• Non ci sono risultati.

Lab #2 Exercise

N/A
N/A
Protected

Academic year: 2021

Condividi "Lab #2 Exercise"

Copied!
2
0
0

Testo completo

(1)

Dynamics and Control of Chemical Processes

Prof. Davide Manca

Chemistry, Material and Chemical Engineering Department, “G. Natta”

Politecnico di Milano  

Lab #2

Exercise 1 

A  cylindrical  tank  with  a  section  area  A30 m2  receive  an  inlet  flowrate  of  Fi 7.5 m s3 .  The  outlet  flowrate  is  proportional  to  the  liquid  height  in  the  tank  as  follows:  Foh r,  where 

0.4s m2

r  is the resistance. The tank is in stationary conditions. 

 

1) Evaluate the height dynamics of the tank after a step disturbance on the inlet flowrate, so to  reduce it to half of the initial value. 

 

2) Evaluate  the  height  dynamics  of  the  tank  after  a  linear  decrease  of  the  inlet  flowrate  that  occurs in 30 s (i.e. ramp) so to reduce it to half of the initial value. 

   

A

h Fi

Fo    

(2)

Exercise 2

 

Two  tanks  can  be  arranged  as  shown  in  Figure  1  and  2.  In  the  second  case,  the  outlet  flowrate  from the first tank depends on the liquid height of both tanks.  

Evaluate  the  height  dynamics  of  the  two  tanks,  in  both  arrangements,  when  there  is  a  step  disturbance on the inlet flowrate so to half its initial value. 

 

A1

h1 Fi

r1

A2

h2

r2    

Figure 1: non‐interacting tanks   

 

A1

h1 Fi

r1

A2

h2 r2

 

Figure 2: interacting tanks  

   

Tank 1: 

2 1

2 1

30 m 1.2 s m A

r

  

 

Tank 2: 

2 2

2 2

50 m 0.7 s m A

r

  

 

Inlet flowrate: 

9.4 m s3

Fi   

     

Riferimenti

Documenti correlati

[r]

[r]

Initially,  the  distillation  column  is  working  in  stationary  conditions  and  in  absence  of 

Modify the parameters for the error control of the ordinary differential system by adopting a relative tolerance of 10  8 and an absolute one of 10  12 (respect to

Simulate the whole process, report the conditions of the PFR outlet, and plot the molar flow of the components versus the length of the reactor. How can the recovery of styrene

The liquid level is controlled by manipulating the liquid outlet flowrate, with a 1 bar pressure

Initially, the distillation column is working in stationary conditions and in absence of external

Implement a shutdown strategy for the C4-C5 separation column. The sequence of events