Effect of furfural on the growth of lactose-utilizing Candida Blankii 35

The effects of furfural on the growth of the lactose-utilizing yeast Candida blankii 35 were investigated using the method of continuous cultivation under conditions of carbon limitation and at dilution rates of 0.1 and 0.25 h⁻¹. The data obtained at dilution rate 0.1 h⁻¹ and 0.04% furfural showed a decrease in the yield of biomass by 6% and in the RNA content, but the synthesis of cell protein increased with 11.6% compared to the control. Treatment with 0.08% furfural induced significant changes in growth and biosynthesizing ability. A strong inhibitory effect of furfural was observed: the biomass yield decreased by half at 48 h and the culture the reached the control level of protein content. The effect of 0.02% furfural at 0.25 h⁻¹ dilution rate caused a significant reduction of biomass yield (34.4%) and the substrate utilization rate reached values higher by 52.4% at 48 h, but the protein-synthesizing ability of the cells slightly increased. The results showed that a treatment with 0.04 or 0.08% furfural caused significant disturbances of cell functions, the yields of biomass and protein drastically decreased and the culture was washed out. Data showed that the inhibitory effect of furfural on the growth and protein-synthesizing ability of Candida blankii 35 depends on the inhibitor concentration as well as the dilution rate. This revised version was published online in August 2006 with corrections to the Cover Date.     

Conversion of furfural into furfuryl alcohol by saccharomyces cervisiae 354

The influence of aeration, stirring conditions, and the addition of furfural on the yield and productivity of furfural – furfuryl alcohol bioconversion by the yeast strain Saccharomyces cerevisiae 354 was investigated. The formation of furfuryl alcohol increases up to 32 hours of incubation corresponding to the addition of furfural, while the cell growth essentially ceased at 20 hours. The conversion of furfural into furfuryl alcohol under anaerobic and low aeration conditions was 70% and the productivity 0.5g · 1^?1 · h^?1, when the final concentrationof of furfural amounted to 35 g · 1^?1.     

Biochemical characterization of ethanol-dependent reduction of furfural by alcohol dehydrogenases

Lignocellulosic biomass is usually converted to hydrolysates, which consist of sugars and sugar derivatives, such as furfural. Before yeast ferments sugars to ethanol, it reduces toxic furfural to non-inhibitory furfuryl alcohol in a prolonged lag phase. Bioreduction of furfural may shorten the lag phase. Cupriavidus necator JMP134 rapidly reduces furfural with a Zn-dependent alcohol dehydrogenase (FurX) at the expense of ethanol (Li et al. 2011). The mechanism of the ethanol-dependent reduction of furfural by FurX and three homologous alcohol dehydrogenases was investigated. The reduction consisted of two individual reactions: ethanol-dependent reduction of NAD⁺ to NADH and then NADH-dependent reduction of furfural to furfuryl alcohol. The kinetic parameters of the coupled reaction and the individual reactions were determined for the four enzymes. The data indicated that limited NADH was released in the coupled reaction. The enzymes had high affinities for NADH (e.g., K _d of 0.043 μM for the FurX-NADH complex) and relatively low affinities for NAD⁺ (e.g., K _d of 87 μM for FurX-NAD⁺). The kinetic data suggest that the four enzymes are efficient “furfural reductases” with either ethanol or NADH as the reducing power. The standard free energy change (ΔG°′) for ethanol-dependent reduction of furfural was determined to be −1.1 kJ mol⁻¹. The physiological benefit for ethanol-dependent reduction of furfural is likely to replace toxic and recalcitrant furfural with less toxic and more biodegradable acetaldehyde.     

Mediated electrochemical measurement of the inhibitory effects of furfural and acetic acid on <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> and <Emphasis Type="Italic">Candida shehatae</Emphasis>

The toxic effects of furfural and acetic acid on two yeasts, Saccharomyces cerevisiae and Candida shehatae, were evaluated using an electrochemical method. Intracellular redox activities were lowered by 40% and 78% for S. cerevisiae and C. shehatae, respectively, by 8 g furfural l^–1, and by 46% and 67%, respectively, by 8 g acetic acid l^–1. The proposed method can accurately measure the effects of inhibitors on cell cultures.Revisions requested 27 September 2004/17 November 2004; Revisions received 15 November 2004/10 December 2004     

<Emphasis Type="Italic">Cupriavidus necator</Emphasis> JMP134 rapidly reduces furfural with a Zn-dependent alcohol dehydrogenase

Ethanol is a renewable biofuel, and it can be produced from lignocellulosic biomass. The biomass is usually converted to hydrolysates that consist of sugar and sugar derivatives, such as furfural. Yeast ferments sugar to ethanol, but furfural higher than 3 mM is inhibitory. It can take several days for yeast cells to reduce furfural to non-inhibitory furfuryl alcohol before producing ethanol. Bioreduction of furfural to furfuryl alcohol before fermentation may relieve yeast from furfural toxicity. We observed that Cupriavidus necator JMP134, a strict aerobe, rapidly reduced 17 mM furfural to less than 3 mM within 14 min with cell turbidity of 1.0 at 600 nm at 50°C. The rapid reduction consumed ethanol. The “furfural reductase” (FurX) was purified, and it oxidized ethanol to acetaldehyde and reduced furfural to furfuryl alcohol with NAD⁺ as the cofactor. The protein was identified with mass spectrometry fingerprinting to be a hypothetical protein belonging to Zn-dependent alcohol dehydrogenase family. The furX-inactivation mutant of C. necator JMP134 lost the ability to rapidly reduce furfural, and Escherichia coli producing recombinant FurX gained the ability. Thus, an alcohol dehydrogenase enabled bacteria to rapidly reduce furfural with ethanol as the reducing power.     

Extreme thermophilic ethanol production from rapeseed straw: Using the newly isolated Thermoanaerobacter pentosaceus and combining it with Saccharomyces cerevisiae in a two‐step process

The newly isolated extreme thermophile Thermoanaerobacter pentosaceus was used for ethanol production from alkaline‐peroxide pretreated rapeseed straw (PRS). Both the liquid and solid fractions of PRS were used. T. pentosaceus was able to metabolize the typical process inhibitors present in lignocellulosic hydrolysate, namely 5‐hydroxymethyl furfural (HMF) and furfural, up to concentrations of 1 and 0.5 g L^?1, respectively. Above these levels, xylose consumption was inhibited up to 70% (at 3.4 g‐furfural L^?1) and 75% (at 3.4 g‐HMF L^?1). T. pentosaceus was able to grow and produce ethanol directly from the liquid fraction of PRS, without any dilution or need for additives. However, when the hydrolysate was used undiluted the ethanol yield was only 37% compared to yield of the control, in which pure sugars in synthetic medium were used. The decrease of ethanol yield was attributed to the high amounts of salts resulting from the alkaline‐peroxide pretreatment. Finally, a two‐stage ethanol production process from PRS using Saccharomyces cerevisiae (utilization of hexoses in the first step) and T. pentosaceus (utilization of pentoses in the second step) was developed. Results showed that the two strains together could achieve up to 85% of the theoretical ethanol yield based on the sugar composition of the rapeseed straw, which was 14% and 50% higher compared to the yield with the yeast or the bacteria alone, respectively. Biotechnol. Bioeng. 2013; 110: 1574–1582. © 2012 Wiley Periodicals, Inc.     

Butanol production from sweet sorghum bagasse with high solids content: Part I—comparison of liquid hot water pretreatment with dilute sulfuric acid

In these studies, we pretreated sweet sorghum bagasse (SSB) using liquid hot water (LHW) or dilute H₂SO₄ (2 g L^?1) at 190°C for zero min (as soon as temperature reached 190°C, cooling was started) to reduce generation of sugar degradation fermentation inhibiting products such as furfural and hydroxymethyl furfural (HMF). The solids loading were 250–300 g L^?1. This was followed by enzymatic hydrolysis. After hydrolysis, 89.0 g L^?1 sugars, 7.60 g L^?1 acetic acid, 0.33 g L^?1 furfural, and 0.07 g L^?1 HMF were released. This pretreatment and hydrolysis resulted in the release of 57.9% sugars. This was followed by second hydrolysis of the fibrous biomass which resulted in the release of 43.64 g L^?1 additional sugars, 2.40 g L^?1 acetic acid, zero g L^?1 furfural, and zero g L^?1 HMF. In both the hydrolyzates, 86.3% sugars present in SSB were released. Fermentation of the hydrolyzate I resulted in poor acetone‐butanol‐ethanol (ABE) fermentation. However, fermentation of the hydrolyzate II was successful and produced 13.43 g L^?1 ABE of which butanol was the main product. Use of 2 g L^?1 H₂SO₄ as a pretreatment medium followed by enzymatic hydrolysis resulted in the release of 100.6–93.8% (w/w) sugars from 250 to 300 g L^?1 SSB, respectively. LHW or dilute H₂SO₄ were used to economize production of cellulosic sugars from SSB. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:960–966, 2018     

分别利用产甘油假丝酵母抗逆转录因子CgSTB5和CgSEF1对酿酒酵母菌株糠醛耐受改造

【背景】纤维素是生物转化解决能源问题的主要原料之一,其水解物中存在严重影响抑制菌株生长的糠醛,需脱毒才可应用于发酵,提高菌株耐受性是解决纤维素水解液实际生产应用的关键。【目的】酿酒酵母(Saccharomyces cerevisiae)是主要的纤维素水解液发酵工业菌株,但糠醛耐受性较低,通过分子改造获得具有高糠醛耐受性的菌株。【方法】利用新获得的产甘油假丝酵母(Candidaglycerinogenes)的相关抗逆转录因子CgSTB5、CgSEF1和CgCAS5,通过分子技术进行S.cerevisiae改造,考察其对酿酒酵母糠醛耐受性的影响,并尝试应用于未脱毒纤维素乙醇发酵。【结果】单个表达CgSTB5和CgSEF1的酿酒酵母,通过菌株点板实验表明菌株的糠醛耐受性提高25%以上,并且摇瓶发酵结果显示糠醛降解性能明显提高,生长延滞期明显缩短,S.cerevisiae W303/p414-CgSTB5的未脱毒纤维素乙醇发酵生产效率提高12.5%左右。【结论】转录因子CgSTB5和CgSEF1均能对提高酿酒酵母糠醛耐受性起到重要作用,并且有助于提高酿酒酵母菌株未脱毒纤维素乙醇发酵性能。     

Biotransformation of furfural by yeast cells covalently bound to cellulose granules

A covalent binding to cellulose granules of two yeast strains Candida tropicalis and Trichosporon cutaneum was achieved. The maximum activity for destroying furfural by the immobilized cells was obtained when the procedure conditions were: reaction medium at pH 5.0, 20°C and cell suspension concentration of 80 mg/ml. The continuous furfural transformation was studied using a growth medium in a fermenter with immobilized Trichosporon cutaneum in which a 84% bioconversion was achieved. The reduced values of furfural remained constant even after 10-fold transformation.     

Genome-Wide Mapping of Furfural Tolerance Genes in Escherichia coli

Advances in genomics have improved the ability to map complex genotype-to-phenotype relationships, like those required for engineering chemical tolerance. Here, we have applied the multiSCale Analysis of Library Enrichments (SCALEs; Lynch et al. (2007) Nat. Method.) approach to map, in parallel, the effect of increased dosage for >10⁵ different fragments of the Escherichia coli genome onto furfural tolerance (furfural is a key toxin of lignocellulosic hydrolysate). Only 268 of >4,000 E. coli genes (∼6%) were enriched after growth selections in the presence of furfural. Several of the enriched genes were cloned and tested individually for their effect on furfural tolerance. Overexpression of thyA, lpcA, or groESL individually increased growth in the presence of furfural. Overexpression of lpcA, but not groESL or thyA, resulted in increased furfural reduction rate, a previously identified mechanism underlying furfural tolerance. We additionally show that plasmid-based expression of functional LpcA or GroESL is required to confer furfural tolerance. This study identifies new furfural tolerant genes, which can be applied in future strain design efforts focused on the production of fuels and chemicals from lignocellulosic hydrolysate.     

Mixed inhibitions by methanol, furfural and acetic acid on xylitol production by Candida guilliermondii

Xylose production by Candida guilliermondii FTI 20037 was carried out in a synthetic medium in the presence of 0–100 g methanol l^–1, 0–0.7 g furfural l^–1 or 0–1.3 g acetic acid l^–1. Kinetic results show a mixed inhibition mechanism in all three cases. Maximum specific productivity and saturation constant for product formation were, in the absence of inhibition, 3.6 g_P g_X ^–1 h^–1 and 232 g_S l^–1, respectively, while the inhibition constants, K _i and K _i, were 17 and 50 g methanol l^–1, 0.62 and 7.0 g furfural l^–1, 0.69 and 3.5 g acetic acid l^–1, which suggests the following order of inhibition: furfural > acetic acid > methanol.     

Furfural formation from d-xylose: the use of different halides in dilute aqueous acidic solutions allows for exceptionally high yields

Starting from the results achieved in a previous work on the effects of Cl⁻ ions on furfural formation in aqueous acid solution [Marcotullio, G. et al., Green Chem.2010, 12, 1739], the general effect of different halides is addressed. Experimental results show the halides to influence at least two distinct steps in the reaction leading from d-xylose to furfural under acidic conditions, via different mechanisms. The nucleophilicity of the halides appears to be critical for the dehydration, but not for the initial enolization reaction. By combining different halides synergic effects become evident resulting in very high selectivities and furfural yields.     

Tolerance to furfural-induced stress is associated with pentose phosphate pathway genes ZWF1, GND1, RPE1, and TKL1 in Saccharomyces cerevisiae

Engineering yeast to be more tolerant to fermentation inhibitors, furfural and 5-hydroxymethylfurfural (HMF), will lead to more efficient lignocellulose to ethanol bioconversion. To identify target genes involved in furfural tolerance, a Saccharomyces cerevisiae gene disruption library was screened for mutants with growth deficiencies in the presence of furfural. It was hypothesized that overexpression of these genes would provide a growth benefit in the presence of furfural. Sixty two mutants were identified whose corresponding genes function in a wide spectrum of physiological pathways, suggesting that furfural tolerance is a complex process. We focused on four mutants, zwf1, gnd1, rpe1, and tkl1, which represent genes encoding pentose phosphate pathway (PPP) enzymes. At various concentrations of furfural and HMF, a clear association with higher sensitivity to these inhibitors was demonstrated in these mutants. PPP mutants were inefficient at reducing furfural to the less toxic furfuryl alcohol, which we propose is a result of an overall decreased abundance of reducing equivalents or to NADPH's role in stress tolerance. Overexpression of ZWF1 in S. cerevisiae allowed growth at furfural concentrations that are normally toxic. These results demonstrate a strong relationship between PPP genes and furfural tolerance and provide additional putative target genes involved in furfural tolerance.Mention of trade names or commercial products in this publication is solely for the purpose of providing specific information and does not imply recommendation or endorsement by the US Department of Agriculture.     

Chitosan production from hemicellulose hydrolysate of corn straw: impact of degradation products on Rhizopus oryzae growth and chitosan fermentation

Aims: To examine the potential use of hemicellulose hydrolysate (HH) for the production of chitosan by Rhizopus oryzae and investigate the influence of contents in HH on mycelia growth and chitosan synthesis. Methods and Results: Compared to xylose medium, HH enhanced mycelia growth, chitosan content and production of R. oryzae by 10·2, 64·5 and 82·1%, respectively. During sulfuric acid hydrolysis of corn straw, sugars (glucose, galactose, etc) and inhibitors (formic acid, acetic acid and furfural) were generated. Acetic acid (2·14 g l^?1) and formic acid (0·83 g l^?1) were stimulative, while furfural (0·55 g l^?1) was inhibitory. Inhibitors, at different concentrations, increased the mycelia growth and chitosan production by 24·5–37·8 and 60·1–207·1%. Conclusions: HH of corn straw is a good source for chitosan production. Inhibitors in HH, at proper concentrations, can enhance chitosan production greatly. Significance and Impact of the Study: This work for the first time reported chitosan production from HH. Chitosan production can be greatly enhanced by cheap chemicals such as inhibitors in HH.     

Anaerobic degradation of sulphite evaporator condensate in a fixed-bed loop reactor by a defined bacterial consortium

Summary After elucidating the composition of an anaerobic bacterial enrichment culture treating sulphite evaporator condensate (SEC), an effluent in the pulp and paper industry, we built up stepwise a defined mixed culture to convert the organic constituents of SEC (acetate, methanol, furfural) to methane and CO₂. In batch cultures Desulfovibrio furfuralis and Methanobacterium bryantii degraded furfural in the absence of sulphate via inter-species H₂ transfer yielding 0.42 mol methane and 1.87 mol acetate/mol furfural degraded. When Methanosarcina barkeri was added to this diculture, acetate was also transformed to methane yielding 0.93 mol methane/mol acetate converted. This consortium (D. furfuralis, Methanobacterium bryantii and Methanosarcina barkeri) degraded furfural in continuous culture (fixed-bed loop reactor) to 92%, but the conversion of acetate was only 67%. The conversion of acetate could be further improved to 86% by adding 10 mm sulphate to the medium. This resulted in a space time yield of 10.9 g chemical oxygen demand (COD)/1 per day for the overall conversion. With a consortium consisting of M. barkeri, Methanobrevibacter arboriphilus, Methanosaeta concilii and D. furfuralis, a synthetic SEC could be degraded at a space time yield of 13.35 g COD/1 per day. This defined culture degraded all the constituents of SEC at an efficiency of almost 90% compared to an enrichment culture under identical conditions.Offprint requests to: U. Ney     

New application of single and mixed immobilized cells for furfural biodegradation

In this study, a new application of immobilized microbial cells for biodegradation of furfural in aqueous solution was investigated using spouted bed bioreactor. Pseudomonas sp., as a single type specie as well as activated sludge as mixed cultures were individually immobilized in 3 different bio-carrier matrices which were prepared by reinforcement of natural polysaccharides including sodium alginate, guar-gum and agar-agar with polyvinyl alcohol. The results demonstrated a complete removal (100%) of furfural from aqueous solutions using immobilized cells (IC) of Pseudomonas sp., and mixed cultures as well. Recycling of used IC for furfural removal in successive treatment cycles provided significant removal rates up to 96%. In general, results revealed that IC exhibited better performance compared to free cells in regard with the removal rate of furfural, duration of biodegradation process, as well as the ability for recycling and sustaining the high concentrations of furfural.     

Evaluation of cellulases produced from four fungi cultured on furfural residues and microcrystalline cellulose

Four fungal strains—Trichoderma viride, Aspergillus niger, Trichoderma koningii, and Trichoderma reesei—were selected for cellulase production using furfural residues and microcrystalline cellulose (MCC) as the substrates. The filter paper activity (FPA) of the supernatant from each fungus was measured, and the performance of the enzymes from different fungal strains was compared. Moreover, the individual activities of the three components of the cellulase system, i.e., β-glucosidase, endoglucanase, and exoglucanase were evaluated. T. koningii showed the highest activity (27.81 FPU/ml) on furfural residues, while T. viride showed an activity of 21.61 FPU/ml on MCC. The FPA of the crude enzyme supernatant from T. koningii was 30% higher on furfural residues than on MCC. T. koningii and T. viride exhibited high stability and productivity and were chosen for cellulases production. The crystallinity index (CrI) of the furfural residues varied after digested by the fungi. The results indicated differences in the functioning of the cellulase system from each fungus. In the case of T. koningii, T. reesei and T. viride, furfural residues supported a better environment for cellulase production than MCC. Moreover, the CrI of the furfural residues decreased, indicating that this material was largely digested by the fungi. Thus, our results suggest that it may be possible to use the cellulases produced from these fungi for the simultaneous saccharification and fermentation of lignocellulosic materials in ethanol production.     

Hydrothermal pretreatment of sugarcane bagasse using response surface methodology improves digestibility and ethanol production by SSF

Sugarcane bagasse was characterized as a feedstock for the production of ethanol using hydrothermal pretreatment. Reaction temperature and time were varied between 160 and 200°C and 5–20 min, respectively, using a response surface experimental design. The liquid fraction was analyzed for soluble carbohydrates and furan aldehydes. The solid fraction was analyzed for structural carbohydrates and Klason lignin. Pretreatment conditions were evaluated based on enzymatic extraction of glucose and xylose and conversion to ethanol using a simultaneous saccharification and fermentation scheme. SSF experiments were conducted with the washed pretreated biomass. The severity of the pretreatment should be sufficient to drive enzymatic digestion and ethanol yields, however, sugars losses and especially sugar conversion into furans needs to be minimized. As expected, furfural production increased with pretreatment severity and specifically xylose release. However, provided that the severity was kept below a general severity factor of 4.0, production of furfural was below an inhibitory concentration and carbohydrate contents were preserved in the pretreated whole hydrolysate. There were significant interactions between time and temperature for all the responses except cellulose digestion. The models were highly predictive for cellulose digestibility (R ² = 0.8861) and for ethanol production (R ² = 0.9581), but less so for xylose extraction. Both cellulose digestion and ethanol production increased with severity, however, high levels of furfural generated under more severe pretreatment conditions favor lower severity pretreatments. The optimal pretreatment condition that gave the highest conversion yield of ethanol, while minimizing furfural production, was judged to be 190°C and 17.2 min. The whole hydrolysate was also converted to ethanol using SSF. To reduce the concentration of inhibitors, the liquid fraction was conditioned prior to fermentation by removing inhibitory chemicals using the fungus Coniochaeta ligniaria.