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(a) Revisit Examples 2-1 through 2-3. How would your an cut in half? If it were doubled? What conversion can be CSTR? (b) Revisit Example 2-2. Being a company about to go bank What conversion can you achieve? (c) Revisit Example 2-3. What conversion could you ac Dr. Pennypincher, to spend more money to buy a 1.0 m (d) Revisit Example 2-4. How would your answers change other 3.2 m) were placed in parallel with the flow, FAQs (e) Revisit Example 2-5. (1) What would be the reactor vol were changed to 20% and 50%, respectively? (2) What if all the reactors had the same volume of 100 dm and is the worst possible way to arrange the two CSTRs and dX (f) Revisit Example 2-6. If the term Chol is 2 secor P2-14 (a) Revisit Examples 2-1 through 2-3. How would your answers change if the flow rate, Fro, were cut in half? If it were doubled? What conversion can be achieved in a 4.5 m PFR and in a 4.5 m CSTR? (b) Revisit Example 2-2. Being a company about to go bankrupt, you can only afford a 2.5 m CSTR. What conversion can you achieve? (c) Revisit Example 2-3. What conversion could you achieve if you could convince your boss, Dr. Pennypincher, to spend more money to buy a 1.0 m PFR to attach to a 2.40 CSTR? (d) Revisit Example 2-4. How would your answers change if the two CSTRS (one 0.82 m and the other 3.2 m) were placed in parallel with the flow, FAQ, divided equally between the reactors. (e) Revisit Example 2-5. (1) What would be the reactor volumes if the two intermediate conversions were changed to 20% and 50%, respectively? (2) What would be the conversions, X1, Xz, and X3, if all the reactors had the same volume of 100 dm and were placed in the same order? (3) What is the worst possible way to arrange the two CSTRs and one PFR? (f) Revisit Example 2-6. If the term Co is 2 seconds for 80% conversion, how much fluid (m/min) can you process in a 3 m reactor? Cro/* dx dX (a) Revisit Examples 2-1 through 2-3. How would your an cut in half? If it were doubled? What conversion can be CSTR? (b) Revisit Example 2-2. Being a company about to go bank What conversion can you achieve? (c) Revisit Example 2-3. What conversion could you ac Dr. Pennypincher, to spend more money to buy a 1.0 m (d) Revisit Example 2-4. How would your answers change other 3.2 m) were placed in parallel with the flow, FAQs (e) Revisit Example 2-5. (1) What would be the reactor vol were changed to 20% and 50%, respectively? (2) What if all the reactors had the same volume of 100 dm and is the worst possible way to arrange the two CSTRs and dX (f) Revisit Example 2-6. If the term Chol is 2 secor P2-14 (a) Revisit Examples 2-1 through 2-3. How would your answers change if the flow rate, Fro, were cut in half? If it were doubled? What conversion can be achieved in a 4.5 m PFR and in a 4.5 m CSTR? (b) Revisit Example 2-2. Being a company about to go bankrupt, you can only afford a 2.5 m CSTR. What conversion can you achieve? (c) Revisit Example 2-3. What conversion could you achieve if you could convince your boss, Dr. Pennypincher, to spend more money to buy a 1.0 m PFR to attach to a 2.40 CSTR? (d) Revisit Example 2-4. How would your answers change if the two CSTRS (one 0.82 m and the other 3.2 m) were placed in parallel with the flow, FAQ, divided equally between the reactors. (e) Revisit Example 2-5. (1) What would be the reactor volumes if the two intermediate conversions were changed to 20% and 50%, respectively? (2) What would be the conversions, X1, Xz, and X3, if all the reactors had the same volume of 100 dm and were placed in the same order? (3) What is the worst possible way to arrange the two CSTRs and one PFR? (f) Revisit Example 2-6. If the term Co is 2 seconds for 80% conversion, how much fluid (m/min) can you process in a 3 m reactor? Cro/* dx dX