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Scale Production (scale + production)
Kinds of Scale Production Selected AbstractsProduction of PHB from Crude GlycerolENGINEERING IN LIFE SCIENCES (ELECTRONIC), Issue 5 2007G. Mothes Abstract Crude glycerol , a by-product of the large scale production of diesel oil from rape , is examined for its possible use as a cheap feedstock for the biotechnological synthesis of poly(3-hydroxybutyrate) (PHB). The glycerol samples of various manufacturers differ in their contamination with salts (NaCl or K2SO4), methanol or fatty acids. At high cell density fermentation these pollutants could possibly accumulate to inhibiting concentrations. The bacteria used were Paracoccus denitrificans and Cupriavidus necator JMP 134, which accumulate PHB from pure glycerol to a content of 70 % of cell dry mass. When using crude glycerol containing 5.5 % NaCl, a reduced PHB content of 48 % was observed at a bacterial dry mass of 50 g/L. Furthermore the PHB yield coefficient was reduced, obviously due to osmoregulation. The effect of glycerol contaminated with K2SO4 was less pronounced. The molecular weight of PHB produced with P. denitrificans or C. necator from crude glycerol varies between 620000 and 750000 g/mol which allows the processing by common techniques of the polymer industry. [source] Phenotypic degeneration occurs during sector formation in Metarhizium anisopliaeJOURNAL OF APPLIED MICROBIOLOGY, Issue 1 2002M.J. Ryan Aims: ,The formation of sectors was observed during subculturing of an isolate of the entomopathogenic fungus Metarhizium anisopliae, a fungus used for biological control of insect pests. The aim of the investigation was to establish whether sector formation was accompanied by changes in physiological characters. Methods and Results: ,Four degenerative morphological states, with reduced sporulation capacity, were characterized. Subcultures were taken from each sector and four new culture lines established. The new lines were further subcultured every 21 d. A physiological assessment of each line was undertaken after 42 d using TLC of secondary metabolites and fluorogenic enzyme tests. Full sporulation capacity was not regained on subculture, although some cultures recovered partially. Changes in secondary metabolite profiles and the loss in detection of activity of specific enzymes were observed. Conclusions: ,Sector formation was frequently accompanied by changes in the ability to produce secondary metabolites and enzymes. Significance and Impact of Study: ,The results illustrate the importance of maintaining the stability of important cultures during routine subculture. The consequences could have significant implications if degenerate cultures are used as inocula for liquid fermentation cultures or industrial scale production. [source] Fermentative production of L(+)-lactic acid from starch hydrolyzate and corn steep liquor as inexpensive nutrients by batch culture of Enterococcus faecalis RKY1JOURNAL OF CHEMICAL TECHNOLOGY & BIOTECHNOLOGY, Issue 10 2008Young-Jung Wee Abstract BACKGROUND: Attempts were made to determine the lactic acid production efficiency of novel isolate, Enterococcus faecalis RKY1 using four different starches (corn, tapioca, potato, and wheat starch) with different concentrations (50, 75, 100, and 125 g L,1) and corn steep liquor as an inexpensive nitrogen source. RESULTS: The yield of lactic acid from each starch was higher than 95% based on initial starch concentrations. High lactic acid concentration (129.9 g L,1) and yield (1.04 g-lactic acid g,1 -starch) were achieved faster (84 h) from 125 g L,1 of corn starch. Among the starches used, tapioca starch fermentation usually completed in a shorter incubation period. The final dry cell weight was highest (7.0 g L,1) for the medium containing 75 g L,1 of corn starch, which resulted in maximum volumetric productivity of lactic acid (3.6 g L,1 h,1). The addition of 30 g L,1 corn steep liquor supplemented with a minimal amount of yeast extract supported both cell growth and lactic acid fermentation. CONCLUSION:Enterococcus faecalis RKY1 was found to be capable of growing well on inexpensive nutrients and producing maximum lactic acid from starches and corn steep liquor as lower-cost raw materials than conventionally-used refined sugars such as glucose, and yeast extract as an organic nitrogen source in laboratory-scale studies. These fermentation characteristics are prerequisites for the industrial scale production of lactic acid. Copyright © 2008 Society of Chemical Industry [source] Biomimetic affinity purification of cardiotoxin and its pharmacological effects on the nervous system,JOURNAL OF MOLECULAR RECOGNITION, Issue 3 2008Dexian Dong Abstract Cobra venom is a very precious natural resource. The traditional method for purification of cardiotoxin from cobra venom is a multi-step, high cost, and low recovery procedure. By molecular modeling and docking with SYBYL software, we designed and synthesized an affinity ligand, m-aminobenzoic acid, for high efficiency purification of this therapeutically useful Chinese cobra venom cardiotoxin. The one-step recovery of cardiotoxin reached 64% and the purity reached 92% upon purification. The binding capacity of this synthetic ligand was 9.1,mg cardiotoxin/g moist weight gel and the affinity constant for cardiotoxin was 5.5,×,103,M,1. Unlike a natural affinity ligand, this synthetic ligand is highly stable, and has great potential for industrial scale production of cardiotoxin. In addition, we examined the effects of cardiotoxin on the nervous system in a mouse model. Results showed that cardiotoxin could maintain analgesic effects for 120,min with a dose of less than 0.06,mg/kg (2.8% of the LD50). Administration of 0.12,mg/kg cardiotoxin could improve scopolamine impairments of memory in mice. These results suggest that cardiotoxin may be a potential drug for nervous system diseases. Copyright © 2008 John Wiley & Sons, Ltd. [source] Bicyclobutanes and cyclobutenes: Unusual carbocyclic monomersJOURNAL OF POLYMER SCIENCE (IN TWO SECTIONS), Issue 5 2003H. K. Hall Jr. Abstract Bicyclobutanes and cyclobutenes substituted with electron-attracting groups represent novel classes of reactive monomers. They readily undergo free-radical and anionic polymerizations to give high polymers consisting of 1,3- and 1,2-enchained cyclobutane rings, respectively. They also copolymerize readily with conventional vinyl monomers. These polymers display numerous attractive properties in comparison with their vinyl counterparts, including enhanced thermal stability, superior optical properties, and higher glass-transition temperatures. The syntheses of these monomers are reviewed, and suggestions toward future larger scale production are made. © 2003 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 625,635, 2003 [source] Sedimentation field-flow fractionation and granulometric analysis of PLGA microspheresJOURNAL OF SEPARATION SCIENCE, JSS, Issue 15-16 2003Nathalie Faisant Abstract Sedimentation field flow fractionation operated in the steric hyperlayer mode was used to obtain fractions of defined characteristics from crude samples of poly(D,L-lactic-co-glycolic acid) microspheres which were polydisperse in size. In less than ten minutes, Sedimentation Field Flow Fractionation (SdFFF) separation yielded three analytical fractions of very different size and particle size distribution (PSD) characteristics, as determined by granulometric analyses (Coulter Counter® and image analysis of SEM). A crude sample (average size = 45 ,m, 105% size polydispersity index) was separated into fractions of 73 ,m, 56 ,m, 8 ,m average diameters which showed a PSD of 39%, 33%, 30%, respectively. Our results demonstrated that SdFFF used in conjunction with particle size analysis offers a new approach to laboratory scale production of drug vectors of a specified average size and reduced size dispersity. In the future, this could be used to select the most convenient particles for drug loading and release. [source] The evolution of coenzyme QBIOFACTORS, Issue 1-4 2008Frederick L. Crane In the 50 years since the identification of coenzyme Q as an electron carrier in mitochondria, it has been identified with diverse and unexpected functions in cells. Its discovery came as a result of a search for electron carriers in mitochondria following the identification of flavin and cytochromes by Warburg, Keilin, Chance and others. As a result of investigation of membrane lipids at D.E. Green's laboratory at University of Wisconsin coenzyme Q was identified as the electron carrier between primary flavoprotein dehydrogenases and the cytochromes. Then Peter Mitchell identified the role of transmembrane proton transfer as a basis for ATP synthesis. The general distribution of coenzyme Q in all cell membranes then led to the recognition of a role as a primary antioxidant. The protonophoric function was extended to acidification of Golgi and lysosomal vericles. A further role in proton release through the plasma membrane and its relation to cell proliferation has not been fully developed. A role in generation of H2 O2 as a messenger for hormone and cytokine action is indicated as well as prevention of apoptosis by inhibition of ceramide release. Identification of the genes and proteins required for coenzyme Q synthesis has led to a basis for defining deficiency. For 50 years Karl Folkers has led the search for deficiency and therapeutic application. The development of large scale production, better formulation for uptake, and better methods for analysis have furthered this search. The story isn't over yet. Questions remain about effects on membrane structure, breakdown and control of cellular synthesis and uptake and the basis for therapeutic action. [source] Metabolism in 1,3-propanediol fed-batch fermentation by a D -lactate deficient mutant of Klebsiella pneumoniaeBIOTECHNOLOGY & BIOENGINEERING, Issue 5 2009Yun-Zhen Xu Abstract Klebsiella pneumoniae HR526, a new isolated 1,3-propanediol (1,3-PD) producer, exhibited great productivity. However, the accumulation of lactate in the late-exponential phase remained an obstacle of 1,3-PD industrial scale production. Hereby, mutants lacking D -lactate pathway were constructed by knocking out the ldhA gene encoding fermentative D -lactate dehydrogenase (LDH) of HR526. The mutant K. pneumoniae LDH526 with the lowest LDH activity was studied in aerobic fed-batch fermentation. In experiments using pure glycerol as feedstock, the 1,3-PD concentrations, conversion, and productivity increased from 95.39,g,L,1, 0.48 and 1.98,g,L,1,h,1 to 102. 06,g,L,1, 0.52,mol,mol,1 and 2.13,g,L,1,h,1, respectively. The diol (1,3-PD and 2,3-butanediol) conversion increased from 0.55,mol,mol,1 to a maximum of 0.65,mol,mol,1. Lactate would not accumulate until 1,3-PD exceeded 84,g,L,1, and the final lactate concentration decreased dramatically from more than 40,g,L,1 to <3,g,L,1. Enzymic measurements showed LDH activity decreased by 89,98% during fed-batch fermentation, and other related enzyme activities were not affected. NADH/NAD+ enhanced more than 50% in the late-exponential phase as the D -lactate pathway was cut off, which might be the main reason for the change of final metabolites concentrations. The ability to utilize crude glycerol from biodiesel process and great genetic stability demonstrated that K. pnemoniae LDH526 was valuable for 1,3-PD industrial production. Biotechnol. Bioeng. 2009; 104: 965,972. © 2009 Wiley Periodicals, Inc. [source] Hydrophobic interaction chromatography in dual salt system increases protein binding capacityBIOTECHNOLOGY & BIOENGINEERING, Issue 5 2009Anna M. Senczuk Abstract Hydrophobic interaction chromatography (HIC) uses weakly hydrophobic resins and requires a salting-out salt to promote protein,resin interaction. The salting-out effects increase with protein and salt concentration. Dynamic binding capacity (DBC) is dependent on the binding constant, as well as on the flow characteristics during sample loading. DBC increases with the salt concentration but decreases with increasing flow rate. Dynamic and operational binding capacity have a major raw material cost/processing time impact on commercial scale production of monoclonal antibodies. In order to maximize DBC the highest salt concentration without causing precipitation is used. We report here a novel method to maintain protein solubility while increasing the DBC by using a combination of two salting-out salts (referred to as dual salt). In a series of experiments, we explored the dynamic capacity of a HIC resin (TosoBioscience Butyl 650M) with combinations of salts. Using a model antibody, we developed a system allowing us to increase the dynamic capacity up to twofold using the dual salt system over traditional, single salt system. We also investigated the application of this novel approach to several other proteins and salt combinations, and noted a similar protein solubility and DBC increase. The observed increase in DBC in the dual salt system was maintained at different linear flow rates and did not impact selectivity. Biotechnol. Bioeng. 2009;103: 930,935. © 2009 Wiley Periodicals, Inc. [source] Simultaneous expression and maturation of the iron-sulfur protein ferredoxin in a cell-free systemBIOTECHNOLOGY & BIOENGINEERING, Issue 1 2006Marcus E. Boyer Abstract The model iron-sulfur (Fe-S) protein ferredoxin (Fd) from Synechocystis sp. PCC 6803 has been simultaneously produced and matured in a cell-free production system. After 6 h of incubation at 37°C, Fd accumulated to >450 µg/mL. Essentially all was soluble, and 85% was active. Production and maturation of the protein in the cell-free system were found to be dependent in a coupled manner on the concentration of the supplemented iron and sulfur sources, ferrous ammonium sulfate and cysteine, respectively. The recombinant expression of ISC helper proteins during cell extract preparation did not increase cell-free Fd accumulation or activity, although the efficiency of iron and cysteine utilization increased. Fd maturation was independent of protein production rate, and proceeded at a constant rate throughout the period of active translation. In addition, incubation of denatured apo Fd with cell-free reaction components resulted in recovery of Fd activity, supporting the interpretation that maturation mechanisms did not act co-translationally. Incubation at 28°C increased total and active protein accumulation, but decreased the ratio of active to total Fd produced. In summary, the high product yields and folding efficiency make the cell-free system described here an attractive platform for the study of Fe-S protein production and maturation. The system enables both small-volume, high throughput investigations as well as larger scale production. To our knowledge, this is the first demonstration of directed, high-yield production and maturation of an Fe-S protein in a cell-free system. © 2006 Wiley Periodicals, Inc. [source] Biosynthesis of silver nanoparticles using Eclipta leafBIOTECHNOLOGY PROGRESS, Issue 5 2009Anal K. Jha Abstract A green, low-cost and reproducible Eclipta leaves negotiated synthesis of silver nanoparticles is reported. The synthesis is performed at room temperature. X-ray and transmission electron microscopy analyses are performed to ascertain the formation of Ag nanoparticles. Nanoparticles almost spherical in shape having a size of 2,6 nm are found. UV-visible study revealed the surface plasmon resonance at 419 nm. The lattice strain is estimated to be 0.0045 using Williamson-Hall approach. The use of Eclipta for the synthesis of silver nanoparticles offers the benefit of ecofriendliness and amenability for large scale production through scaling up. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009 [source] Microreactor Technology: A Revolution for the Fine Chemical and Pharmaceutical Industries?CHEMICAL ENGINEERING & TECHNOLOGY (CET), Issue 3 2005D. M. Roberge Abstract 50,% of reactions in the fine chemical/pharmaceutical industry could benefit from a continuous process based mainly on microreactor technology. However, the frequent presence of a solid phase still hinders the widespread application of such a technology as a multi-purpose solution. For small scale and pilot productions, speed in process R&D, as well as the avoidance of scale-up issues, are the main drivers. On the other hand, for large scale productions, a gain in yield and safety are the main motivations for the use of micoreactor technology. The gain in yield must be significant in order to cope with the increase in capital expenditure associated with the development of a new technology. [source] | |||||||||||||