LMAA-pretreatment. The LMAA-pretreated napiergrass contained 39.7 wt% of glucan, 21.4 wt% of xylan, 7.1 wt% of lignin, and 7.1 wt% of ash, while the components of the non-treated napiergrass were determined to be 31.3 (glucan), 16.9 (xylan), 12.6 (lignin), and 13.9 wt% (ash).
Optimization of enzymatic saccharification
Saccharification of LMAA-pretreated napiergrass a)
F X c)
SSCF of the LMAA-pretreated napiergrass
SSCF of LMAA-treated napiergrass a)
209 ± 14 (35)
19 ± 2 (2)
353 ± 31 (43)
73 ± 25 (10)
47 ± 10 (4)
777 ± 15 (74)
148 ± 11 (20)
43 ± 2 (3)
731 ± 12 (70)
473 ± 43 (65)
29 ± 10 (2)
576 ± 39 (55)
304 ± 15 (50)
37 ± 6 (3)
547 ± 41 (63)
385 ± 45 (53)
37 ± 2 (3)
719 ± 13 (59)
438 ± 37 (60)
39 ± 8 (3)
829 ± 28 (60)
The additive effect of Saccharomyces cerevisiae
S. cerevisiae is the most commonly used microorganism for industrial ethanol production. However, it cannot utilize xylose for growth and ethanol production. Therefore, it is requisite to use a recombinant species which can ferment pentose. In our SSCF process, S. cerevisiae was used in addition to a recombinant E. coli KO11 for fermentation, since it was found that the SSCF using four components (S. cerevisiae, E. coli KO11, cellulase, and xylanase) proceeded slightly faster than the SSCF without S. cerevisiae.
We sincerely thank Lonnie O. Ingram from the University of Florida for providing the E. coli KO11 strain. This study was done as a part of the project entitled “Research and Development of Catalytic Process for Efficient Conversion of Cellulosic Biomass into Biofuels and Chemicals (2009–2013)” through Special Funds for Education and Research from the Ministry of Education, Culture, Sports, Science, and Technology of Japan.
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