<Emphasis Type="Italic">In vitro</Emphasis> organogenesis of <Emphasis Type="Italic">Passiflora alata</Emphasis>

Passiflora alata in vitro organogenesis was studied based on explant type, culture medium composition, and incubation conditions. The results indicated that the morphogenic process occurred more efficiently when hypocotyl segment-derived explants were cultured in media supplemented with cytokinin and AgNO₃ incubated under a 16-h photoperiod. The shoot bud elongation and plant development were obtained by transferring the material to MSM culture medium supplemented with GA₃ and incubated in flasks with vented lids. Histological analyses of the process revealed that the difficulties in obtaining plants could be related to the development of protuberances and leaf primordia structures, which did not contain shoot apical meristem. Roots developed easily by transferring elongated shoots to 1/2 MSM culture medium. Plant acclimatization occurred successfully, and somaclonal variation was not visually detected. The efficiency of this organogenesis protocol will be evaluated for genetic transformation of this species to obtain transgenic plants expressing genes that can influence the resistance to Cowpea aphid borne mosaic virus.     

Biotransformation of pineapple juice sugars into dietetic derivatives by using a cell free oxidoreductase from Zymomonas mobilis together with commercial invertase

An easy procedure for cell free biotransformation of pineapple juice sugars into dietetic derivatives was accomplished using a commercial invertase and an oxidoreductase from Zymomonas mobilis. First, pineapple juice sucrose was quantitatively converted into glucose and fructose by invertase, thus increasing the concentration of each monosaccharide in the original juice to almost twice. In a second step, glucose-fructose oxidoreductase (GFOR) transformed glucose into gluconolactone, and fructose into the low calorie sweetener sorbitol. The advantage of using GFOR is simultaneous reduction of fructose and oxidation of glucose, allowing the continuous regeneration of the essential coenzyme NADP(H), that is tightly bound to the enzyme. The yield of GFOR catalyzed sugar conversion depends on initial pH and control of pH during the reaction. At optimal conditions (pH control at 6.2) a maximum of 80% (w/v) sugar conversion was obtained. Without pH control, GFOR is inactivated rapidly due to gluconic acid formation. Therefore, conversion yields are relatively low at the natural pH of pineapple juice. The application of this process might be more advantageous on juices of other tropical fruits (papaya, jackfruit, mango) due to their naturally given higher pH.     

Bacterial proteins carrying twin-R signal peptides are specifically targeted by the delta pH-dependent transport machinery of the thylakoid membrane system

Glucose-fructose oxidoreductase (GFOR), a periplasmic protein of Zymomonas mobilis, is synthesized as a precursor polypeptide with a twin-R signal peptide for Sec-independent protein export in bacteria. In higher plant chloroplasts, twin-R signal peptides are specific targeting signals for the Sec-independent delta pH pathway of the thylakoid membrane system. In agreement with the assumed common phylogenetic origin of the two protein transport mechanisms, GFOR can be efficiently translocated by the delta pH-dependent pathway when analyzed with isolated thylakoid membranes. Transport is sensitive to the ionophore nigericin and competes with specific substrates for the delta pH-dependent transport route. In contrast, neither sodium azide nor enzymatic destruction of the nucleoside triphosphates in the assays affects thylakoid transport of GFOR indicating that the Sec apparatus is not involved in this process. Mutagenesis of the twin-R motif in the GFOR signal peptide prevents membrane translocation of the protein emphasizing the importance of these residues for the transport process.     

Gliding motility of Mycoplasma sp. nov. strain 163K.

The gliding movements of Mycoplasma sp. nov. strain 163K cells were characterized by photomicrographic and microcinematographic studies. The capability of gliding proved to be a very stable property of strain 163K. Cells were continuously moving, without interruption by resting periods, on glass as well as on plastic surfaces covered with liquid medium. Gliding cells always moved in the direction of their headlike structure; their course did not indicate any preference for a certain direction. Under appropriate growth conditions, cells showed linear and circular movements. Under inadequate conditions, cells glided in narrow circles or entered into zigzag trembling and tumbling movements. Organisms glided as single cells, in pairs, and in multicellular configurations. Movement patterns and gliding velocity were significantly affected by the cultivation and preparation time, the medium viscosity, and the storage and observation temperature. The number of passages on artificial media and the composition of the media used did not have a striking influence on gliding motility, but movements were effectively inhibited by homologous antiserum. The data obtained suggest that at least some of the structures associated with gliding are heat sensitive and located on the cell surface, that the gliding mechanism requires an intact energy metabolism, and, finally, that gliding motility is an extremely stable genetic property of Mycoplasma sp. nov. strain 163K.     

Implementing Process Analytical Technology for the Production of Recombinant Proteins in Escherichia coli Using an Advanced Controller Scheme

The performance of a bioreactor in meeting process goals is affected by the microorganism used, medium composition, and operating conditions. A typical bioreactor uses a supervisory control and data acquisition (SCADA) system for control, and a combination of software and hardware tools for real‐time data analysis. However, when the process is disrupted by utility or instrumentation failure, typical process controllers may be unable to reinstate normal operating conditions before the cells in the reactor shift to unfavorable metabolic regimes. The objective of this study is to examine how the response of a controller affects process recovery when disruptive incidences occur under a process analytical technology (PAT) framework. The process used for this investigation is the production of lethal toxin‐neutralizing factor (LTNF) by Escherichia coli (E. coli), which is controlled by a decoupled input–output‐linearizing controller (DIOLC). The performance of the DIOLC is compared to a proportional integral derivative (PID) controller subjected to the same conditions. The disruptions are introduced manually and the effect of controller action on process recovery and LTNF synthesis is measured in terms of peak purity and concentration. It is observed that DIOLC performs better after reinstating operating conditions and results in a meaningful improvement in performance.     

Controlled freezing of nonideal solutions with application to cryosurgical processes.

Success of a cryosurgical procedure, i.e., maximal cell destruction, requires that the cooling rate be controlled during the freezing process. Standard cryosurgical devices are not usually designed to perform the required controlled process. In this study, a new cryosurgical device was developed which facilitates the achievement of a specified cooling rate during freezing by accurately controlling the probe temperature variation with time. The new device has been experimentally tested by applying it to an aqueous solution of mashed potatoes. The temperature field in the freezing medium, whose thermal properties are similar to those of biological tissue, was measured. The cryoprobe temperature was controlled according to a desired time varying profile which was assumed to maximize necrosis. The tracking accuracy and the stability of the closed loop control system were investigated. It was found that for most of the time the tracking accuracy was excellent and the error between the measured probe temperature and the desired set point is within +/- 0.4 degrees C. However, noticeable deviations from the set point occurred due to the supercooling phenomenon or due to the instability of the liquid nitrogen boiling regime in the cryoprobe. The experimental results were compared to those obtained by a finite elements program and very good agreement was obtained. The deviation between the two data sets seems to be mainly due to errors in positioning of the thermocouple junctions in the medium.     

A Weibull statistics‐based lignocellulose saccharification model and a built‐in parameter accurately predict lignocellulose hydrolysis performance

Renewable energy from lignocellulosic biomass has been deemed an alternative to depleting fossil fuels. In order to improve this technology, we aim to develop robust mathematical models for the enzymatic lignocellulose degradation process. By analyzing 96 groups of previously published and newly obtained lignocellulose saccharification results and fitting them to Weibull distribution, we discovered Weibull statistics can accurately predict lignocellulose saccharification data, regardless of the type of substrates, enzymes and saccharification conditions. A mathematical model for enzymatic lignocellulose degradation was subsequently constructed based on Weibull statistics. Further analysis of the mathematical structure of the model and experimental saccharification data showed the significance of the two parameters in this model. In particular, the λ value, defined the characteristic time, represents the overall performance of the saccharification system. This suggestion was further supported by statistical analysis of experimental saccharification data and analysis of the glucose production levels when λ and n values change. In conclusion, the constructed Weibull statistics‐based model can accurately predict lignocellulose hydrolysis behavior and we can use the λ parameter to assess the overall performance of enzymatic lignocellulose degradation. Advantages and potential applications of the model and the λ value in saccharification performance assessment were discussed.     

Fed-batch culture of<Emphasis Type="Italic"> Bacillus thuringiensis</Emphasis> based on motile intensity

The operation of a fed-batch culture is more complicated than that of batch or continuous culture. Thus, an appropriate feeding strategy for fed-batch cultures should be carefully designed. In this study, a simple feeding strategy for fed-batch culture of Bacillus thuringiensis based on motile intensity is described. The feeding strategy consisted of two steps: (1) initiating feeding at the peak of motile intensity; (2) terminating feeding at low motile intensity (or non-motility) of the cells. In addition, the motile intensity of B. thuringiensis was used to determine the optimum environmental conditions (pH, temperature, and dissolved oxygen) and optimum medium composition. Using this fed-batch strategy, the production of thuringiensin increased 34% compared with batch culture using the same environmental conditions and medium composition. The proposed strategy for fed-batch culture helps to avoid overfeeding of substrate and facilitates on-line control. A comparison of several alternative strategies for fed-batch culture demonstrated that strategies such as glucose-stat and DO-stat result in a lower productivity than that obtained using the motility intensity method.     

Microbial lipids as a source of biofuel

This review presents the main directions and experimental data aimed at searching for active producers of lipids among different species of microorganisms and ways to optimize the lipidogenesis process in the most promising stains. It was shown that enzymatic processes can be directed by maintaining the necessary cultivation conditions. The influence on the growth, development, and biochemical activity of the microbial medium composition and temperature and the aeration and oxidation reduction conditions was considered. Changes in these factors affected the biosynthetic activity of microorganisms and lipidogenic yeasts and the composition of synthesized lipids. The ability of lipidogenic yeasts, as well as the relatively rapid ability of changing the amount and composition of lipids by direct cultivation, leads to the conclusion that lipids obtained by microbial synthesis can be a source of commercial raw materials for biofuel.     

Soft sensor based on 2D‐fluorescence and process data enabling real‐time estimation of biomass in Escherichia coli cultivations

In bioprocesses, specific process responses such as the biomass cannot typically be measured directly on‐line, since analytical sampling is associated with unavoidable time delays. Accessing those responses in real‐time is essential for Quality by Design and process analytical technology concepts. Soft sensors overcome these limitations by indirectly measuring the variables of interest using a previously derived model and actual process data in real time. In this study, a biomass soft sensor based on 2D‐fluorescence data and process data, was developed for a comprehensive study with a 20‐L experimental design, for Escherichia coli fed‐batch cultivations. A multivariate adaptive regression splines algorithm was applied to 2D‐fluorescence spectra and process data, to estimate the biomass concentration at any time during the process. Prediction errors of 4.9% (0.99 g/L) for validation and 3.8% (0.69 g/L) for new data (external validation), were obtained. Using principal component and parallel factor analyses on the 2D‐fluorescence data, two potential chemical compounds were identified and directly linked to cell metabolism. The same wavelength pairs were also important predictors for the regression‐model performance. Overall, the proposed soft sensor is a valuable tool for monitoring the process performance on‐line, enabling Quality by Design.     

Localisation of the glucose-fructose oxidoreductase in wild type and overproducing strains of Zymomonas mobilis

Abstract The enzyme glucose-fructose oxidoreductase (GFOR) from the Gram-negative ethanologenic bacterium Zymomonas mobilis was purified to homogeneity and was shown to be a tetrameric protein with a subunit size of M _r 42 500. Using immunogold-labelling in combination with electron microscopy, ultrathin sections of Z. mobilis wild type cells showed that the enzyme GFOR is located in the periplasm off the bacterial cells. Z. mobilis strains which carried the cloned gfo gene on plasmid pSUP104, had 5–6-fold increased GFOR enzyme activities. Moreover, these cells accumulated large amounts of a presumable unprocessed pre-GFOR protein ( M _r 48 000).     

The effects of lack of normality and homogeneity of variance on analysis of variance and clonal heritability in <Emphasis Type="Italic">in vitro</Emphasis> clonal propagation traits

We studied the fulfilment of assumptions of normality and homogeneity of error variance, prior to application of analysis of variance (ANOVA), for in vitro clonal propagation data. We assessed the use of data transformations and mean values for situations when the original data did not satisfy the required assumptions. The purpose of the study was to establish whether the use of original, transformed or mean values had any effect on F values, significance levels and clonal heritability values. The F values, significance levels and values of clonal heritability obtained showed analysis of variance to be reliable, despite deviations with respect to normality and homogeneity of variance and despite the fact that samples sizes were unequal. Original data may be used for ANOVA applied to measured variables such as number of shoots per explant, length of tallest shoot, number of 1-cm segments per explant and also derived variables such as the multiplication coefficient. Frequency data can be used for analysis of variance of categorical-type variables such as apical necrosis and percentage of responsive explant. For shoot colour variables, the distributions were very skewed and the variances were very different, but even though the sample sizes were not identical in all cases, lack of homogeneity of variance did not significantly affect F values, significance levels or clonal heritability values, and thus analysis of variance may be applied to the original data. The use of original and frequency data makes interpretation of the results easier than when transformed data are used and also allows us to calculate variance components more accurately than when using mean values, which do not provide as much information. Clonal heritability values from transformed data and mean values showed differences of less than one hundredth compared with those from original data. Box–Cox-transformed data showed slightly lower heritability values than those corresponding to original data, whereas clonal heritability values from both mean data and angular-transformed data were slightly higher than those obtained using original data. In clonal variability studies with single growth medium, nutritional conditions that encouraged highly unequal growth or characteristics among clones gave rise to data that were unlikely to satisfy the conditions of normality or homogeneity of variance.     

Thermodynamic functions of biopolymer hydration. I. Their determination by vapor pressure studies,discussed in an analysis of the primary hydration process

The primary hydration process of native biopolymers is analyzed in a brief review of the literature, pertaining to various aspects of biopolymer–water systems. Based on this analysis, a hydration model is proposed that implies that the solution conformation of native biopolymers is stable at and above a critical degree of hydration (h_p′ = 0.06–0.1 g H₂O/g polymer). This water content corresponds to the fraction of strongly bound water, and amounts to ～20% of the primary hydration sphere. In order to test this model, detailed sorption–desorption scanning experiments were performed on a globular protein (α-chymotrypsin). The results obtained are consistent with the proposed hydration model. They show that under certain experimental conditions, sorption isotherms can be obtained that do not exhibit hysteresis. These data represent equilibrium conditions and are thus accessible to thermodynamic treatment. Valid thermodynamic functions, pertinent to the interaction of water with biopolymers in their solution state, can be obtained from these sorption experiments.     

Characterization of Adhesive Exopolysaccharide (EPS) Produced by <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> Under Starvation Conditions

Pseudomonas aeruginosa synthesizes large quantities of exopolysaccharide (EPS), making it an excellent model organism for the study of EPS-mediated adhesion. The purpose of this investigation was to evaluate the influence of limited nutrients availability in the culture medium on the composition of EPS produced by P. aeruginosa. The relationship between the EPS production and the adhesion process of the P. aeruginosa cells to stainless steel surface (type 316 L) under starvation conditions were also examined. In all experimental variants P. aeruginosa produced more EPS with an increase of incubation period upon starvation conditions. Under limited nutrients condition, glucose dominated in the EPS materials. After 6 days of the process, only glucosyl units were detected in the extracellular matrix produced by nutrient-deprived P. aeruginosa cells. These extracellular molecules promoted more advanced stages of P. aeruginosa biofilm formation on the surface of stainless steel.     

Estimating single-channel kinetic parameters from idealized patch-clamp data containing missed events.

We present here a maximal likelihood algorithm for estimating single-channel kinetic parameters from idealized patch-clamp data. The algorithm takes into account missed events caused by limited time resolution of the recording system. Assuming a fixed dead time, we derive an explicit expression for the corrected transition rate matrix by generalizing the theory of Roux and Sauve (1985, Biophys. J. 48:149-158) to the case of multiple conductance levels. We use a variable metric optimizer with analytical derivatives for rapidly maximizing the likelihood. The algorithm is applicable to data containing substates and multiple identical or nonidentical channels. It allows multiple data sets obtained under different experimental conditions, e.g., concentration, voltage, and force, to be fit simultaneously. It also permits a variety of constraints on rate constants and provides standard errors for all estimates of model parameters. The algorithm has been tested extensively on a variety of kinetic models with both simulated and experimental data. It is very efficient and robust; rate constants for a multistate model can often be extracted in a processing time of approximately 1 min, largely independent of the starting values.     

Export of the periplasmic NADP-containing glucose-fructose oxidoreductase of Zymomonas mobilis

Glucose-fructose oxidoreductase (GFOR) of the gram-negative bacterium Zymomonas mobilis is a periplasmic enzyme with the tightly bound cofactor NADP. The preprotein carries an unusually long N-terminal signal sequence of 52 amino acid residues. A sorbitol-negative mutant strain (ACM3963) was found to be deficient in GFOR activity and was used for the expression of plasmid-borne copies of the wild-type gfo gene or of alleles encoding alterations in the signal sequence of the pre-GFOR protein. Z. mobilis cells with the wild-type gfo allele translocated pre-GFOR, at least partially, via the Sec pathway since CCCP (carboxylcyanide-m-chlorophenylhydrazone; uncoupler of proton motive force) or sodium azide (inhibitor of SecA) abolished the processing of GFOR. A gfo allele with the hydrophobic region of the signal sequence removed (residues 32–46; Δ32–46) led to a protein that was no longer processed, but showed full enzymatic activity (180 U/mg) and had the cofactor NADP firmly bound. A deletion in the n-region of the signal sequence (residues 2–20; Δ2–20) or exchange of the entire GFOR signal sequence with the signal sequence of gluconolactonase of Z. mobilis led to active and processed GFOR. Strain ACM3963 could not grow in the presence of high sugar concentrations (1 M sucrose) unless sorbitol was added. The presence of the plasmid-borne gfo wild-type allele or of the Δ2–20 deletion led to the restoration of growth on media with 1 M sucrose, whereas the presence of the Δ32–46 deletion led to a growth behavior similar to that of strain ACM3963, with no sorbitol formation from sucrose. Received: 14 December 1995 / Accepted: 4 March 1996     

On criteria of optimal conditions at ballistic disintegration of microbial cells

Summary The present study examines the processes of ballistic disintegration carried out to release active biopolymers. The relationship between the activity of unit volume of homogenates and the time of disintegration has been obtained. Correctness of this relationship for any process of disintegration can serve as the criterion of optimal chemical composition of the medium in which this process occurs. Only two quantitative criteria have been found sufficient for comparison of any regimes of ballistic disintegration. The theoretical conclusions are proved by experiments in ballistic disintegrators of two types.Torulopsis candida cells were used to release the succinate oxidizing enzyme.     

Mimic of a large‐scale diafiltration process by using ultra scale‐down rotating disc filter

Ultra scale‐down (USD) approach is a powerful tool to predict large‐scale process performance by using very small amounts of material. In this article, we present a method to mimic flux and transmission performance in a labscale crossflow operation by an USD rotating disc filter (RDF). The Pellicon 2 labscale system used for evaluation of the mimic can readily be related to small pilot and industrial scale. Adopted from the pulsed sample injection technique by Ghosh and Cui (J Membr Sci. 2000;175:5‐84), the RDF has been modified by building in inserts to allow the flexibility of the chamber volume, so that only 1.5 mL of processing material is required for each diafiltration experiment. The reported method enjoys the simplicity of dead‐end mode operation with accurate control of operation conditions that can mimic well the crossflow operation in large scale. Wall shear rate correlations have been established for both the labscale cassette and the USD device, and a mimic has been developed by operating both scales under conditions with equivalent averaged shear rates. The studies using E. coli lysate show that the flux vs. transmembrane pressure profile follows a first‐order model, and the transmission of antibody fragment (Fab′) is independent of transmembrane pressure. Predicted flux and transmission data agreed well with the experimental results of a labscale diafiltration where the cassette resistance was considered. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Production of palatinose using<Emphasis Type="Italic"> Serratia plymuthica</Emphasis> cells immobilized in chitosan

In recent decades, the production of palatinose has aroused great interest since this structural isomer of sucrose has interesting potential. We describe a simple and effective method of immobilizing Serratia plymuthica cells in chitosan. The sucrose isomerase activity of immobilized preparations was enhanced many times by activation with fresh nutrient medium and subsequent drying. The preparations obtained were physically very stable with high enzyme activity and excellent operational stability. The effect of temperature, pH and substrate concentration on enzyme activity of the immobilized cells was investigated. Using immobilized cells, a complete conversion of sucrose (40% solution) into palatinose was achieved in 4 h in a "batch"-type enzyme reactor. The use of free or immobilized cells had no effect on the composition of the solution, in particular the sugar content. The palatinose content was 80% and that of trehalulose 7%.     

Inhibierungserscheinungen bei der alkoholishchen Gärung III. Der Einfluß des osmotischen Druckes auf die Lebensfähigkeit von Saccharomyces cerevisiae

The influence of the osmotic pressure on the viability of yeast cells was studied in batch processes. It could be found, that the viability is a function of the total osmotic pressure obtained by adding the partial osmotic values of the principal ingredients saccharose, ethanol and salts dissolved in the medium. At optimum process conditions (pH, T, etc.) the cells can tolerate the osmotic pressure up to fixed value π₁. Above π₁ the viability decreases linearly and upward of a second threshold value π₂ nonlinearly. In the case of the used strain Saccharomyces cerevisiae Hansen Sc 5 the values of the both points are π₁ = 25 atm and π₂ = 47 atm.