- Với các tham số vận hành thực tế

- Với các tham số vận hành thực tế hiện tại, hệ số ngập lụt f=0.8713 nhỏ hơn rất nhiều so với 1.2 và cũng lớn hơn 0.7. Đảm bảo cho tháp vận hành bình thường không bị ngập lụt, song nó cũng cho thấy S1 và S1 cũng không quá lớn.
- Khi thay đổi lưu lượng dòng hơi, hệ số ngập lụt thay đổi theo đặc tính như hình 8. Khi đó giới hạn điều chỉnh cho phép khả năng không bị ngập lụt là Qv(max)

Results (English) 1:

-With the actual operating parameters are present, the flood f = 0.8713 smaller than 1.2 and also greater than 0.7. Ensuring normal operation of towers is not flooded, but it also showed that S1 and S1 is not too big.
-When changing the flow somewhat, coefficient of frequency change according to characteristics such as Figure 8. When that limit is adjusted to allow non-flooded the Qv (max)/s. 10m3
<-however should not adjust Qv 5 m 3/s, since < then the coefficient f reach 0.7 to ensure design standards for the distillation Tower is the coefficient S1l/S1 ≈ 1.
-Survey with current operating parameters as necessary supplemented the disc filter parsing capabilities and enhance the purity of the substance. Then the distance between the disc off T = 60 cm (fig. 9). To make sure not flooded, then steam flow controlled, then the limit from 6-9m3/s
-In brief flooding of distillation towers are judged by the size of the Tower, the geometry of the line somewhat, the liquid flows out of the tower. Through the modeled the Tower will evaluate the impact the reciprocity between the operating parameters to the ability to operate the tower. Help for the officers operations and design tuning parameters are appropriate to ensure the system works safely and efficiently.

Results (English) 2:

- With the actual operating parameters present, flooding coefficient f = 0.8713 is much smaller than 1.2 and greater than 0.7. Make sure the tower does not operate normally flooded, but it also shows that S1 and S1 is not too large.
- When changing the gas flow, flooding coefficients vary with characteristics as shown in Figure 8. then allows limited adjustment capability is not flooded qv (max) <10m3 / s.
- however should not adjust qv <5m3 / s, because whereas the asymptotic values ​​f 0.7 to ensure the design criteria for disc distillation S1l/S1 coefficient ≈ 1.
- Surveying the current operating parameters as needed to add additional disks to increase filtration and separation capabilities enhance the purity of the substance. Then reduce the distance between the disk T = 60 cm (Figure 9). To ensure that no traffic is flooded then be adjusted slightly limited from 6-9m3 / s
- summary flooding phenomenon distillation tower was assessed by parameters tower geometry, flow vapor, liquid flow in the tower. Through modeling the tower will evaluate the interaction between the operational parameters to the performance pyramid. Help for staff to operate and adjust design parameters to ensure proper working system to work safely and efficiently.