• Ei tuloksia

0 dt Bx

N/A
N/A
Info
Lataa
Protected

Academic year: 2022

Jaa "0 dt Bx"

Copied!
2
0
0

Kokoteksti

(1)

CHEM-E7130 Process modeling Exam 22.10.2020

Remote exam instructions sent separately, please follow those!

Please give written feedback to the course. Such feedback that may lead to improvements to the course could lead to an extra point.

5 p max in each question

1. Your task is to model mass transfer from dissolving solid particles into liquid in a stirred tank operated batch-wise. You can assume that heat transfer is very efficient, so that the vessel remains at a constant temperature (heating fluid temperature). Which balances and which constitutive equations you would need at minimum? What kind of model results in (mathematically)? Explain how you would 1) verify and 2) validate your model performance. Maximum answer length is half page (with text editor).

2. Consider the following second order differential equation:

0 dt Bx

A dx dt

x d

2

2 + + =

where A and B are constants. Write it as a system of first order differential equations

( )

=

[ ] ( )

dt d

(where ( ) and [ ] are a vector and a matrix that you need to solve) by making a substitution

dt

y

=

dx

. How can you evaluate stability of the original system from the matrix [ ]?

(2)

3. Find out if there is something wrong in the following equations and if needed correct them based on dimensional and physical arguments. Symbols and their dimensions for these equations are given below. Explain shortly in words what the equation describes.

a)

1 E

0

exp k L

V

 

− =   −   a

b)

n

n 1 n

c

c c dc t

+ = +

dt

Symbols

a specific surface area (m2/ m3)

c concentration (mol/m3)

D diffusion coefficient (m2/s)

E efficiency ()

J diffusion flux (mol/m2s)

k mass transfer coefficient (m/s)

L characteristic length (m)

N mass transfer flux (mol/m2s)

r reaction rate (mol/m3s)

T temperature (K)

t time (s)

v velocity (m/s)

V volume (m3)

x space coordinate (m)

y mole fraction ()

ρ density (kg/m3)

λ thermal conductivity (W/mK)

µ dynamic viscosity (Pas = kg/ms)

Viittaukset

LIITTYVÄT TIEDOSTOT

[r]

Prove that the collection of disjoint (pistevieras) open sets in R n is either finite or countable.. Prove

[r]

(2010) Solid phase extraction of organic compounds in atmospheric aerosol particles collected with the particle-into-liquid sampler and analysis by liquid

• RSSI requires precise channel behavioral model TOA/TDOA in the

At present, the pathogens are very unlikely to transfer to suitable hosts since the only possible vector species that is present in Finland (S. mali) is unlikely to act as a

• The total pipe length between the stirred suspension tank and the preparation tank is x.xx m and the concentrator is x.xx m higher than the stirred tank (the presence of

• The total pipe length between the stirred suspension tank and the preparation tank is x.xx m and the concentrator is x.xx m higher than the stirred tank (the presence of