Yong Cheol Park

Fungal pretreatment of lignocellulose by Phanerochaete chrysosporium to produce ethanol from rice straw

Phanerochaete chrysosporium is a wood‐rot fungus that is capable of degrading lignin via its lignolytic system. In this study, an environmentally friendly fungal pretreatment process that produces less inhibitory substances than conventional methods was developed using P. chrysosporium and then evaluated by various analytical methods. To maximize the production of manganese peroxidase, which is the primary lignin‐degrading enzyme, culture medium was optimized using response surface methodologies including the Plackett–Burman design and the Box–Behnken design. Fermentation of 100u2009g of rice straw feedstock containing 35.7u2009g of glucan (mainly in the form of cellulose) by cultivation with P. chrysosporium for 15 days in the media optimized by response surface methodology was resulted in a yield of 29.0u2009g of glucan that had an enzymatic digestibility of 64.9% of the theoretical maximum glucose yield. In addition, scanning electronic microscopy, confocal laser scanning microscopy, and X‐ray diffractometry revealed significant microstructural changes, fungal growth, and a reduction of the crystallinity index in the pretreated rice straw, respectively. When the fungal‐pretreated rice straw was used as a substrate for ethanol production in simultaneous saccharification and fermentation (SSF) for 24u2009h, the ethanol concentration, production yield and the productivity were 9.49u2009g/L, 58.2% of the theoretical maximum, and 0.40u2009g/L/h, respectively. Based on these experimental data, if 100u2009g of rice straw are subjected to fungal pretreatment and SSF, 9.9u2009g of ethanol can be produced after 96u2009h, which is 62.7% of the theoretical maximum ethanol yield. Biotechnol. Bioeng. 2009; 104: 471–482

Strain engineering of Saccharomyces cerevisiae for enhanced xylose metabolism.

Efficient and rapid fermentation of all sugars present in cellulosic hydrolysates is essential for economic conversion of renewable biomass into fuels and chemicals. Xylose is one of the most abundant sugars in cellulosic biomass but it cannot be utilized by wild type Saccharomyces cerevisiae, which has been used for industrial ethanol production. Therefore, numerous technologies for strain development have been employed to engineer S. cerevisiae capable of fermenting xylose rapidly and efficiently. These include i) optimization of xylose-assimilating pathways, ii) perturbation of gene targets for reconfiguring yeast metabolism, and iii) simultaneous co-fermentation of xylose and cellobiose. In addition, the genetic and physiological background of host strains is an important determinant to construct efficient and rapid xylose-fermenting S. cerevisiae. Vibrant and persistent researches in this field for the last two decades not only led to the development of engineered S. cerevisiae strains ready for industrial fermentation of cellulosic hydrolysates, but also deepened our understanding of operational principles underlying yeast metabolism.

Microbial formation of esters

Small aliphatic esters are important natural flavor and fragrance compounds and have numerous uses as solvents and as chemical intermediates. Besides the chemical or lipase-catalyzed formation of esters from alcohols and organic acids, small volatile esters are made by several biochemical routes in microbes. This short review will cover the biosynthesis of esters from acyl-CoA and alcohol condensation, from oxidation of hemiacetals formed from aldehydes and alcohols, and from the insertion of oxygen adjacent to the carbonyl group in a straight chain or cyclic ketone by Baeyer–Villiger monooxygenases. The physiological role of the ester-forming reactions can allow degradation of ketones for use as a carbon source and may play a role in detoxification of aldehydes or recycling cofactors. The enzymes catalyzing each of these processes have been isolated and characterized, and a number of genes encoding the proteins from various microbes have been cloned and functionally expressed. The use of these ester-forming organisms or recombinant organisms expressing the appropriate genes as biocatalysts in biotechnology to make specific esters and chiral lactones has been studied in recent years.

Compounds inhibiting the bioconversion of hydrothermally pretreated lignocellulose.

Hydrothermal pretreatment using liquid hot water, steam explosion, or dilute acids enhances the enzymatic digestibility of cellulose by altering the chemical and/or physical structures of lignocellulosic biomass. However, compounds that inhibit both enzymes and microbial activity, including lignin-derived phenolics, soluble sugars, furan aldehydes, and weak acids, are also generated during pretreatment. Insoluble lignin, which predominantly remains within the pretreated solids, also acts as a significant inhibitor of cellulases during hydrolysis of cellulose. Exposed lignin, which is modified to be more recalcitrant to enzymes during pretreatment, adsorbs cellulase nonproductively and reduces the availability of active cellulase for hydrolysis of cellulose. Similarly, lignin-derived phenolics inhibit or deactivate cellulase and β-glucosidase via irreversible binding or precipitation. Meanwhile, the performance of fermenting microorganisms is negatively affected by phenolics, sugar degradation products, and weak acids. This review describes the current knowledge regarding the contributions of inhibitors present in whole pretreatment slurries to the enzymatic hydrolysis of cellulose and fermentation. Furthermore, we discuss various biological strategies to mitigate the effects of these inhibitors on enzymatic and microbial activity to improve the lignocellulose-to-biofuel process robustness. While the inhibitory effect of lignin on enzymes can be relieved through the use of lignin blockers and by genetically engineering the structure of lignin or of cellulase itself, soluble inhibitors, including phenolics, furan aldehydes, and weak acids, can be detoxified by microorganisms or laccase.

Production of 2,3-butanediol from xylose by engineered Saccharomyces cerevisiae

2,3-Butanediol (2,3-BD) production from xylose that is abundant in lignocellulosic hydrolyzate would make the production of 2,3-BD more sustainable and economical. Saccharomyces cerevisiae can produce only trace amounts of 2,3-BD, but also cannot ferment xylose. Therefore, it is necessary to introduce both 2,3-BD production and xylose assimilation pathways into S. cerevisiae for producing 2,3-BD from xylose. A pyruvate decarboxylase (Pdc)-deficient mutant (SOS4) was used as a host in order to increase carbon flux toward 2,3-BD instead of ethanol. The XYL1, XYL2, and XYL3 genes coding for xylose assimilating enzymes derived from Scheffersomyces stipitis were introduced into the SOS4 strain to enable xylose utilization. Additionally, the alsS and alsD genes from Bacillus subtilis and endogenous BDH1 gene were overexpressed to increase 2,3-BD production from xylose. As a result, the resulting strain (BD4X) produced 20.7g/L of 2,3-BD from xylose with a yield of 0.27g 2,3-BD/g xylose. The titer of 2,3-BD from xylose increased up to 43.6g/L under a fed-batch fermentation. The BD4X strain produced (R, R)-2,3-BD dominantly (>97% of the total 2,3-BD) with trace amounts of meso-2,3-BD. These results suggest that S. cerevisiae might be a promising host for producing 2,3-BD from lignocellulosic biomass for industrial applications.

Recent advances in biological production of sugar alcohols

Sugar alcohols, such as xylitol, mannitol, sorbitol, and erythritol are emerging food ingredients that provide similar or better sweetness/sensory properties of sucrose, but are less calorigenic. Also, sugar alcohols can be converted into commodity chemicals through chemical catalysis. Biotechnological production offers the safe and sustainable supply of sugar alcohols from renewable biomass. In contrast to early studies that aimed to produce sugar alcohols with microorganisms capable of producing sugar alcohols naturally, recent studies have focused on rational engineering of metabolic pathways to improve yield and productivity as well as to use inexpensive and abundant substrates. Metabolic engineering strategies to utilize inexpensive substrates, alleviate catabolite repression, reduce byproduct formation, and manipulate redox balances led to enhanced production of sugar alcohols.

Mimicking the Fenton reaction-induced wood decay by fungi for pretreatment of lignocellulose.

In this study, the Fenton reaction, which is naturally used by fungi for wood decay, was employed to pretreat rice straw and increase the enzymatic digestibility for the saccharification of lignocellulosic biomass. Using an optimized Fentons reagent (FeCl3 and H2O2) for pretreatment, an enzymatic digestibility that was 93.2% of the theoretical glucose yield was obtained. This is the first report of the application of the Fenton reaction to lignocellulose pretreatment at a moderate temperature (i.e., 25°C) and with a relatively high loading of biomass (i.e., 10% (w/v)). Substantial improvement in the process economics of cellulosic fuel and chemical production can be achieved by replacing the conventional pretreatment with this Fenton-mimicking process.

Enhanced tolerance of Saccharomyces cerevisiae to multiple lignocellulose-derived inhibitors through modulation of spermidine contents

Fermentation inhibitors present in lignocellulose hydrolysates are inevitable obstacles for achieving economic production of biofuels and biochemicals by industrial microorganisms. Here we show that spermidine (SPD) functions as a chemical elicitor for enhanced tolerance of Saccharomyces cerevisiae against major fermentation inhibitors. In addition, the feasibility of constructing an engineered S. cerevisiae strain capable of tolerating toxic levels of the major inhibitors without exogenous addition of SPD was explored. Specifically, we altered expression levels of the genes in the SPD biosynthetic pathway. Also, OAZ1 coding for ornithine decarboxylase (ODC) antizyme and TPO1 coding for the polyamine transport protein were disrupted to increase intracellular SPD levels through alleviation of feedback inhibition on ODC and prevention of SPD excretion, respectively. Especially, the strain with combination of OAZ1 and TPO1 double disruption and overexpression of SPE3 not only contained spermidine content of 1.1mg SPD/g cell, which was 171% higher than that of the control strain, but also exhibited 60% and 33% shorter lag-phase period than that of the control strain under the medium containing furan derivatives and acetic acid, respectively. While we observed a positive correlation between intracellular SPD contents and tolerance phenotypes among the engineered strains accumulating different amounts of intracellular SPD, too much SPD accumulation is likely to cause metabolic burden. Therefore, genetic perturbations for intracellular SPD levels should be optimized in terms of metabolic burden and SPD contents to construct inhibitor tolerant yeast strains. We also found that the genes involved in purine biosynthesis and cell wall and chromatin stability were related to the enhanced tolerance phenotypes to furfural. The robust strains constructed in this study can be applied for producing chemicals and advanced biofuels from cellulosic hydrolysates.

Aqueous ammonia pretreatment, saccharification, and fermentation evaluation of oil palm fronds for ethanol production

Oil palm fronds are the most abundant lignocellulosic biomass in Malaysia. In this study, fronds were tested as the potential renewable biomass for ethanol production. The soaking in aqueous ammonia pretreatment was applied, and the fermentability of pretreated fronds was evaluated using simultaneous saccharification and fermentation. The optimal pretreatment conditions were 7xa0% (w/w) ammonia, 80xa0°C, 20xa0h of pretreatment, and 1:12 S/L ratio, where the enzymatic digestibility was 41.4xa0% with cellulase of 60xa0FPU/g-glucan. When increasing the cellulase loading in the hydrolysis of pretreated fronds, the enzymatic digestibility increased until the enzyme loading reached 60xa0FPU/g-glucan. With 3xa0% glucan loading in the SSF of pretreated fronds, the ethanol concentration and yield based on the theoretical maximum after 12 and 48xa0h of the SSF were 7.5 and 9.7xa0g/L and 43.8 and 56.8xa0%, respectively. The ethanol productivities found at 12 and 24xa0h from pretreated fronds were 0.62 and 0.36xa0g/L/h, respectively.

Optimal production of 4-deoxy- l -erythro-5-hexoseulose uronic acid from alginate for brown macro algae saccharification by combining endo- and exo-type alginate lyases

AbstractnAlgae are considered as third-generation biomass, and alginate is the main component of brown macroalgae. Alginate can be enzymatically depolymerized by alginate lyases into uronate monomers, such as mannuronic acid and guluronic acid, which are further nonenzymatically converted to 4-deoxy-l-erythro-5-hexoseulose uronic acid (DEH). We have optimized an enzymatic saccharification process using two recombinant alginate lyases, endo-type Alg7D and exo-type Alg17C, for the efficient production of DEH from alginate. When comparing the sequential and simultaneous additions of Alg7D and Alg17C, it was found that the final yield of DEH was significantly higher when the enzymes were added sequentially. The progress of saccharification reactions and production of DEH were verified by thin layer chromatography and gas chromatography–mass spectrometry, respectively. Our results showed that the two recombinant enzymes could be exploited for the efficient production of DEH that is the key substrate for producing biofuels from brown macro algal biomass.