Chemical Question due in 12 hours
maryalt_
AcrylicAcidecampus.xlsmBase
| Prop feed | Air feed | Steam feed | Reactor feed | Reactor Out | Flash top | Flash bottom | Dist top | Dist bot | |
| 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | |
| propylene | 5.00 | 0.00 | 0.00 | 5.00 | 2.50 | 2.50 | 0.00 | 0.00 | 0.00 |
| oxygen | 0.00 | 11.55 | 0.00 | 11.55 | 7.32 | 7.32 | 0.00 | 0.00 | 0.00 |
| acrylic | 0.00 | 0.00 | 0.00 | 0.00 | 2.34 | 0.47 | 1.87 | 1.87 | 0.00 |
| water | 0.00 | 0.00 | 40.00 | 40.00 | 42.82 | 8.56 | 34.25 | 0.00 | 34.25 |
| co2 | 0.00 | 0.00 | 0.00 | 0.00 | 0.48 | 0.48 | 0.00 | 0.00 | 0.00 |
| nitrogen | 0.00 | 43.45 | 0.00 | 43.45 | 43.45 | 43.45 | 0.00 | 0.00 | 0.00 |
| TOTAL | 5.00 | 55.00 | 40.00 | 100.00 | 98.91 | 62.78 | 36.13 | 1.87 | 34.25 |
| propylene | 5 | ||||||||
| air | 55 | ||||||||
| steam | 40 | ||||||||
| T, reactor | |||||||||
| Selectivity | 4.9 | ||||||||
| Conversion | 0.5 | ||||||||
| water vapor | 0.2 | ||||||||
| acrylic vapor | 0.2 | ||||||||
| ξ1 | 2.3407643312 | ||||||||
| ξ2 | 0.1592356688 | ||||||||
Recycle
| Prop feed | Air feed | Steam feed | Feed mix | Reactor Feed | Reactor Out | Flash top | Recycle | Recycle' | Purge | To dist | ||||
| 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 8' | 9 | 10 | error | MW | ||
| propylene | 5.00 | 0.00 | 0.00 | 5.00 | 5.52 | 5.25 | 5.25 | 0.52 | 0.52 | 4.72 | 0.00 | 0.00 | 42 | |
| oxygen | 0.00 | 11.55 | 0.00 | 11.55 | 12.78 | 12.34 | 12.34 | 1.23 | 1.23 | 11.11 | 0.00 | 0.00 | 32 | |
| acrylic | 0.00 | 0.00 | 0.00 | 0.00 | 0.01 | 0.27 | 0.05 | 0.01 | 0.01 | 0.05 | 0.22 | 0.00 | 72 | |
| water | 0.00 | 0.00 | 40.00 | 40.00 | 40.82 | 41.12 | 8.22 | 0.82 | 0.82 | 7.40 | 32.89 | 0.00 | 18 | |
| co2 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.03 | 0.03 | 0.00 | 0.00 | 0.03 | 0.00 | 0.00 | 44 | |
| nitrogen | 0.00 | 43.45 | 0.00 | 43.45 | 48.28 | 48.28 | 48.28 | 4.83 | 4.83 | 43.45 | 0.00 | 0.00 | 14 | |
| TOTAL | 5.00 | 55.00 | 40.00 | 100.00 | 107.42 | 107.29 | 74.18 | 7.42 | 7.42 | 66.76 | 33.11 | 0.00 | ||
| propylene | 5 | T | 0.1 | 0.2 | 0.3 | 0.4 | 0.5 | 0.6 | 0.7 | 0.8 | 0.9 | |||
| air | 55 | 200 | $ (75.22) | $ (74.72) | $ (74.11) | $ (73.39) | $ (72.56) | $ (71.59) | $ (70.48) | $ (69.20) | $ (67.75) | |||
| steam | 40 | 250 | $ (74.29) | $ (73.62) | $ (72.79) | $ (71.72) | $ (70.34) | $ (68.57) | $ (66.27) | $ (63.32) | $ (59.55) | |||
| 300 | $ (68.71) | $ (67.35) | $ (65.64) | $ (63.43) | $ (60.48) | $ (56.45) | $ (50.82) | $ (42.83) | $ (31.44) | |||||
| T, reactor | 250 | 350 | $ (58.72) | $ (56.37) | $ (53.49) | $ (49.85) | $ (45.09) | $ (38.59) | $ (29.31) | $ (15.46) | $ 5.87 | |||
| Selectivity | 10 | 400 | $ (46.58) | $ (43.46) | $ (39.77) | $ (35.31) | $ (29.76) | $ (22.56) | $ (12.71) | $ 1.66 | $ 24.13 | |||
| Conversion | 0.05 | 450 | $ (35.55) | $ (32.17) | $ (28.32) | $ (23.87) | $ (18.63) | $ (12.33) | $ (4.42) | $ 6.09 | $ 21.23 | |||
| water vapor | 0.2 | 500 | $ (28.23) | $ (25.09) | $ (21.63) | $ (17.78) | $ (13.46) | $ (8.56) | $ (2.90) | $ 3.84 | $ 12.25 | |||
| acrylic vapor | 0.2 | 550 | $ (29.04) | $ (26.71) | $ (24.21) | $ (21.51) | $ (18.58) | $ (15.40) | $ (11.91) | $ (8.05) | $ (3.73) | |||
| Recycle Ratio | 0.1 | 600 | $ (29.67) | $ (27.75) | $ (25.72) | $ (23.56) | $ (21.27) | $ (18.82) | $ (16.20) | $ (13.39) | $ (10.36) | |||
| 650 | $ (29.80) | $ (28.00) | $ (26.10) | $ (24.08) | $ (21.95) | $ (19.69) | $ (17.28) | $ (14.73) | $ (12.00) | |||||
| ξ1 | 0.2673320264 | |||||||||||||
| ξ2 | 0.0089110675 | |||||||||||||
| propylene | 79 | $/kmol | ||||||||||||
| acrylic acid | 108 | $/kmol | ||||||||||||
| feed cost | 395 | |||||||||||||
| product value | 24 | |||||||||||||
| profit/kmol | -74.29 |
Reactor Info
| T | S | X | |
| 200 | 10.0 | 0.04 | |
| 250 | 10.0 | 0.05 | |
| 300 | 9.77 | 0.11 | |
| 350 | 8.91 | 0.22 | |
| 400 | 7.24 | 0.36 | |
| 450 | 4.90 | 0.5 | |
| 500 | 2.45 | 0.63 | |
| 550 | 0.891 | 0.76 | |
| 600 | 0.655 | 0.83 | |
| 650 | 0.610 | 0.85 | |
| S | X | ||
| 250 | 2 | 10 | 0.05 |
S 200.0 250.0 300.0 350.0 400.0 450.0 500.0 550.0 600.0 650.0 10.0 10.0 9.77 8.91 7.24 4.9 2.45 0.891 0.655 0.61
X 200.0 250.0 300.0 350.0 400.0 450.0 500.0 550.0 600.0 650.0 0.04 0.05 0.11 0.22 0.36 0.5 0.63 0.76 0.83 0.85
