nHCl(mol)(mL/min) (mL/min) (mL/min) (min) 0.001

40 60 100 4 0.00150 50 100 4 0.00170 30 100 4 0.00180 20 100 4

ZEROn Naoh initn ETOAC inifeed Ca0 Feed Cb0 1/Ca0 XA

0.004 0.006 0.04 0.06 25 0.750.005 0.005 0.05 0.05 20 0.640.007 0.003 0.07 0.03 14.3 0.430.008 0.002 0.08 0.02 12.5 0.39

Flow-Rate of NaOH

Flow-Rate of EtOAc

Total Flow-Rate

Space time, τ

Fractional Conversion

, x

10 12 14 16 18 20 22 24 260.00

0.10

0.20

0.30

0.40

0.50

0.60

0.70

0.80

f(x) = 0.0301449227735787 x + 0.0105241537955966R² = 0.988064472665757

ZERO

-3.30 -3.20 -3.10 -3.00 -2.90 -2.80 -2.70 -2.60 -2.50 -2.40

-5

-4.5

-4

-3.5

-3

-2.5

-2

-1.5

-1

-0.5

0

f(x) = 2.32145787602624 x + 2.90157980371468R² = 0.99495583205169

first

VNaOh nNaOh titreted nNaOh unreacted Cnaoh,f X9 0.0009 0.0001 0.01 0.75

8.2 0.00082 0.00018 0.018 0.646 0.0006 0.0004 0.04 0.43

5.1 0.00051 0.00049 0.049 0.39

FIRST secondLN Cao ln Ca xa/(1-xa) Cao

-3.22 -4.60517018598809 3.00 0.04-3.00 -4.01738352108597 1.78 0.05-2.66 -3.2188758248682 0.75 0.07-2.53 -3.01593498087151 0.63 0.08

-3.30 -3.20 -3.10 -3.00 -2.90 -2.80 -2.70 -2.60 -2.50 -2.40

-5

-4.5

-4

-3.5

-3

-2.5

-2

-1.5

-1

-0.5

0

f(x) = 2.32145787602624 x + 2.90157980371468R² = 0.99495583205169

first

0.50 1.00 1.50 2.00 2.50 3.00 3.500

0.01

0.02

0.03

0.04

0.05

0.06

0.07

0.08

0.09

f(x) = − 0.0158504887825416 x + 0.0844114599773072R² = 0.91337992332503

second

0.50 1.00 1.50 2.00 2.50 3.00 3.500

0.01

0.02

0.03

0.04

0.05

0.06

0.07

0.08

0.09

f(x) = − 0.0158504887825416 x + 0.0844114599773072R² = 0.91337992332503

second