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Develop project plans for the design and construction of the following processes. Use Figure 1.2 as a guide to the activities that must occur. Estimate the overall time required from launching the project to the start of operation.
a. A petrochemical process using established technology, to be built on an existing site.
b. A process for full scale manufacture of a new drug, based on a process currently undergoing pilot plant trials.
c. A novel process for converting cellulose waste to fuel products.
d. A spent nuclear fuel reprocessing facility.
e. A solvent recovery system for an electronics production facility.
in gas-shy-solid fluidization it is frequently common to have a wide size distribution of particles present in the
determine the diode current and voltage and the power delivered by the voltage source. The diode characteristic is given in Figure P7.2.14 (b).
Compute the mean and variance for each of the following activities: Activit y A B C D E F G H I J Optimisti c 5 3 18 9 8 1 45 12 7 22 Pessimisti c 10 21 32 11 8 10 95 15 11 80 Most Likely 7 15 25 10 8 6 60 13 9 60
Draw T-S diagram of the cycle.
The doctor wants to find out the exact time at which the concentration of this antibiotic in the blood peaks in the patient. Determine this time and the concentration of the antibiotic in the blood stream at this time.
What temperature will be indicated by the thermocouple? Assume free convection from the thermocouple.
Design a reactor to remove 1% acetylene from ethylene in a plant that produces 1.5 million metric tons per year of ethylene using this catalyst.
Use the three-element Kelvin model to describe the stress relaxation of a biomaterial of your choice. Using a stress response curve from the literature, compute the model spring constants K1 and K2 and the viscous damping coefficient b.
Calculate the theoretical stages needed to separate a 10 mole% ethanol liquid saturated feed into a 80 mole% distillate and a 0.1 mole% bottoms at 1 atmosphere pressure.
Low pressure steam at 120 °C is available as a heat source. The evaporator is run under a slight vacuum, such that the temperature of the boiling apple juice concentrate is maintained at 100 °C.
In a specific rectification process , operating on ethanol and water mixtures, the vapor and liquid streams entering and leaving the column are those given in the table ethanol water mole% moles liquid entering top 75.1 24.9 liquid leaving bottom ..
A paper by Ruckenstein and Tsai (1981)* shows that an "optimum pore size" can exist for catalytic reactions of large solute molecules in solvent-filled pores. Obtain the paper from your library and read it carefully. Then derive the analytical equati..
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