Amelioration of the ability to decolorize dyes by laccase: relationship between redox mediators and laccase isoenzymes in Trametes versicolor

The effect of redox mediators in the dye decolorization by two laccase isoenzymes from Trametes versicolor cultures supplemented with barley bran has been investigated. All the redox mediators tested, 1-hydroxybenzotriazole (HBT), promazine (PZ), para-hydroxybenzoic acid (pHBA) and 1-nitroso-2-naphthol-3,6-disulfonic acid (NNDS), led to higher dye decolorization than those obtained without mediator addition. Among the different tested mediators, PZ was the most effective one at a low range of concentration (0.5–50 μM) and the natural mediator employed, pHBA did not improve significantly the degree of decolorization, and was slightly inhibitory.The two laccase isoenzymes, LacI and LacII, showed different decolorization capability depending on the mediator used. No significant differences were detected for NNDS, however LacII was more effective than LacI in the presence of PZ, while in the presence of HBT LacI was the fastest and the most effective isoenzyme.     

Repeated-batch fermentation of lignocellulosic hydrolysate to ethanol using a hybrid Saccharomyces cerevisiae strain metabolically engineered for tolerance to acetic and formic acids

A major challenge associated with the fermentation of lignocellulose-derived hydrolysates is improved ethanol production in the presence of fermentation inhibitors, such as acetic and formic acids. Enhancement of transaldolase (TAL) and formate dehydrogenase (FDH) activities through metabolic engineering successfully conferred resistance to weak acids in a recombinant xylose-fermenting Saccharomyces cerevisiae strain. Moreover, hybridization of the metabolically engineered yeast strain improved ethanol production from xylose in the presence of both 30 mM acetate and 20 mM formate. Batch fermentation of lignocellulosic hydrolysate containing a mixture of glucose, fructose and xylose as carbon sources, as well as the fermentation inhibitors, acetate and formate, was performed for five cycles without any loss of fermentation capacity. Long-term stability of ethanol production in the fermentation phase was not only attributed to the coexpression of TAL and FDH genes, but also the hybridization of haploid strains.     

Studies of the production and characterization of laccase activity in the basidiomycete Coriolopsis gallica, an efficient decolorizer of alkaline effluents

The basidiomycete Coriolopsis gallica decolorizes alkaline paper effluents efficiently. In this work, we found that C. gallica produces laccase during this decolorization process. This enzymatic activity was produced in all media studied; however, the highest enzymatic activity was obtained in a medium containing paper effluent, where laccase was detected on the 2nd day of the experiment. The laccase activity of C. gallica was purified and characterized. The amino-terminal sequence of this protein showed the highest similarity with the laccase I of the basidiomycete PM1 and with Coriolus hirsutus laccase. Received: 20 April 1998 / Accepted: 21 September 1998     

New and different lignocellulosic materials from Turkey for laccase and manganese peroxidase production by Trametes versicolor

In the present study, the production of laccase (Lac) and manganese‐dependent peroxidase (MnP) by the white‐rot fungus Trametes versicolor grown in submerged cultures with different agricultural residues was investigated. The lignocellulosic materials studied were almond shells, hazelnut husks, sunflower stems, clover straw and hazelnut cobs, because they are common agricultural wastes in Turkey. Among the different lignocellulosic materials studied, hazelnut cobs provided the highest Lac and MnP activities (47.09 and 109.21 U/L, respectively). The optimum conditions were determined for Lac and MnP production in submerged cultures of T. versicolor by using hazelnut cobs as substrate. For Lac production, the optimum incubation time, hazelnut cob concentration, pH, and shaking rate were found as 4 days, 2% w/v, 6.0 and 130 rpm, respectively. For MnP production, the optimum incubation time, hazelnut cob concentration, pH and shaking rate were found as 5 days, 2% w/v, 6.0 and 90 rpm, respectively.     

毛栓菌产漆酶条件优化及该酶对合成染料脱色的特性

【目的】提高菌株Trametes hirsuta SYBC-L19漆酶产量,并研究该酶对合成染料脱色的性质。【方法】通过单因素和响应面设计,对产漆酶培养基进行优化。【结果】最优培养基为:玉米粉20.0 g/L、马铃薯淀粉32.4 g/L、酒石酸铵2.9 g/L、吐温80 0.5 g/L、CuSO4.5H2O 2.0 mmol/L、香兰素0.54 mmol/L、NaH2PO4.2H2O 2.0 g/L、MgSO4.7H2O0.5 g/L、MnSO4.H2O 0.1 g/L;最佳培养条件为:培养温度30°C,初始pH 6.0,装液量40 mL/250 mL,接种量8%。【结论】培养8 d酶活达35 U/mL,是优化前的39倍。对漆酶催化合成染料脱色进行了考察,发现该酶在60°C下对偶氮类染料AR1和RB5能迅速脱色,5 min内即可完成。     

Enzymatic saccharification of cornstalk by onsite cellulases produced by Trichoderma viride for enhanced biohydrogen production

Lignocellulosic biomass, if properly saccharified, could be an ideal feedstock for biohydrogen production. However, the high cellulases cost is the key obstacle to its development. In this work, cost‐effective enzyme produced by Trichoderma viride was used to saccharify cornstalk. To obtain high sugar yield, a central composite design of response surface method was used to optimize enzymatic saccharification process. Experimental results showed that the enzymatic saccharification rate reached the highest of 81.2% when pH, temperature, cellulases and substrate concentration were 5, 49.7 °C, 35.7 IU g^?1, and 38.5 g L^?1, respectively. The cornstalk hydrolysate was subsequently introduced to fermentation by Thermoanaerobacterium thermosaccharolyticum W16, the yield of hydrogen reached the highest level of 90.6 ml H₂ g^?1 pretreated cornstalk. The present results indicate the potential of using T. thermosaccharolyticum W16 for high yield conversion of cornstalk hydrolysate, which was saccharified by onsite enzyme produced by T. viride.     

Cost reduction and feedstock diversity for sulfuric acid-free ethanol cooking of lignocellulosic biomass as a pretreatment to enzymatic saccharification

We have previously demonstrated that a sulfuric acid-free ethanol (EtOH) cooking treatment enhances the enzymatic digestibility of eucalyptus wood and bagasse flour. In the present study, a reconfigured process that achieves similar performance was developed by identifying possible cost-competitive pretreatments that provide high cellulose-to-glucose conversion during subsequent enzymatic hydrolysis. The series of reconfigurations reduced EtOH usage in the pretreatment by more than 80% in comparison with our previous research. Higher initial pressures and intensive size reduction of the starting material are not required. The reconfigured process was applied to rice straw and Douglas fir, in order to confirm the feasibility of feedstock diversity.     

Ethanol production by continuous fermentation of D-(+)-cellobiose, D-(+)-xylose and sugarcane bagasse hydrolysate using the thermoanaerobe Caloramator boliviensis

The recently isolated anaerobic bacterium Caloramator boliviensis with an optimum growth temperature of 60 °C can efficiently convert hexoses and pentoses into ethanol. When fermentations of pure sugars and a pentose-rich sugarcane bagasse hydrolysate were carried out in a packed bed reactor with immobilized cells of C. boliviensis, more than 98% of substrates were converted. Ethanol yields of 0.40-0.46 g/g of sugar were obtained when sugarcane bagasse hydrolysate was fermented. These features reveal interesting properties of C. boliviensis in producing ethanol from a renewable feedstock.     

Scale-up study of oxalic acid pretreatment of agricultural lignocellulosic biomass for the production of bioethanol

Building on our laboratory-scale optimization, oxalic acid was used to pretreat corncobs on the pilot-scale. The hydrolysate obtained after washing the pretreated biomass contained 32.55 g/l of xylose, 2.74 g/l of glucose and low concentrations of inhibitors. Ethanol production, using Scheffersomyces stipitis, from this hydrolysate was 10.3 g/l, which approached the predicted value of 11.9 g/l. Diafiltration using a membrane system effectively reduced acetic acid in the hydrolysate, which increased the fermentation rate. The hemicellulose content of the recovered solids decreased from 27.86% before pretreatment to only 6.76% after pretreatment. Most of the cellulose remained in the pretreated biomass. The highest ethanol production after simultaneous saccharification and fermentation (SSF) of washed biomass with S. stipitis was 21.1 g/l.     

Efficient oleaginous yeasts for lipid production from lignocellulosic sugars and effects of lignocellulose degradation compounds on growth and lipid production

Microbial lipid production using lignocellulosic biomass is considered an alternative for biodiesel production. In this study, 418 yeast strains were screened to find efficient oleaginous yeasts which accumulated large quantities of lipid when cultivated in lignocellulosic sugars. Preliminary screening by Nile red staining revealed that 142 strains contained many or large lipid bodies. These strains were selected for quantitative analysis of lipid accumulation by shaking flask cultivation in nitrogen-limited medium II containing 70 g/L glucose or xylose or mixture of glucose and xylose in a ratio of 2:1. Rhodosporidium fluviale DMKU-SP314 produced the highest lipid concentration of 7.9 g/L when cultivated in the mixture of glucose and xylose after 9 days of cultivation, which was 55.0% of dry biomass (14.3 g/L). The main composition of fatty acids were oleic acid (40.2%), palmitic acid (25.2%), linoleic acid (17.9%) and stearic acid (11.1%). Moreover, the strain DMKU-SP314 could grow and produce lipid in a medium containing predominantly lignocellulose degradation products, namely, acetic acid, formic acid, furfural, 5-hydroxymethylfurfural (5-HMF) and vanillin, with however, some inhibitory effects. This strain showed high tolerance to acetic acid, 5-HMF and vanillin. Therefore, R. fluviale DMKU-SP314 is a promising strain for lipid production from lignocellulosic hydrolysate.     

Effect of lignocellulose degradation products on microbial biomass and lipid production by the oleaginous yeast Cryptococcus curvatus

This work investigated effects of lignocellulose degradation products on cell biomass and lipid production by Cryptococcus curvatus. Furfural was found to have the strongest inhibitory effect. For the three phenolic compounds tested, vanillin was the most toxic, while PHB and syringaldehyde showed comparable inhibitions in the concentration range of 0–1.0 g/L. Generally little significant differences on the relative cell biomass and lipid contents at the same concentrations of tested compounds were observed between glucose and xylose as a sole carbon source. At 1.0 g/L of furfural, the cell biomass and lipid content decreased by 78.4% and 61.0% for glucose as well as 72.0% and 59.3% for xylose, respectively. C. curvatus ceased to grow at concentrations of PHB over 1.0 g/L or vanillin over 1.5 g/L. The strain could survive in the presence of syringaldehyde up to 2.0 g/L for glucose or 1.5 g/L for xylose. The compounds’ negative impact was reduced by an increase in inoculum size and a 10% (v/v) seed was detected to be optimal for cell biomass and lipid production. The results demonstrated C. curvatus could effectively utilize most of the dominant monosaccharides and cellobiose existing in lignocellulosic biomass hydrolysate in the presence of toxic compounds.     

Supercritical carbon dioxide pretreatment of corn stover and switchgrass for lignocellulosic ethanol production

Supercritical CO₂ (SC-CO₂), a green solvent suitable for a mobile lignocellulosic biomass processor, was used to pretreat corn stover and switchgrass at various temperatures and pressures. The CO₂ pressure was released as quickly as possible by opening a quick release valve during the pretreatment. The biomass was hydrolyzed after pretreatment using cellulase combined with β-glucosidase. The hydrolysate was analyzed for the amount of glucose released. Glucose yields from corn stover samples pretreated with SC-CO₂ were higher than the untreated sample’s 12% glucose yield (12 g/100 g dry biomass) and the highest glucose yield of 30% was achieved with SC-CO₂ pretreatment at 3500 psi and 150 °C for 60 min. The pretreatment method showed very limited improvement (14% vs. 12%) in glucose yield for switchgrass. X-ray diffraction results indicated no change in crystallinity of the SC-CO₂ treated corn stover when compared to the untreated, while SEM images showed an increase in surface area.     

Process and technoeconomic analysis of leading pretreatment technologies for lignocellulosic ethanol production using switchgrass

Six biomass pretreatment processes to convert switchgrass to fermentable sugars and ultimately to cellulosic ethanol are compared on a consistent basis in this technoeconomic analysis. The six pretreatment processes are ammonia fiber expansion (AFEX), dilute acid (DA), lime, liquid hot water (LHW), soaking in aqueous ammonia (SAA), and sulfur dioxide-impregnated steam explosion (SO(2)). Each pretreatment process is modeled in the framework of an existing biochemical design model so that systematic variations of process-related changes are consistently captured. The pretreatment area process design and simulation are based on the research data generated within the Biomass Refining Consortium for Applied Fundamentals and Innovation (CAFI) 3 project. Overall ethanol production, total capital investment, and minimum ethanol selling price (MESP) are reported along with selected sensitivity analysis. The results show limited differentiation between the projected economic performances of the pretreatment options, except for processes that exhibit significantly lower monomer sugar and resulting ethanol yields.     

Time dependent degradation of mixture of structurally different azo and non azo dyes by using Galactomyces geotrichum MTCC 1360

Galactomyces geotrichum MTCC 1360, a yeast species showed 88% ADMI (American dye manufacturing institute) removal of mixture of structurally different dyes (Remazol red, Golden yellow HER, Rubine GFL, Scarlet RR, Methyl red, Brown 3 REL, Brilliant blue) (70 mg l⁻¹) within 24 h at 30 °C and pH 7.0 under shaking condition (120 rpm). Glucose (0.5%) as a carbon source was found to be more effective than other sources used. The medium with metal salt (CaCl₂, ZnSO₄, FeCl₃, MgCl₂, CuSO₄) (0.5 mM) showed less ADMI removal as compared to control, but did not inhibit complete decolorization. The presence of tyrosinase, NADH-DCIP reductase and induction in laccase activity during decolorization indicated their role in degradation. HPTLC (High performance thin layer chromatography) analysis revealed the removal of individual dyes at different time intervals from dye mixture, indicating preferential degradation of dyes. FTIR (Fourier transform infrared spectroscopy) and HPLC (High performance liquid chromatography) analysis of samples before and after decolorization confirmed the biotransformation of dye. The reduction of COD (Chemical oxygen demand) (69%), TOC (Total organic carbon) (43%), and phytotoxicity study indicated the conversion of complex dye molecules into simpler oxidizable products having less toxic nature.     

Recycle of cellulases and the use of lignocellulosic residue for enzyme production after hydrolysis of steam-pretreated aspenwood

Summary Various modes of substrate and enzyme addition were used to hydrolyze a 10% concentration (w/v) of steam-exploded, water-and-alkali extracted aspenwood withTrichoderma harzianum E58 cellulases. Although cellulose conversion was high (94–100%), enzyme recovery was low in all cases. Low enzyme recovery was due to a combination of thermal inactivation and adsorption of the cellulases onto the lignocellulosic residue. Enzyme recycle was not feasible as the activity of the recovered cellulases towards crystalline cellulose was low. However, the residual material from enzyme hydrolysis was a suitable carbon source for cellulase enzyme production byT. harzianum based on enzyme yield and hydrolytic potential. These residues could only be used up to a 1% substrate concentration, since at higher substrate loadings cellulase production was reduced, likely because of lignin inhibitors.     

Effect of culturing processes and copper addition on laccase production by the white-rot fungus Fomes fomentarius MUCL 35117

Aim:  To produce high laccase activities from the white-rot fungus Fomes fomentarius .
Methods and Results:  Different culturing methods, viz, cell immobilization on stainless steel sponges and plastic material and solid-state fermentation (SSF) using wheat bran as substrate were used for laccase production by the white-rot fungus F. fomentarius . The SSF study expresses the highest laccase activities, nearly to 6400 U l⁻¹ after 13 days of laboratory flasks cultivation. When the wheat bran medium was supplemented with 2 mmol l⁻¹ copper sulfate, laccase activity increased by threefold in comparison to control cultures, reaching 27 864 U l⁻¹. With the medium thus optimized, further experiments were performed in a 3 l fixed-bed bioreactor (working volume 1·5 l) leading to a laccase activity of about 6230 U l⁻¹ on day 13.
Conclusions:  The results obtained clearly showed the superiority of wheat bran for laccase production over stainless steel sponges and plastic material. Supplementing the wheat bran solid medium with 2 mmol l⁻¹ copper sulfate allowed obtaining high activities at flask scale. The system was scaled to fixed-bed laboratory reactor.
Significance and Impact of the Study:  The high enzyme production along with the low-cost of the substrate, showed the suitability of the system F. fomentarius – SSF for industrial purposes.     

Purification of pyranose oxidase from the white rot fungus Irpex lacteus and its cooperation with laccase in lignin degradation

Laccase and peroxidases mainly cause polymerization of lignin in vitro due to the random coupling of the phenoxy radicals or quinoid intermediates. White rot fungi may avoid polymerization in vivo by reduction of these intermediates. Pyranose oxidase is suggested to play such a role based on its quinone-reducing activity, but direct evidence has been lacking. In this study, a pyranose oxidase was purified from the white rot fungus Irpex lacteus and partially characterized. The enzyme is composed of four subunits of 71 kDa as determined by SDS-PAGE. It exhibits maximum activity at pH 6.5 and 55 °C and is rather stable. d-glucose is the preferred substrate, but d-galactose, l-sorbose and d-xylose are also readily oxidized. In addition to O₂, the enzyme can also transfer electrons to various quinones and the ABTS [2,2′-azinobis(3-ethylbenzthiazoline-6-sulfonic acid)] cation radical. Laccase-generated quinoids are also reduced by the enzyme. Four different technical lignins were treated with laccase with and without pyranose oxidase. Subsequent gel permeation chromatography analysis demonstrated that the pyranose oxidase efficiently inhibited the polymerization of lignin caused by laccase and even brought about degradation.     

Enzymatic and spectroscopic studies on the activation or inhibition effects by substituted phenolic compounds in the oxidation of aryldiamines and catechols catalyzed by Rhus vernicifera laccase

The effect of various phenolic compounds on the activity of Rhus vernicifera laccase (Lc) has been evaluated using two different substrates, N,N-dimethyl-p-phenylenediamine and p-tert-butylcatechol. The observed effect strongly depends on the phenol employed and involves either a moderate activation, by halophenols, or inhibition, by acidic phenols. The collective data are consistent with an open active site in Lc, which is capable of accommodating more than one substrate or phenol molecule. According to NMR relaxation experiments, a phenol molecule binds at an average distance from type 1 Cu of about 6 Å, while evidence from electron paramagnetic resonance (EPR) experiments shows that binding of another phenol molecule induces a change, and probably occurs close to, the type 2/type 3 cluster. The effect of phenolic compounds on Lc reactivity is related to a modification of the substrate affinity for the enzyme. This affinity can either be increased, probably through π-stacking or other types of interactions, or decreased, due to competition for the same site. In addition, the alteration induced in the trinuclear copper cluster has a marked effect on the enzyme reactivity. The inhibition observed with acidic phenols is probably due to the protonation of an enzyme intermediate produced at the trinuclear site, e.g. the peroxy intermediate, that causes the release of hydrogen peroxide and prevents the reaction of this intermediate with the substrate.