Kinetics and Mechanisms of hydrogenation of DMO

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Kinetics and Mechanisms of hydrogenation of DMO. Li Siming 2012.9.8. C. Perego, S. Peratello, Catalysis Today 1999, 52 , 133-145. Internal Diffusion Effects. 当. 小于 0.1(0.15) 时,可认为无内扩散影响。. External Diffusion Effects. C. Perego, S. Peratello, Catalysis Today 1999, 52 , 133-145. 当. - PowerPoint PPT Presentation

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Kinetics and Mechanisms of hydrogenation of DMO

Li Siming2012.9.8

10~20 目 20~40 目 40~60 目 60~70 目空速 (g/gcat.

h)0.5 1.0 0.5 1.0

XDMO 97.1% 99.0% 100% 100%

SEG 82.4% 93.8% 91.0% 93.9%

C. Perego, S. Peratello, Catalysis Today 1999, 52, 133-145.

Internal Diffusion Effects

obs p2*

eff,i i

r Lηφ =

D C eff,i p

εD = D

τ

P K B,iD D D

1 1 1 K p

i

TD d

M48.5

nj

j=B i i ij

y

D y D2,

1 1

1

iji j

i j

TD

M MP V V

13 23 2

21 13 3

1 10 1 1

当 2ηφ小于 0.1(0.15) 时,可认为无内扩散影响。

C. Perego, S. Peratello, Catalysis Today 1999, 52, 133-145.

External Diffusion Effects

0 )obs

gs *g s i i

rCa =

k a (C C

, 1/3 ReB ig D

Dk = Sc J

R

0.82 0.386

1 0.765 0.365)

Re ReDJ = (θ

当 gsCa小于 0.05 时,可认为无外扩散影响。

CH3O C C OCH3 + H2

O OCu/SiO2

CH3O C C OCH3

O OH

H(A)

Cu/SiO2 H2C CH2 + H2

OH OH

CH3 CH2OH + H2O

(E)

(EG)

Cu/SiO2

CH3O C CH2 + H2

OH OH

H2C CH2 + CH3OH

OH OH

Cu/SiO2CH3O C CH2 + CH3OH

O OH

CH3O C C OCH3 + H2

O OH

H (MG) (ME)

CH3O C CH2

OH

(B)

Cu/SiO2CH3O C CH2 + H2

O OH OH

H

Pathway of DMO hydrogenation

H2 + 2# 2H #

DMO * + 2 H# A* + 2# (1)

A* + 2H# + * MG* + 2# + ME* (2)

B* + 2H# + * EG* + ME* + 2# (4)

EG* + 2H# Et* + H2O + 2# (5)

EG* EG + *

ME* ME + *

Et* Et + *

DMO + * DMO *

MG* + 2H# B* +2 # (3)

#, *: Different active site( MG* MG + * )

Ester un-dissociative adsorption

Hydrogen dissociatively adsorb on the active site:

Hydrogen un-dissociatively adsorb on the active site:

Hydrogen un-dissociative adsorption

2H H H vK p

This way is similar to hydrogen dissociative.

The rate control step may be Hydrogen adsorption, surface(1~4) or ester adsorption.

2(1 )H HK pUsing (1+KHpH) instead of in the rate expression.

When the rate is is determined by the un-dissociative adsorption of hydrogen, the rate expression is:

2 2H aH H v dH Hr k p k

C

O

R1 OR2

dissociatively adsorbsR1C*O + R2O*+ 2*

R1C*O

R2O*

hydrogenation and desorbR1CH2OH + *

R2OH + *hydrogenation and desorb

Ester Dissociative adsorption

Pathway of ester dissociative adsorptionH2 + 2# 2H #

EG* + 2H# Et* + H2O + 2# (7)

EG* EG + *

Et* Et + *

MG + 2* HOCH2C*O +OCH3 * (4)

MG* MG + * (3)

CH3OOCC*O + 3H# CH3OOCC*H2OH (MG) + 3# (2)

HOCH2C*O +3H# HOCH2C*H2OH + 3# (5)

OCH3 * + H# ME* + # (6)

ME* ME + *

#, *: Different active site

DMO + 2* CH3OOCC*O +OCH3 * (1)A B

C

The most possible pathwayH2 + 2# 2H #

CH3OOCC*O + H# CH3OOCC*OH + # (1)

EG* + 2H# Et* + H2O + 2#

EG* EG + *

Et* Et + *

DMO + 2* CH3OOCC*O +OCH3 * (9)

MG + 2* HOCH2C*O +OCH3 * (8)

MG* MG + * (7)

CH3OOCC*OH + H# CH3OOCC*HOH + # (2)

CH3OOCC*HOH + H# CH3OOCC*H2OH(MG) + # (3)

HOCH2C*O +H# HOCH2C*OH + # (4)

HOCH2C*OH +H# HOCH2C*HOH + # (5)

HOCH2C*HOH +H# HOCH2C*H2OH + # (6)

OCH3 * + H# ME* + # (10)

ME* ME + *

#, *: Different active site

Summary of model of DMO hydrogenation

DMO dissociative adsorption

DMO molecular adsorption

H2

molecular adsorption

H2

dissociative adsorption

Control step

① DMO adsorption ② H2 adsorption

③ Surface reaction 7 kinds

① ester adsorption

② H2 adsorption ③ Surface reaction 4 kinds

④adsorption/desorption of intermediate-MG

① ester adsorption

② H2 adsorption

③ Surface reaction 4 kinds

23 kind

s

8 月 25 日评价 8 月 27 日评价

0.5h-1 1.0h-1 0.5h-1 1.0h-1

XDMO ( % ) 100 97.0 100 /

SEG ( % ) 97.85 33.84 47.37 /

SMG ( % ) 1.06 65.7 51.52 /

SEt ( % ) 0.84 0.30 0.36 /

表 1 25/27 日催化剂评价表

表 2 设备维修前下催化剂评价表

XDMO ( % ) SEG ( % ) 0.5h-1 100 91.0

1.0h-1 100 93.9

Catalytic performance

0

20

40

60

80

100

120

0 1 2 3 4 5LHSV/ h-1

DMO

/EG(

MG,E

t)

%转

化率

选择

X dmoS EGS MGS Et

Catalytic performance on No.3 reactor

Work plan

1.Finish the work about elimination of External/ Internal Diffusion effects

2. Measure the intrinsic reaction rate and select the most possible model.

①. Reaction rate and adsorption equilibrium constant must higher than > 0;

② Activation energy can not be below zero.

③ Reaction rate constant and adsorption equilibrium constant must satisfy th

e Arrhenius and Van’t Hoff equation;

④ A close correlation with experiment data.

3. Think about further verification of mechanism after kinetics experiment.

Key Laboratory for Green Chemical Technology of Ministry of Education

Thanks for Your Attention!Thanks for Your Attention!

QQss & A & As s

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