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Similarities in sizing methodologies include standard information supplied by the consumer (system volume, feed rate, etc).
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The reactor temperature, volume, reactant feed rates, and reactant concentrations may be adjusted to enable students to obtain a wide range of kinetic data.
The most proper optimization problem appears to be minimization of the reactor volume, assuming that the feed rate is fixed at its upper limit and that the VFA concentration is at its upper limit.
Table 3 Setting parameters of the BonNDTinspect system Measurement System BonNDTinspect Aerosol-liquid Ultrapure water Volume flow 3.0 ml/min Feed rate 100 mm/s Airflow 60% Test mode Half-automated Evaluation criteria 1 Wetting fraction Evaluation criteria 2 Roundness Evaluation criteria 3 Modus/cm2 Evaluation criteria 4 Mean droplet size.
A reanalysis of the present study based on treatment given, in terms of patients reaching their preoperative target volume or maximum postoperative hourly feed rate, showed no difference in outcome (data not shown).
The effects of feed tube positions, addition feed rate, intensity of mixing, initial reagent concentration and volume ratio on particle size distribution and particle morphology were investigated.
This paper reports on results of computations and measurements to determine the influence of process parameters like the cone rotational speed (6 15 Hz), the reactor volume (3 200 l), the wood-dust feed rate (1 3.5 g s−1) and the reactor temperature (550−700°C) on the product composition.
The reactor had a volume of 300 m and a feed rate of 60 75 m h−1 The ratio between the amount of electron donor added and the amount of sulfate in the reactor was around 0.4 kg/kg.
Reactor sizing represents a "point" on these operating curves and the required volume is readily determined for a specified feed rate and given reaction rates.
Apart from feed rate, the influence of volume of concentrate and current on membrane performance was evaluated to optimize current utilization.
The resulting model then predicted well the influences of jet velocity, reagent volume and stoichiometric ratios, reagent concentrations and feed rate on the product distribution.
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