Why should chemical equation be balanced?
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What is the purpose of capacitor? What does capacitor load means? How does it connect?
REACTION ENGINEERING - EXAMPLE 13.2 : A batch reactor is designed for the system of the irreversible, elementary liquid-phase hydration of butylene oxide that produces butylene glycol. At the reaction temperature T = 323 K, the reaction rate constant is k = 0.00083 L / (mol - min). The initial concentration of butylene oxide is 0.25 mol / L = Ca. The reaction is conducted using water as the solvent, so that water is in large excess. (a) Let the molecular weight of water is 18 g / mol and the mass of 1 kg in 1 L of water, calculate the molar density of water, Cb in the unit of mol / L. (b) Determine the final conversion, X of butylene oxide in the batch reactor after t = 45 min of reaction time. Use the formula X = 1 - 1 / exp [ kt (Cb) ] derived from material balance. (c) Find the equation of t as a function of X.
what are the reaction between sodium meta bi sulphate and chlorine?
What is some common piping materials used to transport slurries?
UNIT OPERATION - EXAMPLE 9.1 : Which of the sequence below represent a feasible flows of ethanol processing plants using cellulose as starting material? A. raw material -> heat exchanger -> distillation column -> reactor. B. reactor -> distillation column -> raw material -> heat exchanger. C. heat exchanger -> raw material -> distillation column -> reactor. D. raw material -> heat exchanger -> reactor -> distillation column. E. distillation column -> raw material -> reactor -> heat exchanger.
why distillation of water takes more time than toluene ,eventhough the later boiling point is more than water ?
cetane no. and sulphur required in diesel fuel for euro-IV
What is Pinch Technology?
when liquid stored in spherical vessel,equilibrium shift towards liquid.what is the benefit of it?
Name some guidelines for designing for liquid and gas velocities in process plant piping?
What parameters should be considered while selecting type of filter?
What is a good way to get started in doing a plant-wide steam consumption analysis?