Bonus
A fluidized bed can be used as one of these devices to allow for more uniform particle mixing compared to a packed bed. For 10 points each:
[10m] Name these devices that have “batch” and “continuous stirred-tank” varieties, the latter of which can achieve steady state by receiving reagents (“re-AGE-ints”) at an inlet and expelling products at an outlet.
ANSWER: chemical reactors [accept continuous stirred-tank reactors; accept vat reactors or backmix reactors or mixed flow reactors or continuous-flow stirred-tank reactors; accept batch reactors; accept packed bed reactors; accept fluidized bed reactors; accept reaction vessels; prompt on process vessels; prompt on CSTRs or CFSTRs]
[10h] Continuous stirred-tank reactors can be modelled using a “control” form of this quantity, which is minimized by cascading reactors in series. Residence time equals mass or this quantity divided by the appropriate flow rate.
ANSWER: volume [accept control volume; prompt on V or CV]
[10e] The goal of designing highly efficient reactors is primarily to maximize this quantity, the amount of actual product produced divided by the theoretical maximum.
ANSWER: yield [accept theoretical yield; accept actual yield; accept percent yield]
<Editors, Chemistry>
| Editions | Heard | PPB | Easy % | Medium % | Hard % |
|---|---|---|---|---|---|
| 2 | 38 | 11.05 | 61% | 21% | 29% |
Conversion
Summary
| Tournament | Edition | Exact Match? | Heard | PPB | Easy % | Medium % | Hard % |
|---|---|---|---|---|---|---|---|
| UK (South) | UK | Y | 1 | 20.00 | 100% | 0% | 100% |
| Eastern Canada (2) | US | Y | 1 | 10.00 | 100% | 0% | 0% |
| Upper Mid-Atlantic | US | Y | 12 | 10.00 | 58% | 8% | 33% |
| Midwest | US | Y | 1 | 30.00 | 100% | 100% | 100% |
| Northeast | US | Y | 12 | 10.00 | 50% | 25% | 25% |
| Pacific | US | Y | 9 | 10.00 | 56% | 33% | 11% |
| Southeast | US | Y | 1 | 10.00 | 100% | 0% | 0% |
| Upstate NY | US | Y | 1 | 20.00 | 100% | 0% | 100% |