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You want to ferment 250 kg/hr of product from a fruit that contains 50% glucose. In addition, glucose with 60% water is inserted through 25 kg/hr of the mixture. A liquor with a lot of sugar is obtained and there is a reaction in the fermentation. The reaction efficiency is 100% Do the mass balance by finding what is left of each reactant and product at the end.
Steam flows in a long, noninsulated pipe under a constant pressure of 2 bar. At the inlet of the pipe the temperature is 300 °C. Due to losses to the surroundings, the temperature at the exit of the pipe is 60 °C. Assume the surroundings to be at ..
Then determine the approximate maximum angle through which the vehicle will rotate during powered flight, assuming no drag. Discuss the result.
Terephthalic Acid. (TPA) is produced by the reaction of p-Xylene. ,(PX) and Oxygen in the presence of a catalyst and solvent (S): Process conditions are provided for the Air entering the reactor and the reactor off gas.
A charge variation with time is given in Figure P1.1.8. Draw the corresponding current variation with time.
a)Draw and label the flowchart and carry out the degree-of-freedom analysis using balances on atomic species.(b)Determine the molar flow of oxygen supplied to the boiler.
Prepare a piping diagram and calculate the pipe size as well as the required power of the pump. You need to specify the type of fittings and the pipe material for your calculations.
a. Set up and simplify the energy balance and entropy balance for this problem.
Compute the sending-end voltage, current, real power, and reactive power for the following conditions:
Devise a control system for this reactor, and draw up a preliminary piping and instrument diagram. The following points need to be considered:
If ethanol and oxygen are completely consumed in the combustion, and if the only additional product of incomplete combustion is CO, find the CO mixing ratio
Assuming adiabatic mixing and negligible changes in potential and kinetic energies, what is the equilibrium condition after mixing and what is SG for each kg of discharge steam?
The recovery of each main component in each product is to be 98%. For example, 98% of the propane in the feed stream is to appear in the propane-rich product, and 98% of the combined pentanes in the feed stream is to appear in the bottoms product ..
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