Day 2 Equations Flashcards

1
Q

Calderwood Equation

A

%C = 5.88 + 2.206(CV - 0.094S) + 0.0053 [80 - 100(VCM/FC)]^1.55

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
2
Q

equilibrium at stage 2 countercurrent extraction

A

y_2 = (L/V)(x_1 - x_N) + y_N+1

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
3
Q

amount of A in raffinate n

A

A,Rn = A,F [B/(KD*S + B)]^n ; applicable if S fed in each stage are equal

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
4
Q

Tiller-Tour Equation

A

N - 1 = log[(x_1 - y_2)/(x_N - y_N+1)] / log [(x_1 - x_N)/(y_2 - y_N+1)]

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
5
Q

Raoult’s Law & Dalton’s Law

A

Pi = Pi*xi ; P_T = ΣPi

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
6
Q

relative volatility

A

α_AB = [y_A(1 - x_A)] / [x_A(1 - y_A)]

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
7
Q

Rayleigh Equation

A

ln(A_1/A_2) = (α_AB)[ln(B_1/B_2)] ; A_1 B_1 = from feed, A_2 B_2 = from residue

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
8
Q

flash distillation slope & the fraction of F that vaporized

A

y = (x_F)/f - [(1-f)/f]x, f = V/F

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
9
Q

theoretical O2

A

O2,theo = C + H/4 + S - O2

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
10
Q

free O2

A

O2,free = O2,xs + CO/2 + H2/2

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
11
Q

supplied O2

A

O2,supp = O2,theo + O2,xs = N2,supp(21/79)

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
12
Q

dry basis (db) vs wet basis (wb)

A

db -> (A/H2O)100 ; wb -> [A/(A+H2O)]100

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
13
Q

amount of H2O, CO2 and CO produced from combustion

A

H2O = H/2 ; CO2 + CO = C_total

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
14
Q

octane number

A

[C8H18/(C8H18+C7H16)]*100 , variables in unit volume

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
15
Q

cetane number

A

[C16H34/(C16H34+C11H10)]*100 , variables in unit volume

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
16
Q

H & O from ultimate analysis(UA) ; net H if UA is given

A

H = netH + (M + CW)(2/18) ; O = (M + CW)(16/18) ; net H = H - O/8

17
Q

Ruth Equation, Filter Medium Resistance(Rm)

A

E18-59 but P = -ΔP, w = C and r = Rm (also multiply P to gc)
Rm = (αCVe)/A, (***if Rm or Ve not given, both and θe = zero)
C = concentration = Mc/V

18
Q

Constant Pressure Filtration eqn, θe, K

A

(V + Ve)^2 = K(θ + θe), θe = (Ve^2)/K, K =2(-ΔP)gc(A^2)/(μαC)

19
Q

rw of: Plate and Frame Filter, Leaf Filter

A

rw = rf/4 (default), rw = rf

20
Q

Constant Rate Filtration, (-ΔP), K, β

A

-ΔP = KrV + β, Kr = [(μαC)/(gcA^2)](Vr/θr), β = KrVe

21
Q

Constant Pressure Filtration PRECEDED by Constant Rate Filtration, K

A

(V^2 - Vr^2) + 2Ve(V - Vr) = K(θ - θr), K = 2Vr*(Vr + Ve)/θr

22
Q

Relationship of height of solids(Lo) vs porosity(Ɛ) in fluidization

A

inversely proportional (L ∝ 1/(1-Ɛ) )

23
Q

Pressure drop for fluidization

A

-ΔP/L = (1 - Ɛ)(ρp - ρ)g/gc

24
Q

Equation used in getting minimum fluidizing velocity

A

Ergun Equation (E17-1)

25
Q

screen effectiveness

A

E = (xP/xF)[(xF-xR)/(xP-xR)]{1-[(1-xP)/(1-xF)][(xF-xR)/(xP-xR)]}