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1.
The performance of a tapered reactor for the continuous cultivation of bakers' yeast (SCP) from cane molasses has been compared with that of a conventional cylindrical reactor. It is found that the tapered reactor has less non-idealities (bypass and deadspace).Using the experimentally evaluated bypass and deadspace values, a model for predicting conversions of substrate (cane molasses), based on the RTD model proposed by Cholette and Cloutier has been developed. The experimental substrate conversions are found to match the model satisfactorily.List of Symbols D h–1 dilution rate - E() exit age distribution function - K s kg/m3 Monod's saturation constant - -r sa kg/(m3 · h) rate of substrate utilization - S kg/m3 substrate concentration expressed as dextrose equivalent (DE) - S a kg/m3 substrate concentration in active zone - S 0 kg/m3 initial substrate concentration - S/S 0 dimensionless substrate concentration - v a dm3/h volumetric flow through active zone - v b dm3/h volumetric flow through bypass stream - u l dm3/h substrate feed rate - v g dm3/min air-flow rate - V dm3 total working volume of the reactor - V a dm3 volume of active zone in reactor - V d dm3 volume of dead zone in reactor - X kg/m3 biomass concentration Greek Letters fraction of bypass of feed, v b /v l - fraction of deadspace, V d /V - dimensionless residence time - m h–1 maximum specific growth rate - h mean residence time, V/v l   相似文献   
2.
The effect of micromixing and macromixing on enzyme reaction of Michaelis-Menten type in a real continuously stirred tank reactor (CSTR) is considered. The effect of bypassing of a fraction of feed stream, dead space, initial enzyme concentration and Michaelis-Menten constant on substrate conversion is evaluated. Bypass reduces the substrate conversion significantly compared with other parameters in the case of micro and macromixing. Micromixing predicts higher substrate conversions compared with macromixing. The effect of micro and macromixing on substrate conversion is negligible at low and high conversions.List of Symbols C kmol/m3 concentration of reactant - ¯C kmol/m3 average concentration of reactant - CA kmol/m3 exit concentration of reactant A - CAa kmol/m3 exit concentration of reactant A from active zone - CAO kmol/m3 initial concentration of reactant A - CEO kmol/m3 initial enzyme concentration - CO kmol/m3 initial concentration of reactant - E(t) 1/s exit age distribution function - k 1/s reaction rate constant - M kmol/m3 Michaelis-Menten constant - r kmol/(m3s) rate of reaction - –rA kmol/(m3s) rate of reaction with respect to A - t s time - v m3/s volumetric feed rate - va m3/s volumetric feed rate entering the active zone - vb m3/s volumetric feed rate entering the bypass stream - V m3 total volume of the vessel - Va m3 active volume of the vessel - Vd m3 volume of dead space - XA conversion of A Greek Letters fraction of feed stream bypassing the vessel (vb/v) - fraction of the total volume as dead space (Vd/V) - (t) 1/s Dirac delta function, an ideal pulse occurring at time t = 0 - s life expectancy of a molecule - 1/s intensity function or escape probability function - s space time or mean residence time  相似文献   
3.
A series of 1-substituted-3-(6-methylpyridin-2-yl)-4-([1,2,4]triazolo[1,5-a]pyridin-6-yl)pyrazoles 14a-ae, 16a, 16b, and 21a-c has been prepared and evaluated for their ALK5 inhibitory activity in an enzyme assay and in a cell-based luciferase reporter assay. The 4-([1,2,4]triazolo[1,5-a]pyridin-6-yl)-N-(4-methoxyphenyl)-3-(6-methylpyridin-2-yl)-1H-pyrazole-1-carbothioamide (14n) inhibited ALK5 phosphorylation with IC(50) value of 0.57 nM and showed 94% inhibition at 100 nM in a luciferase reporter assay using HaCaT cells permanently transfected with p3TP-luc reporter construct.  相似文献   
4.
Summary Different commercial enzymes, used individually or in combination, released upto 96% starch from whole cassava chips with pectinase I and cellulase combination. The enzymic action on macerating chips and disintegrating root cells was dependent on size of chips, presence of peel, temperature, time, agitation and type as well as concentration of enzymes. Significantly higher starch recovery and elimination of cost-intensive mechanical pulverization indicate potential of the enzymic technique.  相似文献   
5.
1. Feeding of alpha-p-chlorophenoxyisobutyrate (CPIB) to rats increased ubiquinone concentration in the liver but not in other tissues. The increase was progressive with the time of feeding and related to the concentration of CPIB in the diet. 2. Incorporation of [1-(14)C]acetate, but not of [2-(14)C]mevalonate, into sterols in the liver in vivo or by liver slices in vitro was decreased on feeding the rats with CPIB. However, incorporation of mevalonate into ubiquinone increased. 3. CPIB, when added in low concentrations to liver slices, had no effect on isoprene synthesis from acetate; higher concentrations, however, were inhibitory. 4. No activation of ubiquinone synthesis from mevalonate was observed when CPIB was added to the liver slices synthesizing ubiquinone. 5. The increase in ubiquinone in CPIB-fed animals appears to be due to increased synthesis in the initial stages and to decreased catabolism in the later stages. 6. An inverse relationship was found between the concentration of ubiquinone in the liver and the serum sterol concentration in CPIB-fed rats.  相似文献   
6.
The aim of this work was to develop a standard quantitative method to measure the acid tolerance of probiotic cells when exposed to a simulated gastric fluid. Three model strains of different cell concentrations were exposed to a standard simulated gastric fluid of fixed volume. The fluid pH ranged from pH 1.5 to 2.5. In general, the death kinetics followed an exponential trend. The overall death constant, k d, for all strains was found to be in a power relationship with the pH value and the initial cell concentration, and it can be expressed as
k\textd\text = k\textAII( \textp\textH - \text9.0N0 - 0.\text19 ) {k_{\text{d}}}{\text{ = }}{k_{\text{AII}}}\left( {{\text{p}}{{\text{H}}^{ - {\text{9}}.0}}{N_0}^{ - 0.{\text{19}}}} \right)  相似文献   
7.
A procedure was developed for the determination of Cu, Mn, Pb, Cd, Co, Cr, and Zn in water samples by Inductively Coupled Plasma-Optical Emission Spectrometry (ICP-OES) after preconcentration on synthesized 2-propylpiperidine-1-carbodithioate supported by Borassus flabellifer Inflorescence (BFI). The sorbed element was subsequently eluted with 0.4 M HNO3, and the acid eluates were analyzed by ICP-OES. The influence of various parameters such as pH, flow rate of sample, eluent concentration, volume of the sample, and volume of eluent were investigated. Under the optimal conditions, Cu, Mn, Pb, Cd, Co, Cr, and Zn in aqueous samples were concentrated ca. 100-fold. Recoveries were obtained by the proposed method in the range of 97.8-99.9%. This method was also applied for the analysis of spiked, natural waters and soil samples. The results provide strong evidence to support the hypothesis of an adsorption mechanism.  相似文献   
8.
A method was developed for the simple, selective, and sensitive spectrophotometric determination of lead in vegetables with synthesized chromogenic reagent 3-[(2,6-dibromo-4-methylphenyl)diazenyl]-4,5-dihydroxy-6-[(2,4,6-tribromophenyl)diazenyl]naphthalene-2,7-disulfonic acid (DBMTBA; 1). In 0.25 M phosphoric acid medium, which greatly increases the selectivity, lead reacts with DBMTBA to form a 1:2 blue complex, which shows maximum absorption at 646 nm. Under optimal conditions, Beer's law is obeyed over the range from 0.09 to 0.8 microg ml(-1) Pb2+, and the apparent molar absorptivity is 1.024x10(5) l mol(-1) cm(-1). The detection limit and the variation coefficient were found to be 2.09 microg ml(-1) and 1.0%, resp. The proposed method has been applied successfully for the determination of lead in vegetables (Solanum melongena fruits, tomato fruits, Ablemoschus esculentus leaves, and Daucous carota leaves) with satisfactory results.  相似文献   
9.
Analysis of ovipositor washings from virgin femaleCnaphalocrocis medinalis Guenée (Lepidoptera: Pyralidae) of Indian origin by linked gas chromatography and electroantennography indicated the presence of three electrophysiologically-active compounds. These were identified on the basis of their gas chromatographic retention times and mass spectra as (Z)-11-hexadecenyl acetate, (Z)-13-octadecenyl acetate and (Z)-13-octadecen-1-ol with (Z)-13-octadecenyl acetate present in amounts of between 0.25 and 1.5 ng per ovipositor and the other two components at less than 10% of this. Trace quantities of octadecyl acetate were identified by mass spectrometry but no electroantennographic responses were observed to this compound. Field trials conducted with a range of blends of the three electrophysiologically-active compounds showed that blends containing between 5% and 30% (Z)-11-hexadecenyl acetate in (Z)-13-octadecenyl acetate dispensed from either white rubber septa or polythene vials were more attractive to male moths than a virgin female moth. Addition of (Z)-13-octadecen-1-ol reduced attractiveness to male moths in the blends and concentrations tested.  相似文献   
10.
Hydrodynamic characteristics of two-phase inverse fluidized bed   总被引:1,自引:0,他引:1  
Hydrodynamic characteristics of a new mode of liquid-solid fluidization, termed as inverse fluidization in which low density floating particles are fluidized with downward flow of liquid, are experimentally investigated. The experiments are carried out with low density particles (<534 kg/m3) which allow high liquid throughputs in the system. During the operation, three regimes, namely, packed, semi-fluidization and fully fluidization are encountered. Empirical correlations are proposed to predict the pressure drop in each regime. A computational procedure is developed to simulate the variation of pressure drop with liquid velocity.List of Symbols Ar modified Archimedes number, d p 3 (– s)g/2 - d p particle diameter, mm - f friction factor (eq. 2) - g acceleration due to gravity, m/s2 - H total bed height, m - H c height of the column, m - Hf height of fluidized bed, m - H0 height of initial bed, m - Hp height of the packed bed, m - (p) pressure drop across the bed, N/m2 - (p) f pressure drop across fluidized bed section, N/m2 - (p) p pressure drop across the packed bed section, N/m2 - (p) sf total pressure drop in semifluidization regime, N/m2 - Re Reynolds number, d pU 1/ - Rem modified Reynolds number, d pU 1/(1– p) - U 1 superficial liquid velocity, m/s - Umf minimum fluidization velocity, m/s - Uosf onset fluidization velocity, m/s Greek Letters f voidage of fluidized bed - p voidage of packed bed - liquid viscosity, kg/ms - liquid density, kg/m3 - s particle density, kg/m3  相似文献   
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