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California Professional Engineers

It is now proposed that a second plant be built to process 5500 gal/h of metaxylene at the same temperature and pressure as described above. What size reactor (i.e., what volume of catalyst) is requited if conversion in the new plant is to be 46% instead of 37% Justify any assumptions made for the scale-up calculation. (Ans, 2931 ft of catalyst.) (From California Professional Engineers Exam.)... [Pg.402]

California Professional Engineers Exam Problem in which the reaction... [Pg.407]

A batch reactor is used for the brominationof p-chlorophei rl isopropyl ether. Calculate the batch reaction time. [2nd Ed P4-29] California Professional Engineers Exam Problem in which the reaction... [Pg.221]

Note ppm = parts of bromine per million parts of brominated water by weight. In dilute aqueous solutions, 1 ppm = 1 milligram per liter.) (California Professional Engineers Exam)... [Pg.272]

No gaseous products were formed by the chemical reaction. What would you conclude about the relative importance of liquid-phase diffusion and about the order of the kinetics of this reaction (California Professional Engineers Exam)... [Pg.730]

In this section, you will solve the equations for an isothermal plug flow reactor. The first problem is very simple, and is patterned after a problem on the California Professional Engineers License Examination, according to Fogler (2005). Here it is modified. You take a reactor in which components A and C are fed in equimolar amounts, and the following reaction takes place ... [Pg.118]

In most systems, the work term, IF, can be neglected (note the excq>-tion in the California Professional Engineers Exam Problem PI2-6b at the end of Chapter 12). Neglecting Wt, the energy balance becomes... [Pg.492]


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