An ultrafiltration membrane reactor for obtaining experimental reaction rates at defined concentrations of inhibiting sugars during enzymatic saccharification of alkali-pretreated sallow: Formulation of a simple empirical rate equation

The kinetics of the enzymatic hydrolysis of sodium hydroxide-pretreated sallow were studied in an ultrafiltration membrane reactor in the presence of different concentrations of glucose. In the UF membrane reactor low-molecular-weight products were continuously removed at a low dilution rate and replaced by a buffer solution that contained different concentrations of glucose, which made it possible to keep the inhibiting product concentration constant throughout an experiment. The reaction rate was related to the degree of substrate conversion and a mathematical relationship was formulated that describes the influence of the product concentration on the rate coefficient.     

Reactor design for minimizing product inhibition during enzymatic lignocellulose hydrolysis: II. Quantification of inhibition and suitability of membrane reactors

Product inhibition of cellulolytic enzymes affects the efficiency of the biocatalytic conversion of lignocellulosic biomass to ethanol and other valuable products. New strategies that focus on reactor designs encompassing product removal, notably glucose removal, during enzymatic cellulose conversion are required for alleviation of glucose product inhibition. Supported by numerous calculations this review assesses the quantitative aspects of glucose product inhibition on enzyme-catalyzed cellulose degradation rates. The significance of glucose product inhibition on dimensioning of different ideal reactor types, i.e. batch, continuous stirred, and plug-flow, is illustrated quantitatively by modeling different extents of cellulose conversion at different reaction conditions. The main operational challenges of membrane reactors for lignocellulose conversion are highlighted. Key membrane reactor features, including system set-up, dilution rate, glucose output profile, and the problem of cellobiose are examined to illustrate the quantitative significance of the glucose product inhibition and the total glucose concentration on the cellulolytic conversion rate. Comprehensive overviews of the available literature data for glucose removal by membranes and for cellulose enzyme stability in membrane reactors are given. The treatise clearly shows that membrane reactors allowing continuous, complete, glucose removal during enzymatic cellulose hydrolysis, can provide for both higher cellulose hydrolysis rates and higher enzyme usage efficiency (kg_product/kg_enzyme). Current membrane reactor designs are however not feasible for large scale operations. The report emphasizes that the industrial realization of cellulosic ethanol requires more focus on the operational feasibility within the different hydrolysis reactor designs, notably for membrane reactors, to achieve efficient enzyme-catalyzed cellulose degradation.     

Poly(vinyl alcohol) Ultrafiltration Membranes: Synthesis,Characterization, the Use for Enzyme Immobilization

An enzymatic hydrolysis in a symmetric membrane, combining reaction and separation, has been studied. PVA hydrogel was chosen because of its hydrophilicity expecting to minimize membrane fouling and concentration polarization. The membrane pores containing covalently bound enzymes serve as catalyst support. The membrane immobilization of the enzyme and the filtration mode of operating the process were chosen in order to avoid product inhibition of the enzyme. The properties of cross‐linked PVA hydrogel were investigated. The conversion of the hydrolysis of p‐nitrophenyllaurate with two different loadings of Cr lipase was evaluated. The conversion of the reaction decreased with both increasing substrate flux and initial concentration. The kinetic parameters were obtained. Compared to the free lipase, the K_m of the membrane bonded enzyme was lower and its R_max approximately the same.     

Continuous enzymatic cellulose hydrolysis in a tubular membrane bioreactor

Cellulose hydrolysis by Celluclast 1.5L (Novozymes A/S, Denmark) enzyme preparation was studied in a special tubular membrane reactor, where a porous stainless steel filter was covered by a non-woven technical textile layer providing a fine, hairy surface for simultaneous adsorption of both the cellulose particles and the biocatalyst. Solka Floc BW 200 powder and Mavicell pellets were used as substrates in the process. Beyond the adsorption studies, the composite membrane was characterized, having 30 l/m² bar h hydraulic permeability and an ability to retain both cellulose and enzyme, while glucose (product) permeated easily across the membrane. Using Solka Floc substrate experiments were carried out in both the hairy tubular and a “normal” flat sheet membrane bioreactor. It was found that 10% higher average conversion was possible to achieve in the special layered tubular unit compared to the “traditional” ultrafiltration membrane reactors. Finally, milled and sieved Mavicell pellets were applied as substrates, and 70% conversion was reached with the pretreated fraction.     

Formation of ribonucleotide 2'',3''-cyclic carbonates during conversion of ribonucleoside 5''-phosphates to diphosphates and triphosphates by the phosphorimidazolidate procedure.

Ribo- and 2'-deoxyribonucleoside 5'-di- or triphosphates are commonly synthesized by reaction of inorganic phosphate or pyrophosphate with phosphorimidazolidates obtained by reaction of nucleoside 5'-phosphates with 1,1'-carbonyldiimidazole. The latter reaction, however, converted UMP, CMP, IMP, GMP, and AMP in high yield to the 2',3'-cyclic carbonate derivatives of their phosphorimidazolidates. Acidic treatment of the product from AMP gave AMP 2',3'-cyclic carbonate dihydrate; this was characterized by its uv, ir, and pmr spectra and by its conversion to adenosine 2',3'-cyclic carbonate by acid phosphatase and to AMP by basic hydrolysis. ADP or ATP synthesized by the phosphorimidazolidate method contained equal or greater amounts of their respective 2',3'-cyclic carbonates. The latter could be quantitatively converted to ADP and ATP, respectively, by 4-hr hydrolysis at pH 10.5, 22 degrees. ADP or ATP can be synthesized without concomitant 2',3'-cyclic carbonate formation by reaction of AMP with phosphorimidazolidates of inorganic phosphate or pyrophosphate.     

Efficiency of lactic acid production by Lactobacillus helveticus in a membrane cell recycle reactor

Abstract: An economic evaluation is presented of lactic acid production in a membrane cell recycle reactor. From this evaluation it is concluded that the economic feasibility of the process is primarily limited by production capacity and product concentration and to a lesser extent by productivity. In membrane cell recycle reactor experiments and batch cultivation experiments with Lactobacillus helreticus , it is shown that the economic feasibility of the process using this organism is limited by organic acid inhibition resulting in energy uncoupling of anabolism and catabolism. Due to this inhibition, the maximum lactic acid concentration that can be obtained in the membrane reactor process is 50 g I^1—. Furthermore it is shown that not only the fermentative conversion of lactose into lactic acid but also the hydrolysis of lactose into glucose and galactose is an important process. The β-galaetosidase activity needed for the hydrolysis is generated during the exponential growth phase of Lb. helveticus     

Enzymatic resolution of (S)-(+)-naproxen in a trapped aqueous-organic solvent biphase continuous reactor

A trapped aqueous-organic biphase system for the continuous production of (S)-(+)-2-(6-methoxy-2-naphthyl) propionic acid (Naproxen) has been developed. The process consists of a stereoselective hydrolysis of the racemic Naproxen methyl ester by Candida rugosa lipase in a trapped aqueous-organic biphase system. The reaction has been carried out in a laboratory-scale continuous-flow stirred tank reactor (CSTR). The staring material has been supplied in and remaining substrate recovered by organic phase. YWG-C(6)H(5), a poorly polar synthetic support, has been employed to immobilize the lipase and to restrict the aqueous phase. Lipase immobilized on YWG-C(6)H(5) containing aqueous phase has been added into the CSTR to catalyze the hydrolysis. A dialysis membrane tube containing a continuous flow closed-loop buffer has been applied in the CSTR for the extraction of product and recruiting of the aqueous part consumed. Various reaction conditions have been studied. The activity of immobilized enzyme was effected by the polarity of support, the substrate concentration, logP value of organic phase and the product inhibition. At steady-state operating conditions, an initial conversion of 35% has been obtained. The CSTR was allowed to operate continuously for 60 days at 30 degrees C with a 30% loss of activity. The hydrolysis reaction yielded (S)-(+)-Naproxen with >90% enantiomeric excess and overall conversion of 30%.     

Substrate reactivity as a function of the extent of reaction in the enzymatic hydrolysis of lignocellulose

In an effort to better understand the role of the substrate in the rapid fall off in the rate of enzymatic hydrolysis of cellulose with conversion, substrate reactivity was measured as a function of conversion. These measurements were made by interrupting the hydrolysis of pretreated wood at various degrees of conversion; and, after boiling and washing, restarting the hydrolysis in fresh buffer with fresh enzyme. The comparison of the restart rate per enzyme adsorbed with the initial rate per enzyme adsorbed, both extrapolated back to zero conversion, provides a measurement of the substrate reactivity without the complications of product inhibition or cellulase inactivation. The results indicate that the substrate reactivity falls only modestly as conversion increases. However, the restart rate is still higher than the rate of the uninterrupted hydrolysis, particularly at high conversion. Hence we conclude that the loss of substrate reactivity is not the principal cause for the long residence time required for complete conversion. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 650-655, 1997.     

The Gibbs-Donnan near-equilibrium system of heart

The gradients of the major inorganic ions across the plasma membrane of heart were examined to determine the factors controlling the extent and direction of the changes induced during injury, certain diseases, and electrolyte disturbances. The ionic environment was altered by changing only the concentration of inorganic phosphate, [sigma Pi]o, from 0 to 1.2 to 5 mM in the Krebs-Henseleit buffer perfusing working rat hearts. Raising [sigma Pi]o from 1.2 to 5 mM resulted in a decrease in total Mg2+ content and calculated free cytosolic [Mg2+] from 0.44 to 0.04 mM, conversion of 4 mmol of MgATP2- to ATP4- and a decrease in measured intracellular [Cl-]i from 41 to 16 mM. At all levels of [sigma Pi]o, both the [Na+]i and [K+]i were invariant at about 3 mM and 130 mM, respectively, as was the energy of hydrolysis of the terminal phosphate bond of sigma ATP, delta GATP Hydr, of -13.2 kcal/mol. The relationship maintained between the ions on both sides of the plasma membrane by the 3Na+/2K(+)transporting ATPase (EC 3.6.1.37) and an open K+ channel was: (formula; see text) The energy of the gradients of the other inorganic ions across the plasma membrane, delta G[ion]o/i, exhibited three distinct quanta of energy derived from the prime quantum of delta GATP Hydr of -13.2 kcal/mol. The second quantum was about one-third of delta GATP Hydr or +/- 4.4 kcal/mol and comprised the delta G[Na+]o/i, delta G[Mg2+]o/i, and delta G[HPO42-]o/i. These results indicated near-equilibrium was achieved by the reactants of the 3Na+/2K(+)-ATPase, the K+ channel, the Na(+)-Pi co-transporter, and a postulated net Mg2+/H2PO4- exchanger. The third quantum was one-third of delta G[Na+]o/i or about +/- 1.5 kcal/mol and comprised delta G[H+]o/i, delta G[HCO3-]o/i, and delta G[Cl-]o/i. The delta G[K+]o/i was 0, indicating near-equilibrium between the chemical energy of [K+]o/i and the E across the plasma membrane of -83 mV. It is concluded that the gradients of the major inorganic ions across the plasma membrane and the potential across that membrane constitute a Gibbs-Donnan equilibrium system catalyzed by transport enzymes sharing common substrates. The chemical and electrical energies of those gradients are equal in magnitude and opposite in sign to the chemical energy of ATP hydrolysis.     

Enhanced enzymatic cellulose degradation by cellobiohydrolases via product removal

Product inhibition by cellobiose decreases the rate of enzymatic cellulose degradation. The optimal reaction conditions for two Emericella (Aspergillus) nidulans-derived cellobiohydrolases I and II produced in Pichia pastoris were identified as CBHI: 52 °C, pH 4.5–6.5, and CBHII: 46 °C, pH 4.8. The optimum in a mixture of the two was 50 °C, pH 4.9. An almost fourfold increase in enzymatic hydrolysis yield was achieved with intermittent product removal of cellobiose with membrane filtration (2 kDa cut-off): The conversion of cotton cellulose after 72 h was ~19 % by weight, whereas the conversion in the parallel batch reaction was only ~5 % by weight. Also, a synergistic effect, achieving ~27 % substrate conversion, was obtained by addition of endo-1,4-β-d-glucanase. The synergistic effect was only obtained with product removal. By using pure, monoactive enzymes, the work illustrates the profound gains achievable by intermittent product removal during cellulose hydrolysis.     

The stereochemical course of phosphoric residue transfer during the myosin ATPase reaction

When adenosine 5'-(3-thiotriphosphate), stereospecifically labeled in the gamma position with 18O, was hydrolyzed in the presence of myosin subfragment 1 in 17O-enriched water, the product inorganic [16O,17O,18O]thiophosphate was chiral. The configuration of this product showed that the hydrolysis proceeds with inversion at the transferred phosphoric residue. This result suggests a direct, in-line hydrolysis mechanism for the ATPase.     

Evaluation of the factors affecting avicel reactivity using multi-stage enzymatic hydrolysis

Multi-stage and single-stage enzymatic hydrolysis of cellulose (Avicel PH-101) were conducted to investigate individual factors that affect the rate-reducing kinetics of enzymatic hydrolysis. Understanding factors affecting enzymatic hydrolysis of Avicel will help improve hydrolysis of various biomasses. Product inhibition, enzyme deactivation, and the changes of substrate are potential factors that can affect the hydrolysis efficiency of Avicel. Multi-stage enzymatic hydrolysis resulted in 36.9% and 25.4% higher carbohydrate conversion as compared to a single-stage enzymatic hydrolysis with an enzyme loading of 5 and 20 FPU/g in a 96 h reaction. However, a decline in carbohydrate conversion of 1.6% and 2.6% was observed through each stage with 5 and 20 FPU/g, respectively. This indicated that the substrate became more recalcitrant as hydrolysis progressed. The decreased reactivity was not due to crystallinity because no significant change in crystallinity was detected by X-ray diffraction. Product inhibition was significant at low enzyme loading, while it was marginal at high enzyme loading. Therefore, product inhibition can only partially explain this decreased conversion. Another important factor, enzyme deactivation, contributed to 20.3% and 25.4% decrease in the total carbohydrate conversion of 96 h hydrolysis with 5 and 20 FPU/g, respectively. This work shows that an important reason for the decreased Avicel digestibility is the effect of enzyme blockage, which refers to the enzymes that irreversibly adsorb on accessible sites of substrate. About 45.3% and 63.2% of the total decreased conversion at the end of the 8th stage with 5 and 20 FPU/g, respectively, was due to the presence of irreversibly adsorbed enzymes. This blockage of active sites by enzymes has been speculated by other researchers, but this article shows further evidence of this effect.     

A mechanistic model for enzymatic saccharification of cellulose using continuous distribution kinetics II: cooperative enzyme action, solution kinetics, and product inhibition

The projected cost for the enzymatic hydrolysis of cellulosic biomass continues to be a barrier for the commercial production of liquid transportation fuels from renewable feedstocks. Predictive models for the kinetics of the enzymatic reactions will enable an improved understanding of current limitations, such as the slow-down of the overall conversion rate, and may point the way for more efficient utilization of the enzymes in order to achieve higher conversion yields. A mechanistically based kinetic model for the enzymatic hydrolysis of cellulose was recently reported in Griggs et al. (2011) (Part I). In this article (Part II), the enzyme system is expanded to include solution-phase kinetics, particularly cellobiose-to-glucose conversion by β-glucosidase (βG), and novel adsorption and product inhibition schemes have been incorporated, based on current structural knowledge of the component enzymes. Model results show cases of cooperative and non-cooperative hydrolysis for an enzyme system consisting of EG(I) and CBH(I). The model is used to explore various potential rate-limiting phenomena, such as substrate accessibility, product inhibition, sterically hindered enzyme adsorption, and the molecular weight of the cellulose substrate.     

Biocatalytic conversion of aloeresin A to aloesin

Leaf exudates from Aloe species, such as the Southern African Aloe ferox, are used in traditional medicines for both humans and livestock. This includes aloesin, a skin bleaching product that inhibits the synthesis of melanin. Aloesin, (a C-glycoside-5-methylchromone) can be released from aloeresin A, an ester of aloesin, through hydrolysis. The objective of the current study was to identify an enzymatic hydrolysis method for converting aloeresin A to aloesin, resulting in increased concentrations of aloesin in the aloe bitters extract. More than 70 commercially available hydrolytic enzymes were screened for the conversion of aloeresin A. An esterase (ESL001-02) from Diversa, a lipase (Novozym 388) and a protease (Aspergillus oryzae) preparation were identified during screening as being capable of providing conversion of pure aloeresin A, with the protease giving the best conversion (~100%). It was found that a contaminating enzyme in Novo 388 was responsible for the conversion of aloeresin A to aloesin. This contaminating enzyme, possibly a protease, was able to give almost complete conversion using crude aloe bitters extract, doubling the concentration of aloesin in aloe bitters extract via the hydrolysis of aloeresin A.     

Mechanistic investigation on the temperature dependence and inhibition of corn root plasma membrane ATPase

The kinetics of corn root plasma membrane-catalyzed Mg-ATP hydrolysis may be satisfactorily described by a simple Michaelis-Menten scheme. It was found that the Km of the process was relatively insensitive to changes in temperature. This property allowed us to conveniently estimate the activation energy of the enzyme turnover process as approximately 14 kcal mol-1 in the temperature range of 10 to 45 degrees C. The enzyme activity was inhibited by the presence of diethystilbestrol (DES), miconazole, vanadate, and dicyclohexylcarbodiimide (DCCD). The inhibition caused by DES and miconazole was strictly uncompetitive and inhibition by vanadate was noncompetitive. The inhibition by DCCD showed a substrate concentration dependence, i.e., competitive at high and uncompetitive at low concentrations of Mg-ATP. The 1/V vs [I] plots suggested that there were different but unique binding sites for DES, vanadate, and miconazole. However, the modification of the plasma membrane by DCCD exhibited interaction with multiple sites. Unlike yeast plasma membrane ATPase, the enzyme of corn root cells was not affected by the treatment with N-ethylmaleimide. Although the enzyme activity was regulated by ADP, a product of the reaction, the presence of inorganic phosphate showed no inhibition to the hydrolysis of Mg-ATP.     

Membrane reactor for enzymatic hydrolysis of cellobiose

A pressurized, stirred vessel attached with an ultrafiltration membrane was used as a membrane reactor, Cellobiose hydrolysis by cellobiase was carried out and theoretically analyzed in terms of steady-state conversion and flow rate through the membrane. When the flow rate exceeds a critical value, a significant fraction of the enzyme inside the reactor is localized in the concentration polarization layer where shear from stirring is high. Consequently, enzyme deactivation inside the concentration polarization layer is accelerated and the conversion decreases due to an exchange of active enzyme in bulk with deactivated enzyme in the polarization layer via convection and back diffusion. Successful operation can be obtained at flow rates lower than the critical point to avoid the polarization and thus the deactivation. It is shown that 6.5 L of 2 mg/mL of cellobiose solution is hydrolyzed to glucose with a conversion of 91% in 20 h with 1.617 mg of cellobiase enzyme, in a reactor attached with a PM 10 membrane of an effective surface area of 39.2 cm².     

5-Oxo-L-prolinase (L-pyroglutamate hydrolase). Studies of the chemical mechanism

Rat kidney 5-oxo-L-prolinase catalyzes the endergonic hydrolysis of 5-oxo-L-proline (L-pyroglutamate, L-2-pyrrolidone-5-carboxylate) to form L-glutamate; the reaction is driven by and dependent on the stoichiometric concomitant hydrolysis of ATP to ADP and inorganic phosphate. The present studies are concerned with the mechanism by which the free energy of ATP hydrolysis is conserved and made available for 5-oxoproline hydrolysis. Studies with 18O-labeled substrates showed that (a) all three oxygen atoms of 5-oxoproline are recovered in the product glutamate, and (b) the two water molecules consumed in the reaction contribute one oxygen atom to inorganic phosphate and one oxygen atom to the gamma-carboxyl group of glutamate. It was shown that the enzyme also catalyzes the intrinsically exergonic hydrolysis of alpha-hydroxyglutarate lactone, a reaction that is ATP-dependent. Intermediates in the 5-oxoprolinase reaction were not detected by exchange experiments with radioactive ADP and phosphate, nor were they trapped by adding hydroxylamine. In the presence of very high glutamate concentrations, a slow reversal of the 5-oxoprolinase reaction was demonstrated by measuring ATP formation. The findings are consistent with a mechanism in which 5-oxo-L-proline is phosphorylated by ATP on the amide carbonyl oxygen and the resulting intermediate is subsequently hydrolyzed to yield gamma-glutamyl phosphate; the latter is hydrolyzed to glutamate and inorganic phosphate.     

Ultrastructural localization of several phosphatases with cerium

Cerium ions have been used as the capture agent for inorganic phosphate released during the enzymatic hydrolysis of phosphate-containing substrates by a variety of phosphatases. Cerium phosphate reaction product accumulation is proportional to the amount of enzyme present in a cell-free model system. Ultrastructurally, cerium phosphate reaction product appears as a very fine electron-dense precipitate. Cerium appears to be a better capture agent for inorganic phosphate than lead in that reaction product is usually more uniform and more consistently reproducible when cerium is used. Furthermore, nonspecific deposits of reaction product that are commonly encountered in lead-based phosphatase reactions are virtually nonexistent when cerium is the capture agent.     

The regulator of the F1 motor: inhibition of rotation of cyanobacterial F1-ATPase by the epsilon subunit

The chloroplast-type F(1) ATPase is the key enzyme of energy conversion in chloroplasts, and is regulated by the endogenous inhibitor epsilon, tightly bound ADP, the membrane potential and the redox state of the gamma subunit. In order to understand the molecular mechanism of epsilon inhibition, we constructed an expression system for the alpha(3)beta(3)gamma subcomplex in thermophilic cyanobacteria allowing thorough investigation of epsilon inhibition. epsilon Inhibition was found to be ATP-independent, and different to that observed for bacterial F(1)-ATPase. The role of the additional region on the gamma subunit of chloroplast-type F(1)-ATPase in epsilon inhibition was also determined. By single molecule rotation analysis, we succeeded in assigning the pausing angular position of gamma in epsilon inhibition, which was found to be identical to that observed for ATP hydrolysis, product release and ADP inhibition, but distinctly different from the waiting position for ATP binding. These results suggest that the epsilon subunit of chloroplast-type ATP synthase plays an important regulator for the rotary motor enzyme, thus preventing wasteful ATP hydrolysis.