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Problem 1 – Unsteady state equimolar counter diffusion in gases Problem Statement: Two bulbs A (V 1 ) and B (V 3 ), which initially contain pure gases A and B at 1 atm, are connected by a tube (V 2 ) of length 5 cm and the internal diameter of 0.4 cm. After 1 hr, the partial pressure of gas A in bulb A (V 1 ) drops to 0.75 atm while its corresponding partial pressure in bulb B (V 3 ) is 0.3 atm. The temperature is constant at 25 o C. If the volume of bulb A is 1 liter, determine: A) The partial pressure of A in bulb B after very long time B) The diffusivity of A in B

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  • Problem 1 Unsteady state equimolar counter diffusion in gases

    Problem Statement:

    Two bulbs A (V1) and B (V3), which initially contain pure gases A and B at 1 atm, are connected by a tube (V2) of length 5 cm and the internal diameter of 0.4 cm. After 1 hr, the partial pressure of gas A in bulb A (V1) drops to 0.75 atm while its corresponding partial pressure in bulb B (V3) is 0.3 atm. The temperature is constant at 25

    oC. If the volume of bulb A is 1 liter, determine:

    A) The partial pressure of A in bulb B after very long time

    B) The diffusivity of A in B

  • Problem 1 Unsteady state equimolar counter diffusion in gases

    Known:

    Two pure gases A and B at 1 atm placed in two separate bulbs connected by a tube of known length and diameter

    Initial partial pressure of gas A in bulb 1 (1 atm) and 3 (0 atm), and partial pressure of gas A in bulb 1 (0.75 atm) and 3 (0.3 atm) after 1 hour

    Volume of bulb 1 (1 L) and constant temperature (25 oC)

    Diameter of the connecting tube (0.4 cm) and length (5 cm)

    Find:

    A) Partial pressure of A in bulb 3 after very long time (pA at t=)

    B) Diffusivity of A in B (DAB)

  • Assumptions:

    1) Applicability of Ideal Gas Law

    2) Equimolar counter diffusion at any time

    3) Pseudo steady state diffusion in the tube

    4) Negligible tube volume compared to bulb volumes

    5) Constant total concentration, temperature, and pressure

    6) Constant diffusivity DAB 7) Well mixed V1 and V3

    Problem 1 Unsteady state equimolar counter diffusion in gases

  • Schematic:

    Problem 1 Unsteady state equimolar counter diffusion in gases

  • A) The partial pressure of gas A in bulb 3 after a very long time.

    Moles are conserved throughout the system.

    1 = 1|=1 + 2|=1 + 3|=1

    1 1

    =1|=11

    +

    2|=12

    +3|=13

    1 1 = 1|=11 + 3|=13

    Check difference in volumes:

    1 = 1 2 = 2

    4 3 =?

  • A) The partial pressure of gas A in bulb 3 after a very long time.

    Was it safe to neglect tube volume?

    2 = (0.004)2

    40.05

    1000

    13

    2 = 6.28 104

    Since V2

  • A) The partial pressure of gas A in bulb 3 after a very long time.

    At = the system will have reached equilibrium, therefore will be constant throughout.

    1|= = 2|= = 3|= = |=

    1 1 = |=1 + |=3

    1 1 = |=(1 + 3)

    |= =1 1

    (1 + 3)

    |= =(1)(1)

    (1 + 0.83)

    |= = 0.55

  • A) The partial pressure of gas A in bulb 3 after a very long time.

    Figure A.1 - Partial pressure profile gradient along z at various times

  • B) Diffusivity of A in B (DAB).

    = , , (. )

    3, 3, = 3,

    3, = 3,

    = 3,3,2 = 3,2 (. )

    3, = 3,3,2

    2 = 3,3, 22

    = 3,3,2 = 3,2 (. )

    General transient mole balance of species i inside

    CV j, no gen/cons:

    3

    =(33)

    = 3

    3

    Knowing that:

    Integrating B.3 over the constant CV area of the inlet cross sectional area of tube outlet:

    Knowing that: 3 = 33

    And that: 3 ()

    Then:

    Knowing that in equimolar counter diffusion: 3, = 3,

    Then substituting B.5 back into B.4:

    3, 3, + 3,3,

    = 3,

    + 3, 3, + 3,

    = 3,

    (. )

    3, = 3,

    2

    33

    = 3,

    2(. )

  • 2 = 0 = 1

    0 + 2 2= 2 = 0 = 1

    2

    = 0 =(

    2 )

    2= 1 =

    2

    2= 1

    + 2

    2

    +2

    = 0

    33

    = 3,

    2 = 3,2(. )

    Problem: we cannot solve this PDE simply

    Solution: perform new balance with CV of the tube and solving for the flux

    Recall the Continuity Equation from Transport Phenomena with a 1-D

    cylinder (axial diffusion only):

    Another Problem: we cannot solve this PDE simply neither!

    Another Solution: HOWEVER, the tube volume V2 is so insignificant relative to the bulb volumes, one may assume pseudo-steady state and thus neglect any accumulation of species in the tube!

    2

    = 0 Since , then is constant! 2

    Integrating and replacing our flux for Ficks First Law to get the concentration as a function of position z:

    Solving for both boundary conditions given after 1 hour and using the assumption of well mixed bulb volumes:

    BC 1:

  • 2 = = 1

    + 2 1=

    2 = 1

    = (3 1)

    33

    = 3,2 = 12 = (3 1) 2

    33

    = 3 1 2

    3

    3

    = 3 1 2

    3 1 2

    =

    3 3 3

    12

    =

    3(1 + 31

    ) 2

    BC 2:

    33

    = 3,

    2 = 3,2 (. ) Recall:

    Substituting K1 into B.6:

    Realizing =

    and that T is constant:

    Yet another problem: cannot integrate both & since both are time dependent 3 1

    Yet another solution: find in terms of 1 3

    Noting that: = 11 + 33 Then: 1 = 3 3

    1

    Thus:

    33

    = 3

    1 + 31

    2

    (. )

  • 3

    3(1 + 31

    )

    3

    3

    = 23

    0

    = 3

    11 + 32

    ln3

    1 + 31

    33

    = 3

    1 + 31

    2

    (. )

    Equation B.7 is now a simple separable variable/first-order DE ready to be solved. Knowing the BCs corresponding to the respective time, and after rearranging for DAB:

    11 + 3

    ln 3

    1 + 31

    3 1 + 3

    1

    = 23

    = (0.83

    1 3

    1000 )(0.05 )1

    1 + 0.83

    0.004 2

    4 (3600 )ln

    (0.3 )1 + 0.83

    1 1

    1

    = 3.99 104

    2

    THE END!