Jia Ouyang

Improved enzymatic hydrolysis of microcrystalline cellulose (Avicel PH101) by polyethylene glycol addition.

The effects of additives on hydrolysis of microcrystalline cellulose (Avicel PH101) were examined using commercial cellulose-degrading enzymes (Celluclast 1.5L and Novozyme 188). Polyethylene glycol 4000 (PEG4000) was the most effective additive tested. When PEG4000 was added at 0.05 g/g glucan, the conversion of Avicel PH101 increased 91% (from 41.1% to 78.9%). The cellulase activity of Celluclast 1.5L increased 27.5% with PEG4000 addition. A positive effect on enzyme stabilities of Celluclast 1.5L and Novozyme 188 also occurred with PEG4000 addition. During hydrolysis process, significant changes in free protein concentration and cellulase activity were observed on Avicel PH101. More than 90% of the original enzyme activity remained in the solution after 48 h hydrolysis. Thus, PEG4000 addition is an efficient method to enhance digestibility of cellulosic materials and make enzyme recovery possible and valuable. This provides an opportunity of decreasing the operational cost of the hydrolysis process.

Open fermentative production of l-lactic acid by Bacillus sp. strain NL01 using lignocellulosic hydrolyzates as low-cost raw material

Highly efficient L-lactate production by a thermophilic strain Bacillus sp. NL01 was demonstrated in this study. Lignocellulosic hydrolyzates containing a high content of glucose, which was prepared from corn stover, was used as substrate for L-lactic acid production. The fermentation was carried out under open condition without sterilization and used NaOH as alkaline neutralizing reagent. In batch fermentation, 56.37 g l(-1) L-lactic acid was obtained from lignocellulosic hydrolyzates which contained the solid residues produced in enzymatic saccharification. In fed-batch fermentation, 75.03 g l(-1) L-lactic acid was obtained from lignocellulosic hydrolyzates supernatant. The yield was 74.5% and the average productivity was 1.04 g l(-1) h(-1).

Optimization of culture conditions for production of yeast biomass using bamboo wastewater by response surface methodology

Response surface methodology (RSM) was applied to optimize culture conditions for the growth of Candida utilis with bamboo wastewater. A significant influence of initial pH, fermentation time and yeast extract on biomass of C. utilis was evaluated by Plackett-Burman design (PBD). These factors were further optimized using a central composite design (CCD) and RSM. A combination of initial pH 6.1, fermentation time 69 h and yeast extract 1.17 g/L was optimum for maximum biomass of C. utilis. A 1.7-fold enhancement of biomass of C. utilis was gained after optimization in shake-flask cultivation. The biomass of C. utilis reached 19.17 g/L in 3 L fermentor.

Impacts of lignocellulose-derived inhibitors on L-lactic acid fermentation by Rhizopus oryzae.

Inhibitors generated in the pretreatment and hydrolysis of corn stover and corn cob were identified. In general, they inhibited cell growth, lactate dehydrogenase, and lactic acid production but with less or no adverse effect on alcohol dehydrogenase and ethanol production in batch fermentation by Rhizopus oryzae. Furfural and 5-hydroxymethyl furfural (HMF) were highly toxic at 0.5-1 g L(-1), while formic and acetic acids at less than 4 g L(-1) and levulinic acid at 10 g L(-1) were not toxic. Among the phenolic compounds at 1 g L(-1), trans-cinnamic acid and syringaldehyde had the highest toxicity while syringic, ferulic and p-coumaric acids were not toxic. Although these inhibitors were present at concentrations much lower than their separately identified toxic levels, lactic acid fermentation with the hydrolysates showed much inferior performance compared to the control without inhibitor, suggesting synergistic or compounded effects of the lignocellulose-degraded compounds on inhibiting lactic acid fermentation.

Enzymatic hydrolysis, adsorption, and recycling during hydrolysis of bagasse sulfite pulp

The high costs of enzymatic hydrolysis along with the high enzyme dosage are often considered as the major bottlenecks in lignocellulosic bioconversion. This study investigated the hydrolysis efficiency, cellulase adsorption and enzyme recycling during the hydrolysis of bagasse sulfite pulp (BSP). After 48 h of hydrolysis, more than 70% of the cellulose was hydrolyzed, while the protein concentration and cellulase activity in solution remained 31% and 17% of the initial value, respectively. The cellulase adsorption on the fresh BSP was better fitted by a Sips model, suggesting the occurrence of a multilayer adsorption at low cellulase concentration and monolayer adsorption at high concentration on the BSP surfaces. Desorption profile studies showed that the optimum desorption condition was at pH 4.8 and 40 °C. Moreover, considering the limited ability to desorption, directly empolying the bound enzyme with residual substrate is more effective method to recover cellulase during the hydrolysis of BSP.

An integrated process to produce ethanol, vanillin, and xylooligosaccharides from Camellia oleifera shell

This study aims to present an integrated process that can be used to produce ethanol, vanillin, and xylooligosaccharides from Camellia oleifera shell. After the shell was pretreated with NaOH, two fractions were obtained: solid and liquid fractions. The solid fraction was hydrolyzed with cellulase and then fermented with Pichia stipitis to produce ethanol. The liquid fraction was subjected to oxidation to prepare vanillin or hydrolysis with xylanase to prepare xylooligosaccharides. The optimal pretreatment conditions of an orthogonal test were as follows: 12% NaOH concentration; 120°C; 150 min; and liquid-solid ratio of 10.0. After pretreatment, the solid fraction containing cellulose and a small part of xylan at 10% substance concentration via enzymatic hydrolysis and glucose-xylose cofermentation could obtain 17.35 g/L of ethanol, 80.90% of the theoretical yield. The liquid fraction was initially hydrolyzed with xylanase to produce 1758.63 mg/L of xylooligosaccharides (DP2-6) and then oxidized to produce 322.07 mg/L of vanillin.

Comparison of hydrolysis efficiency and enzyme adsorption of three different cellulosic materials in the presence of poly(ethylene glycol).

The addition of non-ionic surfactants has recently been confirmed to positively affect the enzymatic hydrolysis of cellulosic materials. However, the functional mechanisms of these surfactants remain unclear. This work investigated the influence of poly(ethylene glycol) (PEG) on the enzymatic hydrolysis of three cellulosic materials, namely, acid steam-exploded corn straw, pure microcrystalline cellulose (Avicel PH101), and bagasse sulfite pulp (BSP). The results showed that PEG addition led to varied effects on the enzymatic hydrolysis of different cellulosic materials. Addition of PEG was most effective on the enzymatic hydrolysis of PH101 and weakly effective on the hydrolysis of BSP. We further investigated PEG concentrations and enzymatic activities in the supernatant during hydrolysis and found that the positive effects of PEG treatment might contribute to its influence on enzyme desorption from different substrates. We also found that the efficiency of PEG depended on its capacity to bind to different substrates. PEG exhibited stronger affinity to pure cellulose than to the two other lignocellulosic substrates. These findings are helpful in further revealing the mechanism of surfactants and improving the enzymatic hydrolysis process.

Efficient Conversion of Inulin to Inulooligosaccharides through Endoinulinase from Aspergillus niger.

Inulooligosaccharides (IOS) represent an important class of oligosaccharides at industrial scale. An efficient conversion of inulin to IOS through endoinulinase from Aspergillus niger is presented. A 1482 bp codon optimized gene fragment encoding endoinulinase from A. niger DSM 2466 was cloned into pPIC9K vector and was transformed into Pichia pastoris KM71. Maximum activity of the recombinant endoinulinase, 858 U/mL, was obtained at 120 h of the high cell density fermentation process. The optimal conditions for inulin hydrolysis using the recombinant endoinulinase were investigated. IOS were harvested with a high concentration of 365.1 g/L and high yield up to 91.3%. IOS with different degrees of polymerization (DP, mainly DP 3-6) were distributed in the final reaction products.

A new magnesium bisulfite pretreatment (MBSP) development for bio-ethanol production from corn stover.

This study established a new more neutral magnesium bisulfate pretreatment (MBSP) using magnesium bisulfate as sulfonating agent for improving the enzymatic hydrolysis efficiency of corn stover. Using the MBSP with 5.21% magnesium bisulfate, 170°C and pH 5.2 for 60 min, about 90% of lignin and 80% of hemicellulose were removed from biomass and more than 90% cellulose conversion of substrate was achieved after 48 h hydrolysis. About 6.19 kg raw corn stover could produce 1 kg ethanol by Saccharomyces cerevisiae. Meanwhile, MBSP also could protect sugars from excessive degradation, prevent fermentation inhibition formation and directly convert the hemicelluloses into xylooligosaccharides as higher-value products. These results suggested that the MBSP method offers an alternative approach to the efficient conversion of nonwoody lignocellulosic biomass to ethanol and had broad space for development.

Cost-effective simultaneous saccharification and fermentation of l-lactic acid from bagasse sulfite pulp by Bacillus coagulans CC17.

The main barriers to cost-effective lactic acid production from lignocellulose are the high cost of enzymes and the ineffective utilization of the xylose within the hydrolysate. In the present study, the thermophilic Bacillus coagulans strain CC17 was used for the simultaneous saccharification and fermentation (SSF) of bagasse sulfite pulp (BSP) to produce l-lactic acid. Unexpectedly, SSF by CC17 required approximately 33.33% less fungal cellulase than did separate hydrolysis and fermentation (SHF). More interestingly, CC17 can co-ferment cellobiose and xylose without any exogenous β-glucosidase in SSF. Moreover, adding xylanase could increase the concentration of lactic acid produced via SSF. Up to 110g/L of l-lactic acid was obtained using fed-batch SSF, resulting in a lactic acid yield of 0.72g/g cellulose. These results suggest that SSF using CC17 has a remarkable advantage over SHF and that a potentially low-cost and highly-efficient fermentation process can be established using this protocol.