Optimum Result (optimum + result)

Distribution by Scientific Domains


Selected Abstracts


Improving the nutritional quality and maintaining consumption quality of akara using curdlan and composite flour

INTERNATIONAL JOURNAL OF FOOD SCIENCE & TECHNOLOGY, Issue 8 2006
Minerva A. Plahar
Summary Soybean flour and curdlan were incorporated into cowpea flour to determine their effect on lowering the fat content and on the physical properties of akara. At 20% substitution, soybean flour lowered the fat content of akara by 7.7% and increased the protein content by 28.7% without significantly affecting the firmness or the colour of akara. Addition of 1% curdlan decreased the fat content by 32.2% but significantly increased the firmness of akara and produced a darker-coloured product. The paste moisture content of akara containing 20% soybean flour and 1% curdlan was modified to obtain product characteristics comparable with the control (100% cowpea flour) while maintaining a lower fat content. Optimum results were obtained for paste with 63% moisture content. Firmness of this modified product was similar to the control and the fat content was lower (17%) compared with the control (26%). [source]


Double-deck aerated biofilm membrane bioreactor with sludge control for municipal wastewater treatment

AICHE JOURNAL, Issue 5 2009
Jirachote Phattaranawik
Abstract Alternative designs of an aerated moving-bed biofilm reactor and a flat-sheet membrane module for a biofilm membrane bioreactor process have been investigated to overcome a membrane clogging problem and to determine the performance of a new membrane module. Double-deck aerated biofilm reactor with integrated designs of sludge hopper, thickener, and velocity-zone concept for particle settlement was evaluated for the suspended solid control and removal. Hydrodynamics of bubbling, liquid, and solid particles were arranged in the bioreactor to obtain a particle settlement. New membrane modules used under low suspended solid environment having smaller membrane gaps were evaluated for filtration performance and clogging problems for long-term operation. The average suspended solids concentration in the bioreactor effluent was 44.6 mg/L. Relaxation applied with the membrane module provided the most optimum result for fouling control, and no clogging problems in the modules were observed in the system after continuous operation of 3 weeks. © 2009 American Institute of Chemical Engineers AIChE J, 2009 [source]


Non-linear stability in the Bénard problem for a double-diffusive mixture in a porous medium

MATHEMATICAL METHODS IN THE APPLIED SCIENCES, Issue 16 2001
S. Lombardo
The linear and non-linear stability of a horizontal layer of a binary fluid mixture in a porous medium heated and salted from below is studied, in the Oberbeck,Boussinesq,Darcy scheme, through the Lyapunov direct method. This is an interesting geophysical case because the salt gradient is stabilizing while heating from below provides a destabilizing effect. The competing effects make an instability analysis difficult. Unconditional non-linear exponential stability is found in the case where the normalized porosity , is equal to one. For other values of , a conditional stability theorem is proved. In both cases we demonstrate the optimum result that the linear and non-linear critical stability parameters are the same whenever the Principle of Exchange of Stabilities holds. Copyright © 2001 John Wiley & Sons, Ltd. [source]


Mathematical model for mixing index in gas,solid fluidized bed: an analysis

ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, Issue 4 2010
Abanti Sahoo
Abstract An available theoretical model for mixing index in gas-solid fluidized bed has been analyzed for further modification and improvement. Assumption of 50% bed material moving in the upward direction and rest 50% in the downward direction considered for the above model (the counter-flow circulation model) has been analyzed for optimum result. A computer program was run for different bed conditions by varying operating parameters, namely, the mixture composition, fractions of bed materials, minimum fluidization velocity of the jetsam particles and that of the bed materials (i.e. mixture of the jetsam and the flotsam particles). The developed model was solved by finite difference (central differencing). Fraction of the bed material moving in the upward direction was varied from 0 to 100% and the minimum fluidization velocity was varied within the Umf of the flotsam to that of the jetsam particles (i.e. 0.465,1.0335 m/s). Optimum fraction of bed materials with respect to its distribution (as per the earlier proposed model) in the upward and downward streams during the fluidization process was found to be 20 and 80%, respectively. The modified model was validated by conducting experiments on fluidization and studying the mixing characteristics of regular homogeneous materials (sago) in a 15 × 100 cm cylindrical column. Fairly good agreement was observed between the values of mixing index obtained from the proposed modified model and the experimental observations. Copyright © 2009 Curtin University of Technology and John Wiley & Sons, Ltd. [source]


Pollutant Emissions Management in an Existing Plant: The CHF3 Case,

CHEMICAL ENGINEERING & TECHNOLOGY (CET), Issue 2 2005
M. N. Pantzali
Abstract Changing production patterns towards waste reduction in a globalizing world can be considered a starting point towards sustainable development. The aim of the chemical plant designer is to reduce pollutant emissions, not by cleaning the effluents but by diminishing the production of the undesirable compounds. The case study examined is focused on reducing the CHF3 emission of an existing difluorochloromethane (HCFC-22) plant by allocating the source of the problem and trying to decrease byproduct emissions by reducing their production. The effect of the operating conditions on the formation rate of both the product and the byproduct of the plant is studied and it is proved that the optimum result is accomplished simply by reducing the residence time in the fluorination reactor, that is, without the need for extra investment and/or energy consumption, a solution highly desirable from an economic point of view. The results of the study were applied to an existing plant leading to 50,% reduction of the CHF3 emissions. [source]