Kinetic modeling of brewery's spent grain autohydrolysis

Isothermal autohydrolysis treatments of brewery's spent grain were used as a method for hemicellulose solubilization and xylo-oligosaccharides production. The time course of the concentrations of residual hemicelluloses (made up of xylan and arabinan) and reaction products were determined in experiments carried out at temperatures in the range from 150 to 190 degrees C using liquid-to-solid ratios of 8 and 10 g/g. To model the experimental findings concerning to brewery's spent grain autohydrolysis several kinetic models based on sequential pseudo-homogeneous first-order reactions were tested. Xylan and arabinan were assumed to yield oligosaccharides, monosaccharides (xylose or arabinose), furfural, and other decomposition products in consecutive reaction steps. The models proposed provide a satisfactory interpretation of the hydrolytic conversion of xylan and arabinan. An additional model merging the two proposed models for xylan and arabinan degradation assuming that furfural was formed from both pentoses was developed and the results obtained are discussed. The dependence of the calculated kinetic coefficients on temperature was established using Arrhenius-type equations.     

Valorisation of a leguminous specie, Sesbania grandiflora, by means of hydrothermal fractionation

For the purpose of hydrolysing hemicelluloses to oligomers and monomers, Sesbania grandiflora samples were subjected to isothermal autohydrolysis in the temperatures ranging from 145 °C to 190 °C, using a solid to liquid ratio of 8 and reaction times up to 7.5 h. Kinetic models based on sequential pseudo-homogeneous first order Kinetics with Arrhenius type temperature dependence were employed for describing the time course of the main hemicelluloses compounds and their degradation products. The hydrothermal treatment results show that Sesbania grandiflora can be employed as an alternative raw material for the production of XOS leading to high concentrations of XOS (14.1 g/L in the experiment carried out at 190 °C and 0.1 h) and xylan to XOS conversion (62.6% in the experiment carried out at 190 °C and 6 min). The model proposed provides a satisfactory interpretation of the experimental data obtained in the hydrothermal treatments of this study.     

Biohydrogen production from cellulosic hydrolysate produced via temperature-shift-enhanced bacterial cellulose hydrolysis

A “temperature-shift” strategy was developed to improve reducing sugar production from bacterial hydrolysis of cellulosic materials. In this strategy, production of cellulolytic enzymes with Cellulomonas uda E3-01 was promoted at a preferable temperature (35 °C), while more efficient enzymatic cellulose hydrolysis was achieved under an elevated culture temperature (45 °C), at which cell growth was inhibited to avoid consumption of reducing sugar. This temperature-shift strategy was shown to markedly increase the reducing sugar (especially, monosaccharide and disaccharide) concentration in the hydrolysate while hydrolyzing pure (carboxymethyl-cellulose, xylan, avicel and cellobiose) and natural (rice husk, rice straw, bagasse and Napier-grass) cellulosic materials. The cellulosic hydrolysates from CMC and xylan were successfully converted to H₂ via dark fermentation with Clostridium butyricum CGS5, attaining a maximum hydrogen yield of 4.79 mmol H₂/g reducing sugar.     

Methane fermentation of xylan by mesophilic and thermophilic methane sludges

The degradation of xylan during methane fermentation proceeded as a first-order reaction. The rate constants were calculated to be 0.40–0.09 day^–1 at 37° C and 0.341 day^–1 at 55° C. From calculations based on the experimental data, K _A and C _A values in the expression of the velocity of xylose consumption changed as the fermentation progressed. In the mesophilic fermentation, the degradation of xylan slowed down after 2 days of incubation, but the rate of consumption of xylose increased between days 3 and 4 of incubation and slow again at the 5th day of incubation. In the thermophilic fermentation, the degradation of xylan proceeded at a constant rate and the rate of consumption of xylose increased slightly on the 3rd day of incubation. When the velocity of gas evolution was determined, the C _G value for acetate at 55° C was about 1.8 times larger than the value at 37° C.     

Production of xylanase and β-xylosidase from autohydrolysis liquor of corncob using two fungal strains

Agroindustrial residues are materials often rich in cellulose and hemicellulose. The use of these substrates for the microbial production of enzymes of industrial interest is mainly due to their high availability associated with their low cost. In this work, corncob (CCs) particles decomposed to soluble compounds (liquor) were incorporated in the microbial growth medium through autohydrolysis, as a strategy to increase and undervalue xylanase and β-xylosidase production by Aspergillus terricola and Aspergillus ochraceus. The CCs autohydrolysis liquor produced at 200 °C for 5, 15, 30 or 50 min was used as the sole carbon source or associated with untreated CC. The best condition for enzyme synthesis was observed with CCs submitted to 30 min of autohydrolysis. The enzymatic production with untreated CCs plus CC liquor was higher than with birchwood xylan for both microorganisms. A. terricola produced 750 total U of xylanase (144 h cultivation) and 30 total U of β-xylosidase (96-168 h) with 0.75% untreated CCs and 6% CCs liquor, against 650 total U of xylanase and 2 total U of β-xylosidase in xylan; A. ochraceus produced 605 total U of xylanase and 56 total U of β-xylosidase (168 h cultivation) with 1% untreated CCs and 10% CCs liquor against 400 total U of xylanase and 38 total U of β-xylosidase in xylan. These results indicate that the treatment of agroindustrial wastes through autohydrolysis can be a viable strategy in the production of high levels of xylanolytic enzymes.     

Electrochemistry of some substituted pteridines

Some substituted 4(3H)-pteridones have been investigated by classical polarography, cyclic voltammetry, and controlled potential electrolysis; based on these results, the following reaction path for substituted 2-amino-4(3H)-pteridones seems likely. In neutral and slightly alkaline solution the first step is a reversible two-electron reduction to the unreducible 5,8-dihydro derivative, which tautomerizes into a reducible 7,8-dihydropteridone at a rate depending on the substituents. At a more negative potential the 7,8-dihydro derivative is reduced in a two-electron reaction to the unreducible 5,6,7,8-tetrahydropteridone. This compound can be oxidized in a reversible reaction to a 6,7-dihydropteridone, a “quinonoid” form, which tautomerizes into the 7,8-dihydropteridone. The data from cyclic voltammetry favour the formulation of the “quinonoid” form as the 6,7-dihydropteridone, an “o-quinonoid” structure.     

Simulation and optimization of batch autohydrolysis of wheat straw to monosaccharides and oligosaccharides

Twenty-four non-isothermal wheat straw autohydrolysis experiments were performed in a batch reactor in order to support the development of a new kinetic model. An optimum of 76% w/w total xylose was obtained due to 5% w/w xylose degradation at 180 °C for 70 min. An optimum of 31% w/w total glucose was obtained due to 22% w/w glucose degradation at 240 °C for 82 min. The autohydrolysis of cellulose and hemicelluloses was simulated using a new kinetic model, in which a new phenomenological first-order reaction was introduced to take into account the increasing concentration of acids that are produced during the complex cascade of reactions. The new model simulated experimental results more accurately than the severity factor (R0) model.     

A comparison of liquid hot water and steam pretreatments of sugar cane bagasse for bioconversion to ethanol.

Sugar cane bagasse was pretreated with either liquid hot water (LHW) or steam using the same 25 l reactor. Solids concentration ranged from 1% to 8% for LHW pretreatment and was > or = 50% for steam pretreatment. Reaction temperature and time ranged from 170 to 230 degrees C and 1 to 46 min, respectively. Key performance metrics included fiber reactivity, xylan recovery, and the extent to which pretreatment hydrolyzate inhibited glucose fermentation. In four cases, LHW pretreatment achieved > or = 80% conversion by simultaneous saccharification and fermentation (SSF). > or = 80% xylan recovery, and no hydrolyzate inhibition of glucose fermentation yield. Combined effectiveness was not as good for steam pretreatment due to low xylan recovery. SSF conversion increased and xylan recovery decreased as xylan dissolution increased for both modes. SSF conversion, xylan dissolution. hydrolyzate furfural concentration, and hydrolyzate inhibition increased, while xylan recovery and hydrolyzate pH decreased, as a function of increasing LHW pretreatment solids concentration (1-8%). These results are consistent with the notion that autohydrolysis plays an important. if not exclusive, role in batch hydrothermal pretreatment. Achieving concurrently high (greater than 90%) SSF conversion and xylan recovery will likely require a modified reactor configuration (e.g. continuous percolation or base addition) that better preserves dissolved xylan.     

Production of xylooligosaccharides from enzymatic hydrolysis of xylan by the white-rot fungi Pleurotus

The white-rot fungi basidiomycetes Pleurotus sp. BCCB068 and Pleurotus tailandia were used to degrade oat-spelt xylan under submerged fermentation over a period of 40 days. Activities of endo-1,4-β-xylanase and β-xylosidase and xylan degradation products were determined. Xylan degradation by Pleurotus sp. BCCB068 and P. tailandia reached 75.1% and 73.4%, respectively. The formation of xylooligosaccharides and the simple sugars xylose, arabinose, cellobiose, mannose, and maltose were observed for both strains. The xylan degradation exhibited by these Pleurotus strains indicates they have potential for use in biotechnological processes related to degradation of hemicellulose sources.     

Kinetic study of hydrolysis of xylan and agricultural wastes with hot liquid water

We investigated the kinetics of hot liquid water (HLW) hydrolysis over a 60-min period using a self-designed setup. The reaction was performed within the range 160–220 °C, under reaction conditions of 4.0 MPa, a 1:20 solid:liquid ratio (g/mL), at 500 rpm stirring speed. Xylan was chosen as a model compound for hemicelluloses, and two kinds of agricultural wastes–rice straw and palm shell–were used as typical feedstocks representative of herbaceous and woody biomasses, respectively. The hydrolysis reactions for the three kinds of materials followed a first-order sequential kinetic model, and the hydrolysis activation energies were 65.58 kJ/mol for xylan, 68.76 kJ/mol for rice straw, and 95.19 kJ/mol for palm shell. The activation energies of sugar degradation were 147.21 kJ/mol for xylan, 47.08 kJ/mol for rice straw and 79.74 kJ/mol for palm shell. These differences may be due to differences in the composition and construction of the three kinds of materials. In order to reduce the decomposition of sugars, the hydrolysis time of biomasses such as rice straw and palm shell should be strictly controlled.     

Kinetics of polysaccharide degradation during ethanol–alkali delignification of giant reed—Part 1. Cellulose and xylan

The degradation kinetics of the principal polysaccharides (cellulose and xylan) of the agro-fibre crop Arundo donax L. (giant reed) during ethanol–alkali delignification is reported. Based on the properties of a multi-component reaction system, the degradation kinetics of both polysaccharides was accurately described in terms of two simultaneous irreversible first-order reactions corresponding to removal of two kinetically homogeneous fractions. The moderate cellulose losses during pulping (about 4.5%) result mainly from the removal of the more reactive cellulose fraction, that accounted for 4% of initial cellulose. The bulk of the cellulose (96%) degrades slowly with three orders lower rate with pulping progress. The apparent activation energy of cellulose fractions degradation was estimated as 105.2 and 106.5 kJ mol⁻¹, respectively. Substantial loss of xylan during pulping (about 55%, as a homoxylan) is caused by fast removal of the first very reactive fraction, covering about 48% of total xylan. The degradation rate of the second xylan fraction is only one order higher of the bulk cellulose degradation. The activation energy of xylan fractions degradation was found as 74.4 and 140.9 kJ mol⁻¹, respectively.     

Synthesis and Enantioseparation Ability of Xylan Bisphenylcarbamate Derivatives as Chiral Stationary Phases in HPLC

Ten novel xylan bisphenylcarbamate derivatives bearing meta‐ and para‐substituents on their phenyl groups were synthesized and their chiral recognition abilities were evaluated as the chiral stationary phases (CSPs) for high‐performance liquid chromatography (HPLC) after coating them on macroporous silica. The chiral recognition abilities of these CSPs depended on the nature, position, and number of the substituents on the phenyl moieties. The introduction of an electron‐donating group was more attractive than an electron‐withdrawing group to improve the chiral recognition ability of the xylan phenylcarbamate derivatives. Among the CSPs discussed in this study, xylan bis(3,5‐dimethylphenylcarbamate)‐based CSP seems to possess the highest resolving power for many racemates, and the meta‐substituted CSPs showed relatively better chiral recognition than the para‐substituted ones. For some racemates, the xylan bis(3,5‐dimethylphenylcarbamate) derivative exhibited higher enantioselectivity than the CSP based on cellulose tris(3,5‐dimethylphenylcarbamate). Chirality 27:518–522, 2015 © 2015 Wiley Periodicals, Inc.     

Selectivity and delignification kinetics for oxidative and nonoxidative lime pretreatment of poplar wood, part III: long-term

Lime pretreatment is an effective method for improving lignocellulose digestibility by removing lignin. For several weeks, mixtures of poplar wood, water, and calcium hydroxide (lime) were submitted to temperatures from 25 to 65°C, with and without aeration. Kinetic models for lignin and carbohydrate degradation were obtained as functions of temperature, time, and aeration using first-order kinetics in lignin and carbohydrates. Model 1 considered two reacting moieties (slow and fast), and Model 2 considered three (slow, medium, and fast). Model 1 was statistically better and was employed to determine differential and integral selectivities, which measure the ability of pretreatment to retain carbohydrates while removing lignin. During the first 2 weeks, when lignin content ≥ 0.80 g/g lignin in raw biomass, both glucan and xylan differential and integral selectivities decreased rapidly. Afterwards, selectivities were nearly constant ranging between 0 and 3 g lignin removed/g carbohydrate degraded.     

Inhibition of ethanol-producing yeast and bacteria by degradation products produced during pre-treatment of biomass

An overview of the different inhibitors formed by pre-treatment of lignocellulosic materials and their inhibition of ethanol production in yeast and bacteria is given. Different high temperature physical pre-treatment methods are available to render the carbohydrates in lignocellulose accessible for ethanol fermentation. The resulting hydrolyzsates contain substances inhibitory to fermentation—depending on both the raw material (biomass) and the pre-treatment applied. An overview of the inhibitory effect on ethanol production by yeast and bacteria is presented. Apart from furans formed by sugar degradation, phenol monomers from lignin degradation are important co-factors in hydrolysate inhibition, and inhibitory effects of these aromatic compounds on different ethanol producing microorganisms is reviewed. The furans and phenols generally inhibited growth and ethanol production rate (Q_EtOH) but not the ethanol yields (Y_EtOH) in Saccharomyces cerevisiae. Within the same phenol functional group (aldehyde, ketone, and acid) the inhibition of volumetric ethanol productivity was found to depend on the amount of methoxyl substituents and hence hydrophobicity (log P). Many pentose-utilizing strains Escherichia coli, Pichia stipititis, and Zymomonas mobilis produce ethanol in concentrated hemicellulose liquors but detoxification by overliming is needed. Thermoanaerobacter mathranii A3M3 can grow on pentoses and produce ethanol in hydrolysate without any need for detoxification.     

Effect of alkaline and autohydrolysis processes on the purity of obtained hemicelluloses from corn stalks

A study of the potential of autohydrolysis and alkaline extraction processes from corn stalks was performed for high purity hemicellulose extraction. The influence of process parameters on the purity of obtained hemicelluloses was analyzed. An experimental design was developed for the autohydrolysis treatments to determine the optimal conditions to solubilize the hemicelluloses with lowest content in contaminants. On the other hand, alkaline extraction, including raw material pretreatment (dewaxing and delignification step) was carried out analyzing the effectiveness of this processes for maximum pure hemicellulose recovery. The maximum yield (54% of the raw material hemicelluloses) and the best physicochemical properties (highest hemicellulose content free of lignin) were obtained with these pretreatments in alkaline extraction. Moreover, the effect of lignin removal by sulfuric acid from the autohydrolysis liquors before hemicellulose precipitation was studied. This purification step has allowed to obtain lignin-free autohydrolysis hemicellulose but with the presence of sulfur as predominant contaminant.     

Different conversion metabolic rates of testosterone are associated to hormone-sensitive status and -response of human prostate cancer cells

The main goal of the present work was to compare the ability of human prostate cancer (PCa) cells to metabolize testosterone (T) in living conditions. To this end we studied three different human PCa cell lines (LNCaP, DU145 and PC3) having different hormone-sensitive status and capability of response to androgens. We used an original approach which allows the evaluation of conversion metabolic rates in growing cells after administration of labeled steroid precursor (presently T), at physiological concentrations (1–10 nM). Analysis of both precursor degradation and formation of several products was carried out using reverse phase-high performance liquid chromatography (RP-HPLC) and “on line” radioactive detection. Comparison of the three human PCa cells revealed that their metabolic aptitude differed in many respects: (i) rates of precursor degradation, (ii) different products' formation, and (iii) extent of conjugate production. In detail, PC3 cells quickly degraded T and exhibited high formation rates of androstenedione (A-4-ene-Ad); both DU145 and LNCaP cells mostly retained high levels of unconverted T, with a limited production of A-4-ene-Ad and its 17-keto derivatives (if any). Either LNCaP or DU145 cells generated a relatively high amount of dihydrotestosterone (DHT). In contrast, neither DHT nor its main metabolites were detected in PC3 cells at both short and longer incubation times. As expected, T degradation and A-4-ene-Ad production were highly correlated (r = 0.97; P < 0.03); similarly, A-4-ene-Ad and DHT formation showed a negative, significant correlation. Negligible production of conjugates was noted in both PC3 and DU145 cells, whilst it was remarkable in LNCaP cells (ranging from 43 to 57%). Overall, our data indicate that human PCa cells degrade T quite differently, favoring alternatively reductive or oxidative patterns of androgen metabolism.     

Cytoplasmic peptide:N-glycanase and catabolic pathway for free N-glycans in the cytosol

Peptide:N-glycanase (PNGase) releases N-glycans from glycoproteins/glycopeptides. Cytoplasmic PNGase is widely recognized as a component of machinery for ER-associated degradation (ERAD), i.e. proteasomal degradation of misfolded, newly synthesized (glyco)proteins that have been exported from the ER. The enzyme belongs to the “transglutaminase superfamily” that contains a putative catalytic triad of cysteine, histidine, and aspartic acid. The mammalian orthologues of PNGase contain the N-terminal PUB domain that serves as the protein–protein interaction domain. The C-terminus of PNGase was recently found to be a novel carbohydrate-binding domain. Taken together, these observations indicate that C-terminus of mammalian PNGase is important for recognition of the substrates while N-terminus of this enzyme is involved in assembly of a degradation complex.     

Phospholipid regulation of a cyclic AMP-specific phosphodiesterase (PDE4) from U937 cells

The regulation of phosphodiesterase-4 (PDE4) by various phospholipids was explored using PDE4s partially purified from U937 cells. Preincubation (5 min, 4°C) of the large molecular weight PDE4 denoted “Peak 2 PDE4” with mixed phosphatidic acids (PAs) produced a 2-fold increase in its V_max without changing its K_m ( 2 μM) for cyclic AMP. This “activation” was not limited to PAs with specific fatty acid substituents: Synthetic PAs containing saturated and/or unsaturated fatty acids 16-20 carbons long produced similar effects. Lysophosphatidic acids (LPAs) and phosphatidylserines (PSs) also induced PDE4 activation, whereas phosphatidylcholines (PCs), phosphatidylethanolamines (PEs) and diacylglycerol did not. Antibodies to a peptide region near the PDE4 catalytic site specifically inhibited PA-induced activation. The data demonstrate that anionic phospholipids can act as non-essential activators of a leukocyte PDE4, and suggest biochemical crosstalk between phospholipid-dependent and cyclic AMP-dependent signalling pathways in human leukocytes.     

Advantages of isothermal titration calorimetry for xylanase kinetics in comparison to chemical-reducing-end assays

In lignocellulosic raw materials for biomass conversion, hemicelluloses constitute a substantial fraction, with xylan being the primary part. Although many pretreatments reduce the amount or change the distribution of xylan, it is important to degrade residual xylan so as to improve the overall yield. Typically, xylanase reaction rates are measured in stopped assays by chemical quantification of the reducing ends. With isothermal titration calorimetry (ITC), the heat flow of the hydrolysis can be measured in continuous fashion, with the reaction rate being directly proportional to the heat flow. Reaction enthalpies for carbohydrate hydrolysis are typically below 5 kJ/mol, which is the limiting factor for straight forward calorimetric quantification of enzymatic reaction rates using current ITC technology. To increase the apparent reaction enthalpy, we employed a subsequent oxidation of hydrolysis products by carbohydrate oxidase and catalase. Here we show that the coupled assay with carbohydrate oxidase and catalase can be used to measure enzyme kinetics of a GH10 xylanase from Aspergillus aculeatus on birch xylan and wheat arabinoxylan. Results are discussed in the light of a critical analysis of the sensitivity of four chemical-reducing-end quantification methods using well-characterized substrates.