FLASH DRUM DESIGN - The University of Oklahoma

FLASH DRUM DESIGN ChE 4253 - Design I Who came up with this rule and why? What is so magic about 3 ft? (Room for demister?) Again, why 2ft? (Residence...

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FLASH DRUM DESIGN

Vertical vessel

ChE 4253 - Design I

Horizontal Vessel

FLASH DRUM DESIGN Installed Units

ChE 4253 - Design I

FLASH DRUM DESIGN Deflectors, and Diffusers

ChE 4253 - Design I

FLASH DRUM DESIGN Demisters

ChE 4253 - Design I

FLASH DRUM DESIGN Control Schemes

ChE 4253 - Design I

FLASH DRUM DESIGN Dimensions to decide D hV hL hf

ChE 4253 - Design I

FLASH DRUM DESIGN Calculations to make

F = L +V Fzi = Lxi + Vyi

yi = K i xi



xi = 1



yi = 1

i

i

zi ⎧ = x ⎪ i ⎡ V 1+ ( K − 1) ⎤ ⎪ F i ⎣ ⎦ ⇒⎨ ⇒ K z i i ⎪y = i ⎪ ⎡1 + V ( K i − 1) ⎤ F ⎣ ⎦ ⎩

ChE 4253 - Design I

Ratchford Rice Equation (look for it!!)

FLASH DRUM DESIGN Dimensions to decide

D hV hL hf

related to vapor velocity. related to vapor velocity. related to level control related to flooding

ChE 4253 - Design I

FLASH DRUM DESIGN D related to vapor velocity. Permitted velocity

K =e

v perm = K

A+ B ln Flv + C (ln Flv ) 2 + d (ln Flv )3 + E (ln Flv )4

Where do these come from ? ChE 4253 - Design I

( ρ L − ρV )

ρV

Flv =

WL WV

ρL ρV

A = −1.877478 B = −0.814580 C = −0.187074 D = −0.014523 E = −0.001015

FLASH DRUM DESIGN D related to vapor velocity.

Fvis Fdrag

Fg

Stokes Fvis = 6πμ Rd vd 1 Fdrag = CD AρV vd2 drag 2 4 Fg = ( ρ L − ρV ) g π Rd3 gravity-Buoyancy 3

Fdrag + Fvis ≈ Fdrag Fdrag >> Fvis

1 4 2 2 = Fg ⇒ CD (π RD ) ρV vd = ( ρ L − ρV ) g π Rd3 2 3

⇒ v perm = K ChE 4253 - Design I

( ρ L − ρV )

ρV

8 gRd K= 3CD

FLASH DRUM DESIGN Dimensional analysis for drag: Force is dependent on velocity, cross sectional area, density and viscosity. f a ( Fdrag , vd , A, ρV , μ ) = 0 Two nondimensional numbers:

Re =

vd A / π

μ

CD =

Fdrag 1 ρV Avd2 2

Therefore

f b (Re, CD ) = 0 Thus

CD

Î

CD =

FD 1 ρV Avd2 2

= f c (Re)

is a function of the particle Reynolds number. Î

ChE 4253 - Design I

8 gRd K= 3 f c (Re)

FLASH DRUM DESIGN But, what Rd should be used? The criteria is that 5% of the liquid is entrained.

Thus

K =e

A+ B ln Flv + C (ln Flv )2 + d (ln Flv )3 + E (ln Flv ) 4

W

ρ

; Flv = WL ρ L V V

were obtained

fitting experimental data. Therefore

D=

4

π

AD =

Demisters should take care of 4% (or less) of the 5%.

ChE 4253 - Design I

4

V

π v perm ρV

FLASH DRUM DESIGN 1 hV = 36"+ diameter of feedline 2 Who came up with this rule and why? What is so magic about 3 ft? (Room for demister?)

1 h f = 12"+ diameter of feedline 2 Again, why 2ft? (Residence Time, Failure Analysis, Other Control issues?)

hL = Finally:

V pool

π D2

or ~2 minutes residence time.

4

L = hV + h f + hL ChE 4253 - Design I

Nozzle size

FLASH DRUM DESIGN Final considerations IF

L < D

3 increase Vpool (Why???)

IF

L > D

5 Use horizontal drum (Why???)

Different design protocol: Why?

ChE 4253 - Design I