Ethanol Production from Starch Hydrolyzates using <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> and Glucoamylase Entrapped in Polyvinylalcohol Hydrogel

The glucoamylase from Aspergillus niger, immobilized into poly(vinylalcohol) hydrogel lens-shaped capsules LentiKats®, was used for simultaneous saccharification and fermentation (SSF) with Zymomonas mobilis in free form. This system was stable in both the repeated batch and continuous mode of SSF. The microorganism was found to adsorb on the capsules with immobilized enzyme. This increased the ethanol productivity of the repeated batch system with 5% w/v of immobilized glucoamylase almost 2.1 times (7.2 g l^?1 h^?1) compared to free enzyme–free microorganism system (3.5 g l^?1 h^?1). The continuous SSF with the immobilized glucoamylase (11.5% w/v) tested for 15 days had productivity 10 g l^?1 h^?1, which is comparable to continuous experiments on semi-defined glucose medium (10 g l^?1 h^?1). These two systems were stable in both glucoamylase activity and microorganism productivity.     

Experimental techniques,data treatment for studying the dynamics of ethanol production/consumption in baker's yeast

The dynamics of ethanol production/consumption in baker's yeast were studied under feed- rate controlled conditions. The yeast was grown on molasses in an 8-l fed-batch reactor and experiments were done at cell concentrations between 5 and 65 g l^?1. Small changes in the feed rate were made around a feed rate corresponding to the critical growth rate, at which the yeast cell metabolism switches between ethanol consumption and production. A membrane gas sensor was used for on-line measurement of the ethanol concentration in the broth. The measured ethanol signal was used for control and the system was excited through changes in the regulator set-point. The closed-loop experiments ensured that feed variations were within the critical range, and thus facilitated reproducible experiments. Data were fitted to a second-order difference equation by statistical methods. Results were compared with a theoretically derived model. The process gain could be understood in terms of the underlying stoichiometry by using the “bottleneck” view of yeast glucose metabolism. The process time constant was found to be longer than is implied by a simple Monod relation between glucose uptake rate and concentration.     

Ethanol Production by Fermentation Using Immobilized Cells of Saccharomyces cerevisiae in Cashew Apple Bagasse

In this work, cashew apple bagasse (CAB) was used for Saccharomyces cerevisiae immobilization. The support was prepared through a treatment with a solution of 3% HCl, and delignification with 2% NaOH was also conducted. Optical micrographs showed that high populations of yeast cells adhered to pre-treated CAB surface. Ten consecutive fermentations of cashew apple juice for ethanol production were carried out using immobilized yeasts. High ethanol productivity was observed from the third fermentation assay until the tenth fermentation. Ethanol concentrations (about 19.82–37.83 g L^?1 in average value) and ethanol productivities (about 3.30–6.31 g L^?1 h^?1) were high and stable, and residual sugar concentrations were low in almost all fermentations (around 3.00 g L^?1) with conversions ranging from 44.80% to 96.50%, showing efficiency (85.30–98.52%) and operational stability of the biocatalyst for ethanol fermentation. Results showed that cashew apple bagasse is an efficient support for cell immobilization aiming at ethanol production.     

A sensitive continuous-flow bioluminescent system for determining ethanol in serum and saliva

A continuous-flow system, based on NAD(P)H:FMN oxidoreductase and bacterial luciferase co-immobilized on a nylon coil placed in front of a photomultiplier, and alcohol dehydrogenase separately immobilized on a second nylon coil, is described for the assay of ethanol in serum and saliva. The flow is air-segmented and 5–50-μl samples are required. The sample throughput is 25–30 h^?1 with no carryover. The detection limit is 1 μmol l^?1 ethanol (50 pmol injected) and the response is linear between 50 and 2500 pmol of ethanol. The relative standard deviation is 3–10% for both within-day and between-day assays, and serum and saliva can be analyzed directly. The immobilized enzymes are satisfactorily stable and up to 900 samples can be analyzed with one enzyme reactor.     

Kinetics and Thermodynamics of Ethanol Production by Saccharomyces cerevisiae MLD10 Using Molasses

In this study, we have used ultraviolet (UV) and γ-ray induction to get a catabolite repression resistant and thermotolerant mutant with enhanced ethanol production along with optimization of sugar concentration and temperature of fermentation. Classical mutagenesis in two consecutive cycles of UV- and γ-ray-induced mutations evolved one best catabolite-resistant and thermotolerant mutant Saccharomyces cerevisiae MLD10 which showed improved ethanol yield (0.48?±?0.02 g g^?1), theoretical yield (93?±?3 %), and extracellular invertase productivity (1,430?±?50 IU l^?1 h^?1), respectively, when fermenting 180 g sugars l^?1 in molasses medium at 43 °C in 300 m³ working volume fermenter. Ethanol production was highly dependent on invertase production. Enthalpy (ΔH*) (32.27 kJ M^?1) and entropy (ΔS*) (?202.88 J M^?1 K^?1) values at 43 °C by the mutant MLD10 were significantly lower than those of β-glucosidase production by a thermophilic mutant derivative of Thermomyces lanuginosus. These results confirmed the enhanced production of ethanol and invertase by this mutant derivative. These studies proved that mutant was significantly improved for ethanol production and was thermostable in nature. Lower fermentation time for ethanol production and maintenance of ethanol production rates (3.1 g l^?1 h^?1) at higher temperature (43 °C) by this mutant could decrease the overall cost of fermentation process and increase the quality of ethanol production.     

Enzymatic methods for the determination of ethanol based on linear and cyclif flow-injection systems

Linear and cyclic systems are described for the determination of ethanol (ca. 0.17–30×10^?3 M). In the linear system, the solution passes either through a minicolumn of yeast alcohol dehydrogenase (YADH) immobilized on controlled-pore glass or through minicolumns of the immobilized YADH and of yeast aldehyde dehydrogenase immobilized on cyanogen bromide-activated Sepharose-4B. The NADH formed is monitored either spectrophotometrically or spectrofluorimetrically. In the cyclic system, the solution passes through the same enzyme columns, and the NADH produced is monitored similarly before reconversion to NAD⁺ in a minicolumn of glutamate dehydrogenase immobilized on cyanogen bromie-activated Sepharose-4B in the presence of α-ketoglutarate and ammonium ions also present in the flow system. the sample throughout for both systems is ca. 40 h^?1 and 50 h^?1 for spectrophotometric and spectrofluorimetric detection, respectively. An on-line double-injection technique is described as an alternative to the cyclic system for limiting the consumption of NAD⁺.     

Continuous-flow extraction of organophosphorus pesticides coupled on-line with high-performance liquid chromatography

A continuous-flow extraction system coupled on-line with a high-performance liquid chromatograph with an ultraviolet detector is used to study the extraction of three organophosphorus pesticides (fenthion, azinphos methyl and diazinon) from aqueous samples with n-heptane as the organic solvent. Diazinon was not extracted significantly. The influence on the extraction of different parameters (coil length, flow rate and phase volume ratio) were studied. The calibration graphs are linear for 0.5–7 mg l^?1 and 8–20 mg l^?1 foor azinphos methyl where the percentage extraction (E%) is 90% and 70%, respectively, and up to 4 mg l^?1 for fenthion, where the E% is 33%. The detection limits and the relative standard deviations are 0.04 and 0.09 mg l^?1, and 3.4 and 5.3%, for azinphos methyl fenthion, respectively. Other pesticides and related compounds were found not to interfere. The sample throughput of this method was 15 h^?1.     

Efficient Production of Ethanol from Empty Palm Fruit Bunch Fibers by Fed-Batch Simultaneous Saccharification and Fermentation Using Saccharomyces cerevisiae

The concentration of ethanol produced from lignocellulosic biomass should be at least 40 g l^?1 [about 5 % (v/v)] to minimize the cost of distillation process. In this study, the conditions for the simultaneous saccharification and fermentation (SSF) at fed-batch mode for the production of ethanol from alkali-pretreated empty palm fruit bunch fibers (EFB) were investigated. Optimal conditions for the production of ethanol were identified as temperature, 30 °C; enzyme loading, 15 filter paper unit g^?1 biomass; and yeast (Saccharomyces cerevisiae) loading, 5 g l^?1 of dry cell weight. Under these conditions, an economical ethanol concentration was achieved within 17 h, which further increased up to 62.5 g l^?1 after 95 h with 70.6 % of the theoretical yield. To our knowledge, this is the first report to evaluate the economic ethanol production from alkali-pretreated EFB in fed-batch SSF using S. cerevisiae.     

Spectrophotometric determination of ethanol in blood using a flow-injection system with an immobilized enzyme (alcohol dehydrogenase) reactor coupled to an on-line dialyser

The determination of ethanol in whole blood without pretreatment using spectrotometric detection with an immobilized enzyme reactor coupled to an on-line dialyser is described. Optimum working conditions are given. The effects of the injection volume and the flow-rate on the peak height using the dialyser were investigated. A good linear calibration graph over the ethanol concentration range 3–40 μg ml^?1 was observed; these concentrations correspond to 0.3?4.0 g of ethanol per 1000 g of whole blood prior to dilution. For comparison, whole blood samples were analysed by gas chromatography with direct injection. The effect of temperature on the peak height was also studied in a system without the dialyser.     

On-line application of ion chromatography in a thermal power plant

Complete monitoring of the “condensate-feedwater” cycle in power plants requires reliable automatic methods suitable for very low concentrations of various chemical species. A complete on-line ion-chromatography monitoring system is under development. It comprises an automatic on-line sampling system two Dionex Model QUIC (process instrument) ion chromatographs, an on-line calibration systems, and a data acquisition/processing system. The present model serves for the determination of sodium, chloride and sulfate ions. Detection limits are < 1 μg l^?1 (P = 95%) with liner ranges up to 10 μ l^?1 or about 200 μ l^?1 depending on settings. The importance of statistical evaluation of data is emphasized. The instrumentation was tested for sequential samples from crucial points of a 320-MW thermal power station with satisfactory results. Problems of reliability are discussed.     

In Situ Biphasic Extractive Fermentation for Hexanoic Acid Production from Sucrose by Megasphaera elsdenii NCIMB 702410

Hexanoic acid production by a bacterium using sucrose as an economic carbon source was studied under conditions in which hexanoic acid was continuously extracted by liquid–liquid extraction. Megasphaera elsdenii NCIMB 702410, selected from five M. elsdenii strains, produced 4.69 g l^?1 hexanoic acid in a basal medium containing sucrose. Production increased to 8.19 g l^?1 when the medium was supplemented by 5 g l^?1 sodium butyrate. A biphasic liquid–liquid extraction system with 10 % (v/v) alamine 336 in oleyl alcohol as a solvent was evaluated in a continuous stirred-tank reactor held at pH 6. Over 90 % (w/w) of the hexanoic acid in a 0.5 M aqueous solution was transferred to the extraction solvent within 10 h. Cell growth was not significantly inhibited by direct contact of the fermentation broth with the extraction solvent. The system produced 28.42 g l^?1 of hexanoic acid from 54.85 g l^?1 of sucrose during 144 h of culture, and 26.52 and 1.90 g l^?1 of hexanoic acid was accumulated in the extraction solvent and the aqueous fermentation broth, respectively. The productivity and yield of hexanoic acid were 0.20 g l^?1 h^?1 and 0.50 g g^?1 sucrose, respectively.     

l-Ribose Production from l-Arabinose by Immobilized Recombinant Escherichia coli Co-expressing the l-Arabinose Isomerase and Mannose-6-Phosphate Isomerase Genes from Geobacillus thermodenitrificans

l-Ribose is an important precursor for antiviral agents, and thus its high-level production is urgently demanded. For this aim, immobilized recombinant Escherichia coli cells expressing the l-arabinose isomerase and variant mannose-6-phosphate isomerase genes from Geobacillus thermodenitrificans were developed. The immobilized cells produced 99 g/l l-ribose from 300 g/l l-arabinose in 3 h at pH 7.5 and 60 °C in the presence of 1 mM Co²⁺, with a conversion yield of 33 % (w/w) and a productivity of 33 g/l/h. The immobilized cells in the packed-bed bioreactor at a dilution rate of 0.2 h^?1 produced an average of 100 g/l l-ribose with a conversion yield of 33 % and a productivity of 5.0 g/l/h for the first 12 days, and the operational half-life in the bioreactor was 28 days. Our study is first verification for l-ribose production by long-term operation and feasible for cost-effective commercialization. The immobilized cells in the present study also showed the highest conversion yield among processes from l-arabinose as the substrate.     

Enhancing pIFN-α Production and Process Stability in Fed-Batch Culture of Pichia pastoris by Controlling the Methanol Concentration and Monitoring the Responses of OUR/DO Levels

Effective expression of porcine interferon-α (pIFN-α) with recombinant Pichia pastoris was conducted in a bench-scale fermentor using an in situ methanol electrode-based feeding process with the control level of methanol concentration linearly increased to 10 g l^?1 for the first 20 h and maintained at 10 g l^?1 for the rest of expression phase. With this two-stage control process, the highest pIFN-α concentration reached a level of 1.81 g l^?1, which was 1.5-fold of that in the previous constant 10 g l^?1 induction experiments. There is an improvement of the pIFN-α productivity from more distribution of carbon flux to protein expression. The pIFN-α expression stability could be further enhanced by a simple on-line fault diagnosis method for methanol overfeeding based on oxygen uptake rate changing patterns. By implementing corrective action of feeding glycerol after fault detection, the production yield increased to twice the amount it would have been without the diagnosis.     

Flow-injection spectrophotometric determination of glucose in blood plasma with bindschedler's green leuco base as color reagent

The hydrogen peroxide produces in the oxidation of glucos in an immobilized glucose oxidase reactor is determined by using Bindschedler's green (leuco base) as color reagent with iron(II) as catalyst; the increase in the absorbance at 725 nm is measured. For 100-μl samples, calibration was almost linear in the range 0–2.5 mg l^?1 glucose; the relative standard deviation for 1 mg l^?1 glucose was 0.6% (n=10) and the detection limit (S/N= 2) was 0.02 mg l^?1. The injection rate was 20 h^?1. Glucose was determined satisfactorily in control sera and in real blood sera.     

Elimination of Acetate Production to Improve Ethanol Yield During Continuous Synthesis Gas Fermentation by Engineered Biocatalyst Clostridium sp. MTEtOH550

Acetogen strain Clostridum sp. MT653 produced acetate 273?mM (p?<?0.005) and ethanol 250?mM (p?<?0.005) from synthesis gas blend mixture of 64?% CO and 36?%?H₂. Clostridum sp. MT653 was metabolically engineered to the biocatalyst strain Clostridium sp. MTEtOH550. The biocatalyst increased ethanol yield to 590?mM with no acetate production during single-stage continuous syngas fermentation due to expression of synthetic adh cloned in a multi-copy number expression vector. The acetate production was eliminated by inactivation of the pta gene in Clostridium sp. MTEtOH550. Gene introduction and gene elimination were achieved only using Syngas Biofuels Energy, Inc. electroporation generator. The electrotransformation efficiencies were 8.0?±?0.2?×?10⁶ per microgram of transforming DNA of the expression vector at cell viability ~15?%. The frequency of suicidal vector integration to inactivate pta was ~10^?5 per the number of recipient cells. This is the first report on elimination of acetate production and overexpression of synthetic adh gene to engineer acetogen biocatalyst for selective biofuel ethanol production during continuous syngas fermentation.     

Characteristics of an Immobilized Yeast Cell System Using Very High Gravity for the Fermentation of Ethanol

The characteristics of ethanol production by immobilized yeast cells were investigated for both repeated batch fermentation and continuous fermentation. With an initial sugar concentration of 280?g/L during the repeated batch fermentation, more than 98% of total sugar was consumed in 65?h with an average ethanol concentration and ethanol yield of 130.12?g/L and 0.477?g ethanol/g consumed sugar, respectively. The immobilized yeast cell system was reliable for at least 10 batches and for a period of 28?days without accompanying the regeneration of Saccharomyces cerevisiae inside the carriers. The multistage continuous fermentation was carried out in a five-stage column bioreactor with a total working volume of 3.75?L. The bioreactor was operated for 26?days at a dilution rate of 0.015?h^?1. The ethanol concentration of the effluent reached 130.77?g/L ethanol while an average 8.18?g/L residual sugar remained. Due to the high osmotic pressure and toxic ethanol, considerable yeast cells died without regeneration, especially in the last two stages, which led to the breakdown of the whole system of multistage continuous fermentation.     

Kinetics of sorption and permeation of water in glassy polyimide

A vapor permeation experiment for water–ethanol mixtures was carried out using asymmetric Ube polyimide hollow-fiber membranes, which exhibit high selective permeability for water vapor, under the conditions of T=413 K, upstream gas pressure P_h=1.5×10⁵∼2.95×10⁵ Pa and downstream gas pressure P_l=400 Pa. To represent gas separation properties of the Ube polyimide membrane with a high transition temperature (570 K), the contribution of Henry's law part and Langmuir part modes on the diffusion through the membrane is studied on the basis of the dual-mode transport models. The results show that Henry's law penetrant controls the diffusion in the membrane. For the separation of water–ethanol mixtures by permeation through Ube polyimide membranes, the water trapped in microcavities can be assumed to be totally immobilized under the operating conditions applied here.     

Efficient Microbial Conversion of l-Tyrosine to l-DOPA by Brevundimonas sp. SGJ

l-DOPA (3,4-dihydroxyphenyl-l-alanine), the most widely used drug for the treatment of Parkinson??s disease, was produced in buffer using biomass of Brevundimonas sp. SGJ. The effects of enhancers, such as carrageenan, diatomaceous earth, and activated charcoal, on the l-DOPA production were evaluated to obtain the maximum yield. The optimal process conditions found were pH?8, 2?g?l^?1 cell mass, 2?g?l^?1 l-tyrosine, 0.04?g?l^?1 CuSO₄, 0.02?g?l^?1 l-ascorbic acid, 0.5?g?l^?1 carrageenan, and 40?°C temperature. In addition, repeated use of cells resulted in the highest yield of 3.81?g?l^?1 (95.2%) of l-DOPA with utilization of 4?g?l^?1 l-tyrosine, and the highest tyrosinase activity (9,201?U?mg^?1) was observed at 18?h of incubation. Furthermore, the produced l-DOPA was confirmed by high-performance thin-layer chromatography, high-performance liquid chromatography, and gas chromatography?Cmass spectroscopy. Kinetic studies showed significant values of Y _p/s, Q _s, and q _s after optimization of the process. Thus, Brevundimonas sp. SGJ could be an eventual new source for large-scale production of l-DOPA.     

Gas-diffusion dilution flow-injection method for the determination of ethanol in beverages without sample pretreatment

The combination of immobilized alcohol oxidase (AOD) with a gas-diffusion membrane in a flow-injection system greatly enhanced the specificity of ethanol determination. This gas-diffusion flow-injection system with amperometric detection of hydrogen peroxide had a linear range of analysis from 0.0006 up to 60% (v/v) ethanol. Silicone-modified polypropylene membranes of different thickness were used. Undiluted samples of beer, wine, spirits and medicine could be investigated with excellent correlation with standard methods (r > 0.997). The frequency of analysis was 120–180 samples h^?1 and the operational half-life of the immobilized enzyme was 8000 injections within 44 h.     

Flow-injection extraction spectrophotometric method for the determination of lead and its combination with minicolumn preconcentration

An automatic flow-injection method was developed for the determination of lead in the range 50–2000 μg l^?1. The method is based on the extraction of lead with the crown ether dicyclohexyl-18-crown-6 into chloroform from an acidic medium, subsequent addition of dithizone as chromogenic reagent to the extract and measurement of absorbance. The sample throughput is 45 h^?1. A microcolumn containing Chelex-100 chelating resin is used for on-line preconcentration of lead, giving a detection limit of 5 μg l^?1 with a sample throughout of 36 h^?1. The method compares favourably with the dithizone and diethyldithiocarbamate methods with respect to selectivity. Application to standard alloys, soil leachates and sea water is demonstrated.