Ethanol production from a biomass mixture of furfural residues with green liquor-peroxide saccarified cassava liquid
© The Author(s). 2016
Received: 9 January 2016
Accepted: 23 May 2016
Published: 1 June 2016
As the most abundant renewable resources, lignocellulosic materials are ideal candidates as alternative feedstock for bioethanol production. Cassava residues (CR) are byproducts of the cassava starch industry which can be mixed with lignocellulosic materials for ethanol production. The presence of lignin in lignocellulosic substrates can inhibit saccharification by reducing the cellulase activity. Simultaneous saccharification and fermentation (SSF) of furfural residues (FR) pretreated with green liquor and hydrogen peroxide (GL-H2O2) with CR saccharification liquid was investigated. The final ethanol concentration, yield, initial rate, number of live yeast cells, and the dead yeast ratio were compared to evaluate the effectiveness of combining delignificated lignocellulosic substrates and starchy substrates for ethanol production.
Our results indicate that 42.0 % of FR lignin removal was achieved on FR using of 0.06 g H2O2/g-substrate and 9 mL GL/g-substrate at 80 °C. The highest overall ethanol yield was 93.6 % of the theoretical. When the ratio of 0.06 g/g-H2O2-GL-pretreated FR to CR was 5:1, the ethanol concentration was the same with that ratio of untreated FR to CR of 1:1. Using 0.06 g/g-H2O2-GL-pretreated FR with CR at a ratio of 2:1 resulted in 51.9 g/L ethanol concentration. Moreover, FR pretreated with GL-H2O2 decreased the concentration of byproducts in SSF compared with that obtained in the previous study.
The lignin in FR would inhibit enzyme activity and GL-H2O2 is an advantageous pretreatment method to treat FR and high intensity of FR pretreatment increased the final ethanol concentration. The efficiency of ethanol fermentation of was improved when delignification increased. GL-H2O2 is an advantageous pretreatment method to treat FR. As the pretreatment dosage of GL-H2O2 on FR increased, the proportion of lignocellulosic substrates was enhanced in the SSF of the substrate mixture of CR and FR as compared with untreated FR. Moreover, the final ethanol concentration was increased with a high ethanol yield and lower byproduct concentrations.
There is currently an upsurge of interest in the search for renewable biomass to produce liquid transportation fuels such as bioethanol. This interest has been resulted from environmental concerns about toxic-gas emissions from burning petroleum fuels as well as a decrease in the available petroleum resources and fossil fuels. Increased attention has been paid on bioethanol as a promising alternative energy source . Bioethanol is the most important biofuel today, which accounts for more than 90 % of total biofuel use .
Increasing attention is paid on ethanol production from lignocellulosic materials, especially low-cost waste materials , due to the abundance of lignocellulosic materials among the renewable resources. FR is an industrial byproduct from corncobs-based furfural production . Furfural production process involves treating corncobs under heated and acidic conditions (hemicelluloses) . The resultant FR is composed mainly of cellulose and lignin . Cellulose and lignin in the cobs are relatively stable under furfural production conditions. Therefore, FR could be a great candidate material for ethanol production after pretreatment. Utilization of FR to produce ethanol would be effective in the dispose of waste products, while reducing environmental pollution.
It has been previously reported that the presence of lignin in biomass substrates might inhibit enzymatic hydrolysis , as the interaction between the lignin and the enzyme would reduce the activity of cellulase. The conversion of fermentable sugars is a crucial process for bioethanol production [8, 9]. Therefore, biomass delignification is an efficient approach for ethanol production to increase the available surface area of cellulose, dissolve the lignin, and break the bonds between lignin and carbohydrate polymers, and finally dissolve the lignin. As for FR, alkaline hydrogen peroxide pretreatment could effectively degrade the acidic lignin .
Green liquor (GL), which is an alkaline mixture of sodium carbonate and sodium hydroxide, can be used in alkaline pretreatment, and it has recently been developed for biomass applications . This method could selectively remove lignin and recover cellulose efficiently . The previous study showed that there was 56.7 % lignin removal ratio using alkaline hydrogen peroxide pretreatment . In the present study, GL and hydrogen peroxide (GL-H2O2) were combined as a pretreatment for FR delignification with the addition of ethylenediaminetetraacetic acid (EDTA), which is a heavy metal ion chelate effective in reducing H2O2 degradation .
Cassava residues (CR) are dry solid fibrous byproducts of the starch industry , with an annual production of approximately 30 thousand tons in China . CR is composed of starch (45–60 %), cellulose (15–25 %), and hemicellulose (<5 %) . Due to the low cellulose content and high starch content, CR might be considered as a cellulosic starch byproduct  that could be easily processed using starch ethanol techniques into several valuable products. In addition, CR contains a certain amount of protein, which could provide the necessary nutrients for yeast fermentation. However, low ethanol yields have been reported with CR due to the poor accessibility of the CR slurry to cellulolytic enzymes . It is more advantageous to combine CR with lignocellulosic material for use in ethanol production .
With a high ethanol concentration in the fermentation broth, the energy consumption of distillation could be reduced. A higher sugar concentration can be achieved by using a higher substrate concentration during the process of lignocellulose enzymatic hydrolisis. However, this can also lead to a higher concentration of inhibitors and when the whole slurry is used it may lead to a decreased yield as a result of inhibition such as by glycerol and due to poor mass transfer . Recently, methods have been developed for efficient hydrolysis and fermentation of mixed fermentative microorganisms [19, 20]. Erdei et al.  developed a simultaneous saccharification and fermentation (SSF) process for wheat straw and wheat meal and illustrated that SSF of these mixed substrates could enhance ethanol production. Using substrate mixtures is promising to increase final ethanol concentrations and to replace starch with lignocelluloses. One possibility to produce a high final yield in SSF of mixtures is the dilution of inhibitors. Brandberg et al.  showed that starch hydrolysates are potential supplements for ethanol production from lignocellulosic hydrolysates. In the present work, the SSF of FR, which was subjected to GL-H2O2 pretreatment (GL-H2O2-FR), and CR, were carried out. The final ethanol concentration, yield, concentrations of byproducts, number of live yeast cells, and the dead yeast ratio were compared.
Results and discussion
Effects of H2O2 concentration on the chemical composition of pretreated FR
Ethanol and glucose concentrations during SSF with various mixture ratios of pretreated FR and CR
As shown in Fig. 2b, more than 25 g/L of ethanol was obtained using a mixture of 0.03 g/g-H2O2-GL-pretreated FR and CR, and the highest ethanol concentration was 35.6 g/L with an ethanol yield of 88.4 % of the theoretical yield when the ratio was 1:1 (Fig. 3b). The lowest ethanol concentration occurred at a mixture ratio of 5:1 with an ethanol concentration of 25.5 g/L and an ethanol yield of 75.4 % of the theoretical yield.
There were similar results for ethanol concentration in SSF when the ratio of 0.06 g/g-H2O2-GL-pretreated FR to CR was 5:1 and the 0.03 g/g-H2O2-GL-pretreated FR to CR ratio was 3:1 (Fig. 2). For untreated FR, the ethanol concentration could reach the similar level under the FR:CR ratio of 1:2, (data not shown). GL-H2O2 pretreatment has a positive impact on FR, as the proportion of FR in SSF of the CR and FR mixture was enhanced after pretreatment with GL-H2O2 compared with untreated FR . Thus, decreasing the content of lignin within FR using GL-H2O2 pretreatment improved the material usage. CR promotes FR by providing important nutrients for fermentative organisms, and in turn when SSF is performed with the substrate of FR as well as CR, it is necessary to add cellulase, and they hydrolyse the cellulosic fraction in CR for additional ethanol. Tang et al.  showed that SSF of FR alone with mineral-salt medium (without yeast extract) exhibited ethanol yield lower than that with organic medium, and also lower than that of mixture substrates with corn kernels. The organic nutrients were crucial for SSF of FR.
The effects of substrate mixture ratios on final ethanol yield (% of the theoretical) and the initial rates of products before 4 h
g/(L · h)
g/(L · h)
g/(L · h)
g/(L · h)
g/(L · h)
0.06 g/g-H2O2-GL-pretreated FR: CR
0.03 g/g-H2O2-GL-pretreated FR: CR
Byproducts in SSF of different mixture ratios of pretreated FR and CR
In sample A (Fig. 4A1), the highest glycerol concentration (8.6 ± 0.16 g/L) was formed at 120 h with a ratio of 0.06 g/g-H2O2-GL-pretreated FR to CR of 5:1, while in sample B it reached 9.3 ± 0.13 g/L with the same ratio (Fig. 4B1). Glycerol acts as an inhibitor of SSF as it consumes at least 4 % of the carbon source for the fermentation . There was a high concentration of glycerol at 24 h, ranging from 1.8 to 4.7 g/L, with an increase of the mixture substrate ratio of 0.06 g/g-H2O2-GL-pretreated FR to CR from 1:1 to 5:1 (Fig. 4A1); however, it ranged from 4.4 to 7.8 g/L for the mixture of 0.03 g/g-H2O2-GL-pretreated FR and CR (Fig. 4B1). A decrease in glycerol concentration occurred at 48 h, which is likely the result of the conversion of glycerol into dihydroxyacetone . When half pretreated FR (either 0.06 g/g or 0.03 g/g-H2O2-GL-pretreated FR) and half CR was used in a mixture, the highest glycerol concentrations were 5.1 to 6.0 g/L, while 8.3 g/L was reached using untreated FR plus CR with the same ratio (data not shown). These results indicate that delignification of the source material used for SSF could produce less glycerol byproducts under the same conditions. In addition, glycerol would be against the osmotic pressure and would reduce the oxidation-reduction potential , which would result in the concentration fluctuation (Fig. 4). Yeast cells lack acetaldehyde as a hydrogen acceptor, which leads to increased NADH as concentration is increased. NAD+ required for xylitol dehydrogenase (XDH), can be regenerated by reducing dihydroxyacetone phosphate to glycerol .
Lactic acid (LA)
The increase in the production of LA would accompany a decrease in the final ethanol concentration . Figure 4 shows that little LA was produced during the first 8 h for both levels of H2O2 pretreated FR. For mixtures containing a ratio of 0.06 g/g-H2O2-GL-pretreated FR to CR of 1:1, LA production occurred after 24 h. The production of LA was delayed in 0.06 g/g-H2O2-GL-pretreated FR compared with 0.03 g/g-H2O2-GL-pretreated FR. This could be due to the high delignification that occurred with 0.06 g/g-H2O2-GL-pretreated FR leading to a lower concentration of LA . The overall trend of the LA concentration was increasing with increasing proportion of pretreated FR. However, the final LA concentration for the mixture ratios of 2:1 and 1:1 were quite similar. The reduced LA concentration was observed when more CR was used in the substrate mixture. Besides that, the absence of LA with increased pretreatment of FR indicates that the degraded lignin in the pretreatment liquid inhibit LA bacteria . Moreover, increased concentrations of CR provide more nutrients, which decrease the production of LA in both cases .
In SSF of mixtures of 0.06 g/g-H2O2-GL-pretreated FR and CR, the acetic acid concentration at 24 h was 1.1 g/L, 1.8 g/L, and 2.7 g/L for mixture have a ratio of 3:1, 4:1, and 5:1, respectively (Fig. 4A3). However, in SSF with mixture having a ratio of 1:1 or 2:1, there was no acetic acid production prior to 24 h. On the other hand, 0.03 g/g-H2O2-GL-pretreated FR mixtures with CR incurred higher concentrations of acetic acid (Fig. 4B3). The addition of CR delayed the production of acetic acid; at 48 h, for mixtures with ratio of 1:1 and 2:1, the acetic acid concentration was 1.3 g/L and 1.8 g/L, respectively. Acetic acid concentrations more than 2 g/L would reduce ethanolic fermentation . The acetic acid concentration of the mixtures of 0.03 g/g-H2O2-GL-pretreated FR and CR was twice that of the mixtures of 0.06 g/g-H2O2-GL-pretreated FR and CR, indicating that FR delignification has a positive effect on lowering acetic acid production. The formation of acetic acid is a kind of metabolism emanation . Hanmilton considered that the inhibition of acetic acid growth was not only the release of proton but also the accumulation of the anion. The inhibition of acetic acid formation was the comprehensive results .
The initial rate of byproduct production in SSF is shown in Table 1. Both the concentration and initial production rate of glycerol and acetic acid were increased with increasing addition of pretreated FR or by reducing the pretreatment intensity (or level of peroxide), resulting in lower ethanol production. An additional benefit of substrate delignification for ethanol production is clearly reflected in the current study. When the pretreated substrate is added to the medium, it reduces the effect of the inhibitors.
Ethanol and glucose concentrations of SSF with different substrate loadings
Another potential explanation for the increase in ethanol production when using CR might be the supplemented nutrient content. It has been shown that wheat hydrolysate can sustain anaerobic cultivation of Saccharomyces cerevisiae . In addition, Tang et al. illustrated that corn hydrolysate can be used for the replacement of the organic medium in SSF of FR, as it is a complex organic nutrient . The additional benefits of the amount of CR in the medium is clearly reflected in the current study.
The number of live yeast cells and the dead yeast ratio during SSF of pretreated FR mixed with CR
The results of this investigation indicated that using delignified FR combined with CR as a source of readily fermentable sugars represents an untapped source for ethanol biofuel production. Our results suggested that the increase in H2O2 concentration intensified the delignification of FR by increasing oxidation. The efficiency of ethanol fermentation was improved when delignification increased.
High intensity of FR pretreatment increased the final ethanol concentration, resulting in a high ethanol yield and a downward trend in the production of byproducts compared with SSF of the mixture of untreated FR and CR. The combination of GL-H2O2 pretreated FR and CR provided sufficient organic nutrients from starch materials for SSF and the production of additional ethanol from CR is beneficial for the integration of cellulosic and starch material, which leads to a high ethanol yield in SSF. Ethanol production from SSF of a high substrate concentration of GL-H2O2 pretreated FR and CR is therefore cost-efficient.
The ethanol concentration increased by 27.8 % from untreated FR to 0.06 g/g-H2O2-GL-pretreated FR under the same substrate loading conditions. The number of live yeast cells increased with increasing substrate concentration, while the dead yeast ratio decreased.
Further investigation is necessary to balance the ratio of GL-H2O2 pretreated FR and CR at high substrate concentration to improve the final ethanol concentration.
Raw FR was kindly provided by Chunlei Company (Hebei Province China). Raw FR, with an initial pH value was dried at 50 °C for 12 h after rinsed with water to neutral pH to remove inhibitors, including furfural and 5-HMF . The FR filtered through the 40 meshes was collected as the substrate for use in this study. CR was kindly provided by Guangxi Key Laboratory of Chemistry and Engineering of Forest Products (Nanning, China).
The raw GL was supplied by Chenming Group (Shandong, China). A supernatant was obtained by the precipitation the raw GL overnight. The contents of sodium hydroxide and sodium carbonate were tested according to TAPPI T6424 cm-00 . Calcium and iron contents of GL were measured according to TAPPI T266 om-2 . The main composition of GL was sodium carbonate reaching to 75.2 ± 0.25 g/L. The sodium hydroxide content was 23.04 ± 0.25 g/L. Other metal elements in GL such as iron and calcium were 1.14 ± 0.08 g/L and 0.39 ± 0.03 g/L, respectively .
Pretreatment with green liquor and hydrogen peroxide
CR-starch hydrolysis was performed by a two-step enzyme method in a 500 mL flask with 20 % dry matter. Briefly, CR was firstly liquefied at 85 °C for 2 h using commercial amylase enzyme at a loading of 150 u/g-CR to decrease the viscosity of CR . Subsequent saccharification was conducted at 60 °C for 1 h by glucoamylase at a loading of 20 u/g-CR (pH 4.0). Incomplete saccharification was implemented to reduce high concentrations of sugar and osmotic pressure on yeast . The pH of CR saccharification liquid was adjusted to 5.5 with 10 % sodium hydroxide before SSF.
Microorganism, inoculum and enzyme preparation
The microorganism used for fermentation was S. cerevisiaein, the form of dry yeast (Angel Yeast Company Ltd, Yichang, China). Dry yeast was activated in a 2 % glucose solution at 36 °C for 15 min, then at 34 °C for 1 h before SSF. The α-amylase and glucoamylase (Aoboxing Universeen Bio-Tech Company Ltd, Beijing, China) were used for CR liquefaction and saccharification, respectively. Cellulase (Celluclast1.5 L) with an activity of 75 filter paper units (FPU)/ml and β-glucosidase (Novozyme 188) with an activity of 43.9 IU/ml enzyme preparations (both Novozymes A/S, Bagsvaerd, Denmark) were used for SSF. The enzyme loading of Celluclast 1.5 Land Novozyme 188 were 15 FPU and 17 IU pergram cellulose of dry substrate, respectively.
Simultaneous saccharification and fermentation
The SSF experiments were performed in a 100-mL Erlenmeyer flask with a working volume of 60 mL with a loop trap containing sterile glycerol. There were two sections of this study: fixed substrate concentration (12 %) with various ratios (ranging from 1:1 to 5:1) of pretreated FR to CR and fixed ratio (2:1) of pretreated FR to CR with different substrate concentrations (6 to 12 %). The concentrations ranged from 2 to 6.7 % for CR and 3 to 13.3 % for GL-H2O2-FR. Each Erlenmeyer flask loaded with substrate and fermentation medium was sterilized separately (121 °C, 20 min). The enzymes, CR hydrolysate and yeast, with an initial inoculum concentration of 3.3 g/L were then added to the Erlenmeyer flask directly. SSF was conducted at 38 °C and 120 rpm with an initial pH of 5.5 in an air bath shaker.
SSF, simultaneous saccharification and fermentation; CR, cassava residue; FR, furfural residue; GL, green liquor; GL-H2O2, green liquor and hydrogen peroxide; 0.06 g/g-H2O2-GL-pretreated FR, FR pretreated with high loading of 0.06 g H2O2/g-substrate and 9 mL GL/g-substrate at 80 °C; WIS, water-insolible solids; 0.03 g/g-H2O2-GL-pretreated FR, FR pretreated with high loading of 0.03 g H2O2/g-substrate and 9 mL GL/g-substrate at 80 °C; PTFE, polytetrafluoroethylene; EDTA, ethylenediaminetraacetic acid; FPU, Filter paper units.
The authors are grateful for the financial support of this research provided by the State Forestry Administration (2012-03), the China Ministry of Science and Technology (2014DFG32550), and the Guangxi Key Laboratory of Chemistry and Engineering of Forest Products (GXFC12-07).
All sources of funding in the manuscript are declared.
Availability of data and material
All the data supporting our findings can be found.
JL and JJ conceived the study the study; JL and ZT carried out the experiments; ZP provided project supervision, helped with statistical design and analysis; JL and ZW wrote the paper; JJ and JL reviewed the paper. All authors read and approved the final manuscript.
The authors declare that they have no competing interests.
Consent for publication
Ethics approval and consent to participate
There are no ethics in our study and this has been added in the revised manuscript.
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