Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage

Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage

Accepted Manuscript Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage Zhang Hang, Deng Shengxiang,...

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Accepted Manuscript Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage

Zhang Hang, Deng Shengxiang, Cao Xiaolin PII:

S0960-1481(17)30854-6

DOI:

10.1016/j.renene.2017.08.095

Reference:

RENE 9193

To appear in:

Renewable Energy

Received Date:

03 March 2017

Revised Date:

14 July 2017

Accepted Date:

31 August 2017

Please cite this article as: Zhang Hang, Deng Shengxiang, Cao Xiaolin, Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage, Renewable Energy (2017), doi: 10.1016/j.renene.2017.08.095

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ACCEPTED MANUSCRIPT 

We propose four decomposition and four subsequent reaction pathways.



We calculate bond dissociation energies of homolytic cleavage for lignin dimmer.



We calculate enthalpy changes and Gibbs free energy changes of each reaction.



The equilibrium geometries of stagnation points in the reaction are optimized.

ACCEPTED MANUSCRIPT

2

Density functional theory investigation of gasification mechanism of a lignin dimer with β-5 linkage

3

Zhang Hang 1*, Deng Shengxiang1, Cao Xiaolin2

1

4 5

1 College 2 Energy

of Energy Science and Engineering, Central South University, Changsha 410083, China

& Power Engineering College, Changsha University of Science & Technology, Changsha 410012, China

6

Abstract: Density functional theory was employed to investigate gasification mechanism of β-5

7

linkage lignin in high temperature steam at B3LYP/6-31G++(d,p) level. Four possible

8

decomposition reaction pathways and four successive reactions pathways were proposed. The

9

equilibrium geometries of the reactants, transition states, intermediates and products were

10

optimized. The activation energies, Gibbs free energy changes and enthalpy changes of each

11

reaction step in gasification pathways were analyzed. From the calculation results of ΔHθ, it is

12

concluded that the four decomposition reaction are endothermic below 1300 K, and exothermic

13

exceed 1500 K. Furthermore, the ΔHθ of each reaction decrease with temperature increasing. From

14

the ΔGθ calculation results, Path 2 and Path 3 occur spontaneously without temperature limited.

15

Path 1 and Path 4, however, are spontaneous reaction above 700 K. It is not ensure that Path 5,

16

Path 6, Path 7 and Path 8 can occur spontaneously. Comparison of activation energy of each

17

reaction pathway, Path 2 is optimal decomposition reaction without a competitive reaction. The

18

main products in decomposition reaction are 5-hydroxyphenyl-acetaldehyde (P5) and 12-

19

hydoxymethyl-phenol (P4). Path7 is the optimal subsequent reaction with a competitive reaction,

20

i.e., Path 5. The main products in subsequent reaction are CO, phenol and formaldehyde.

21

Keywords: Lignin dimer; Density function theory; Gasification; Thermodynamic; Dynamic

22

1. Introduction

23

The rising concerns about energy security and environmental degradation in newly

24

industrialized and transition economies has increased renewable energy demand and alternate

25

energy resources [1-2]. CO2 emissions, especially, are becoming a major problem all around

26

world. Biomass is viewed as a potentially significant source of renewable energy[3-4].

1

*Corresponding author. Address: School of Energy Science and Engineering, Central South University, Changsha 410083, China. Tel: +86 18508449270; e-mail: [email protected] (H. Zhang) 1

ACCEPTED MANUSCRIPT 27

Gasification of biomass in the high-temperature steam, being as a technology which is quite

28

promising[5-6], is greatly featured that the emission of CO2 can be lowered by 30%, 15-30% of

29

energy can be saved and the emission of NOX is lower than 100ppm.

30

Lignin, being as one of the three major components of biomass[7,8], can reflect the

31

gasification rules of biomass by its gasification features. Therefore, it is necessary to study lignin

32

pyrolysis mechanism in gasification process. For lignin, the polymerization is via the

33

dehydrogenation of monomer, which is made up of some chemical bonds (like C-C bond and C-O

34

bond) in an unordered way. For example, β-5 type lignin dimmer, a typical structure of lignin, is a

35

propyl structure consisting of two benzene rings with a Cβ-C5 bond linkage (see Fig. 1).

36

In recent years, Tan et al. [9]and Yue et al. [10] found that abundant phenol after the

37

decomposition reaction in their experiments. It is well known that phenol will not be produced

38

unless cleavage of Cα-Cβ and Cβ-C5. In fact, Beste et al. [11]studied that the initial step in the

39

thermal decomposition of PPE (β-O-4 type lignin dimer) is the hemolytic cleavage of the oxygen-

40

carbon bond, and that carbon-carbon bond cleavage in PPE could be a competitive initial reaction

41

under high-temperature pyrolysis conditions. According to the experiment result in reference [12],

42

it is concluded that phenol, p-hydroxybenzyl alcohol and ethyl alcohol are the main products of

43

Cα-Cβ bond cleavage and β-O-4 bond cleavage. Qin et al. [13] investigated that the saw powder

44

rich in lignin will produce oil tar after gasification, which exist large amounts of

45

aromatic compounds (side chain). They also found that the side chain cracking with experiment

46

temperature increasing. As we know, lignin are interconnected by a variety of linkages (β-O-4, α-

47

O-4, β-1, β-5). The β-O-4 bond is the major type of linkage which occupies 48-60% of the total

48

linkages depending on the type of wood. Regarding β-O-4 lignin, there are different views on its

49

mechanism of thermal cracking. For example, Elder and Beste [14]did a quantum chemical study

50

on pyrolysis mechanism of β-O-4 lignin, concluding that activation energy of concerted reaction is

51

lower than the bond dissociation energy of homolytic reaction, which reflects that homolytic

52

reaction plays a leading role among these reactions. On the contrary, Huang et al. [15]found that

53

concerted reaction and homolytic reaction are both the major reaction paths of lignin dimer, which

54

will be affected by the temperature. It is summarized that concerted reaction will play the leading

55

role during the pyrolysis at the low-temperature, but homolytic reaction will do at high-

56

temperature. Apart from β-O-4 lignin, there are other kinds of lignin, such as β-1 lignin (Huang et 2

ACCEPTED MANUSCRIPT 57

al. [16]once studied the pyrolysis mechanism); α-O-4 lignin (Wu et al. [17]studied the pyrolysis

58

process of lignin dimer with α-O-4 linkage). Moreover, Cao et al. [18]once studied the reaction

59

mechanism of high temperature steam gasification of β-1 lignin dimer in the water solvent

60

environment.

61

However, today, there are few related to high temperature steam gasification of β-5 linkage

62

lignin dimer in terms of its chemical reaction, evolution reaction between intermediates and

63

transition state. In order to gain a better understanding of the detailed mechanism of lignin

64

gasification and the temperature effects on gasify process, mechanism of β-5 linkage lignin dimer

65

gasification at different temperature steam have been investigated in this paper.

66

2. Density functional theory (DFT) calculation methods

67

As for the electric correlation effects, DFT will calculate the large molecular system, whose

68

calculation results are quite accurate and reliable[19,20].In this paper, the relevant calculation

69

work was relied on DFT method with B3LYP (Becke’s three parameter gradient corrected

70

exchange functional with the gradient corrected correlation function [21]) and 6-31++G(d, p) basis

71

set (“6-31G” is an expression of splitting valence bond basis set. “++” are addition diffuse

72

functions of heavy atom and hydrogen. “d” and “p” are addition polarization functions of carbon

73

and hydrogen,respectively [22]), which consists of optimizing the equilibrium geometries such

74

as reactant, intermediates, products and transition states. The reason for providing the polarized

75

function is that is better to describe the system. Transition states (TS) method was employed to

76

find the transition state[23]. Intrinsic reaction coordinate (IRC) calculations were applied to

77

identify the minimum energy path from a transition state to the two corresponding local minima.

78 79

Thermodynamic data such as enthalpy changes (ΔHθ) and Gibbs free energy changes (ΔGθ) were calculated to analyze priorities of the reaction pathways.

80

For reaction:

81

A  B  A· B·

82

Enthalpy change of the reaction are calculated by Eq. (2) [24]:

83

H  H ( A)  H ( B)  H ( A  B)

84

Enthalpy change are estimated by the following expression:

85

H  E  nRT

(1)

(2)

(3) 3

ACCEPTED MANUSCRIPT 86

E =E0  Etrans  Erot  Evib

87

E0 =Eelec  ZPE

88

Which, ∆Eelec is internal energy, ZPE is zero point energy, ∆Etrans is translation energy, ∆Erot is

89

(4) (5)

rotation energy, and ∆Evib is vibration energy.

90

The gibbs free energy change calculation equation:

91

G  H  T  S

92

Which, T is reaction temperature, ∆S is entropy change.

93

When ΔH < 0, it means that the reaction is exothermic, it is endothermic if ΔH > 0. When ΔG <

94

0, it indicated that the reaction can be carried out spontaneously, instead, it can not occur

95

spontaneously if ΔG > 0. Furthermore, the size of ΔG determines conversion rate of reaction

96

reaching equilibrium.

(6)

97

According to transition state theory, activation energy is the minimal potential-energy

98

difference between transition state and reactants in ground state[25]. Since temperature affecting

99

slightly on thermodynamic, it, normally, did not take into account in calculating activation

100

energy[26]. The authors used E0 to represents the activation energy of each species in the reaction.

101

For free-radical reactions, the bond dissociation energies are usually equal or almost equal to the

102

activation energies. All calculations were performed using the Gaussian 09 suites of programs[27].

103

3. Results and discussion

104

3.1 Bond dissociation energies for β-5 linkage lignin dimer

105

Bond dissociation energies (ΔE) are recognized as an important thermodynamic quantity that

106

can exemplify the reaction sensitivity of a hemolytic cleavage of the considered bond. Cao et al.

107

[28] investigated biomass pyrolysis and carbonization process by TG-FTIR experimental. The

108

results show that when the temperature is in the range of 773~1173K, C - C bond and C - H bond

109

were further fractured. Most of the benzene ring has been decomposition or aromatic to form

110

amorphous carbon. In lignin gasification process, the homolytic bond dissociation is an important

111

reaction step. Fig. 1 gives the homolytic cleavage paths for the β-5 type lignin dimmer model

112

compound and their bond dissociation energies. The lowest bond dissociation energy is that of Cγ-

113

Cβ. The order of ΔE is as follows: Cγ-Cβ < Cα-Cβ < Cα-C12 < C5-Cβ < Cγ-OH < Cα-OH < C4-OH < 4

ACCEPTED MANUSCRIPT 114

C9-OH, therefore, the homolytic cleavage of the Cγ-Cβ, Cα-Cβ, Cα-C12, and C5-Cβ bond could be

115

the initial step in the decomposition reaction of β-5 type lignin dimmer. 2

2 1

3

1

3

6

4

6

4

OH



OH

5

HO







OH

+ HO

OH

12

11

1

3

8

10

8

10

6

4

10

E =8 1.

9

7k

HO

cal /m ol

2 1

3

6

7

C

12

8

11 10

+

9

3

6

4

HO

HO

E=40.8 kcal/mol HO

5

OH



OH



CH



CH 



7

10 9

116

HO



+

CH 2

.1

ol l/m a kc

.5

ol /m l a kc

11

8

1

10

2

4

C

1

3

6

4

OH

5

E=35.2 kcal/mol

HO



CH 

7

10 9

HO

-5 linkage lignin dimer

E =3 7

11

8

OH

+

12

H2C 

10 9

.6

HO

kca l/m ol

HO

2 1

3

6

HO

9

OH OH

+

HO

11

8



12

2 11

8

6 =4 E

OH

12 7







12



HO

4 5

2 1



7

4 =6 E

OH

5

HO

 

OH





HO

k

4

11

8

9

C

12 7

9

C

l mo al/ kc



2

7

.2

+

HO



+ HO

11

6 =8

HO

 12

E

5

HC

7

3

6



cal /m ol

2 1

5

3

6

4 5

OH

5

HC 

117

Fig.1.

118

3.2 Reaction pathways of belta-5 linkage lignin dimer gasification



OH OH

+

CH  12

7

11

8

10 9

HO

Homolytic cleavage paths of β-5 linkage lignin dimer and their bond dissociation enthalpies (ΔE).

119

From the above calculation results of bond dissociation enthalpies of β-5 linkage lignin dimer,

120

this paper proposes four decomposition reactions as initial gasification pathways: homolytic

121

cleavage of Cβ-C5 bond, Cα-Cβ bond, Cα-C12 bond and Cβ-Cγ bond (see Fig. 2) and four subsequent

122

reactions as secondary gasification pathways. From the decomposition reactions depicted in Fig.

123

2, it is inferred that the major decomposition products are phenolic compounds, no small molecule

124

gases. So the authors proposed that the four special products (P2, P4, P5 and P6) are utilized to

125

produce small molecule gases with water molecule in the subsequent reactions formed as

126

concerted reaction (see Fig. 3).

5

ACCEPTED MANUSCRIPT HO

CH 



7

11

8

10

Path1

TS1

HO

OH



12

 



-H

7

11

8

10

9

9

HO

HO

+

IM1

2

2

1

3

8

4

HO

OH

HO

CH 

 12

TS2

7

11

8

10

3

6

4 5

OH

HC

OH

Path2





TS3 HO

+

IM4

-H

CH2 

P1

2 1

3

6

4

OH



OH

5

HO





2

2

6

4

TS4 OH

5 

1

3

1

3

6

4

6

4

OH

5 

OH





O

11

8

10

+



12

H

7

11

8

10

9

9

HO

HO

P4

2

8

1

1

3

6

3

3

6

4

10

HO

9

OH

CH 



+H

HO

Path3

OH

 

7

11 10

7

11

8

10

TS6

HO

+

-H

OH

Path4

3 4

OH



OH



C

12

8

11

IM3

10

8

10

3

6

4

HC

1

3 4

OH

+



OH

O





TS9

IM5

9

9

HO

HO

P6

10

2

2 3

6

4

OH



OH

5 

3

1

TS4

1

OH



4

6

OH

5

O

 

IM2

-H



O

2

CH2 

TS9b

11

8

+H OH

CH

12 7

9

1

3

6

4

P9

5

OH



O



10 9

P5

HO

P8

127 Fig.2.

Decomposition reaction pathways schematic of belta-5 linkage lignin dimer model compound gasification O

HO

CH3 





12 7

11

8

10 9

+

H

OH

TS10

12

12 7

11

8

10 9

HO

+

CO 

+

CH3OH

11

8

10

+

H

OH

Path5

TS11

12 7

11

8

10

9

9

HO

HO

P4

2 + 2H2 + CO 

Path6

O

12 7

11

8

10 9  

P5

Fig.3.

7

HO

P2

129 130

1

6



+H

12

8

5

11



HO

O

HO

128

O

-H

7

2

-H

+ 7

CH

5

5

TS8

P7

11

2

1



+ 12



6

OH

7

2

CH

5 



P1

HO

OH

CH2



4

CH3

O

CH2

3

6

CH2

HO

9

9

1



12

8

TS5

4 5

12

R

+H

5 6

4 5

HO

2

1 2

2

11

OH O

P5

12 7

5 



CH

7

P2

O



OH

3

HO

11 10 9

IM2

 12

7 8

HO

CH2

1

+

11 10 9

OH

2

-H

7 8

HO

4

2



12

9

P3

1

TS7

CH3



HO

3

5

11 10

12

9

1

5

7 8

O







12

+H

CH2

O

CH2



HO

6

+H

C

OH

12

OH

+

H

OH

TS12

11

8

10 9

O



12 7

3OH + CH + CO  

12 7

11

8

10

+

H

OH

TS13

HO

10

+

CO2 

+ H2

HO

HO

P6

11

8 9

9

Path7

12 7

Path8

Subsequent reaction pathways schematic of belta-5 linkage lignin dimer model compound gasification 6

ACCEPTED MANUSCRIPT 131 132

3.3 Optimization of geometries and their key bonds length Table 1 shows the equilibrium geometries of the reactants, intermediates and partial transition

133

states after optimizing and lists the key bond length of the species.

134 135

Table 1. Geometric structure and key bond length optimization of the species in each reaction. Optimized structure

Bond length / (Å)

Optimized structure

Bond length / ( Å)

R(19,20)

1.5432

R(19,20)

1.5432

R(20,22)

1.5397

R(20,22)

1.5397

R(1,20)

1.5420

R(12,19)

1.5403

R(12,19)

1.5403

R(19,34)

1.4303

R(19,34)

1.4307

R(22,26)

1.4307

R(20,22)

1.5429

R(19,20)

1.5432

R(1,20)

1.5420

R(1,20)

1.4065

R(12,19)

1.5403

R(19,12)

1.3720

R(22,26)

1.0847

R(19,34)

1.3948

R(19,22)

1.0871

R(19,20)

1.4132

R(19,34)

1.4498

R(20,22)

1.3997

R(19,20)

1.3471

R(22,26)

1.3489

R(19,20)

1.2632

R(20,22)

1.8811

R(19,21)

1.3257

R(22,26)

1.2677

R(1,20)

1.8860

R(26,27)

1.4086

R(19,34)

1.4307

R(1,20)

1.5420

R(19,20)

1.8843

R(20,22)

1.2643

R(20,22)

1.2616

R(22,26)

1.2576

R(22,26)

1.4958

R(26,27)

1.4128

R(1,20)

1.5420

R(1,20)

1.5420

R(20,22)

1.8774

R(19,20)

1.8812

R(22,26)

1.2638

R(19,34)

1.2611

R(26,27)

1.4088

R(34,35)

1.4122

R(1,20)

1.5420

R(20,22)

1.5397

R(19,34)

1.2558

R(19,12)

1.8804

R(19,20)

1.3628

R(19,34)

1.2611

R(34,35)

1.1869

R(34,35)

1.4122

R(20,22)

1.5397

R(19,20)

1.5432

R(19,20)

1.8846

R(20,22)

1.3496

R(22,25)

1.3200

R(1,20)

1.5420

136 137

Table note: bond length of Cγ-Cβ, Cα-Cβ, Cα-C12, C5-Cβ, Cγ-OH and Cα-OH are marked as R(19,20), R(20,22), R(1,20), R(19,12),

138

3.4 Thermodynamics Analysis of the decomposition and subsequent reactions

R(19,34), R(22,26), respectively.

7

ACCEPTED MANUSCRIPT 139 140

Table A1 in appendix gives enthalpy changes ΔHθ and Gibbs free energy changes ΔGθ of each reaction pathway at different temperature.

141

Fig. 4 shows the ΔHθ (θ represents temperature) of each reaction at different temperature (700 -

142

1700 K). The results indicate that the ΔHθ of Path 1 decreases with an increase of temperature

143

(700 K to 1700 K). It is an endothermic reaction because ΔHθ is positive value. The ΔHθ of Path2

144

starts from 3.0 kcal/mol and reduces to -2.4 kcal/mol (at 1500K) with a change of endothermic to

145

exothermic . For Path 3, the ΔHθ is very closed to 0 kcal/mol at 1500 K, and would be a negative

146

value if temperature kept increasing. The ΔHθ of Path 4 are higher than zero, so it is endothermic.

147

The ΔHθ of Path 5 reduces from 12.3 to 1.6 kcal/mol and keeps endothermic reaction. The ΔHθ of

148

Path 6 is down to -1.1 kcal/mol and converts into exothermic reaction until temperature increased

149

to 1700 K. For Path 7, the ΔHθ decreases from 15.4 kcal/mol to 2.2 kcal/mol (at 700-1700 K) and

150

forms as endothermic. The ΔHθ of Path 8 decreases to -0.8 kcal/mol with changing from

151

endothermic to exothermic at 1700 K. (a) Decomposition reaction

 kcalmol-1

40

Path1 Path2 Path3 Path4

30 20 10 0 -10 700

800

900

1000

1100

1200

1300

1400

1500

1600

1700

 kcalmol-1

Tempeature / (K)

152 153

16 14 12 10 8 6 4 2 0 -2

(b) Subsequent reaction

700

800

900

1000

1100

1200

1300

1400

Path5 Path6 Path7 Path8

1500

1600

1700

Tempeature / (K)

Fig.4. Enthalpy changes as function of temperature, (a) decomposition reaction, (b)subsequent reaction.

154

Fig. 5 indicates that the Path 2 and Path 3 are able to be carried out spontaneously because their

155

ΔGθ<0 (at 700 - 1700 K). Path 1 and Path 4, however, are spontaneous reaction until temperature

156

raised to 700 K. Through comparison of the ΔGθ of each reaction pathway, the authors can see

157

that the order of ΔGθ is Path 3
158

as : Path 3< Path 1
159

Path 5, Path 6, Path 7, Path 8 can not occur spontaneously with an order of ΔGθ: Path 8< Path 8

ACCEPTED MANUSCRIPT 160

6
G kcalmol

0 -20 -40 -60 -80 -100 -120

G kcalmol

700

800

900

1000

7 6 5 4 3 2 1 0

1100

700

163

1200

1300

1400

Tempeature / (K)

1500

1600

800

900

1000

1100

1200

1300

1400

1700

Path5 Path6 Path7 Path8

(b) Subsequent reaction

1500

1600

1700

Tempeature / (K)

161 162

Path1 Path2 Path3 Path4

Fig.5. Gibbs free energy changes as function of temperature, (a) decomposition reaction, (b)subsequent reaction.

3.5 Dynamics Analysis of the decomposition and subsequent reactions

164

Table A2 in appendix gives the activation energies of each specie in the reactions proposed.

165

Fig. 6 shows the sectional drawing of potential energy profile along decomposition reaction

166

pathways. In Path 1, β-5 type lignin dimer model compound decomposes into transition state TS1a

167

and TS1b through the homolytic cleavage of the C5-Cβ bond with an energy barrier of 46.1

168

kcal/mol. The TS1a converts into intermediate IM1 through a dehydrogenation, and the TS1b

169

undergoes a hydrogenation to form compound P3. The decomposition reaction absorbs an energy

170

of 24.4 kcal/mol. It can be verified in Table 1 that C5-Cβ bond length enlarges to 1.8860 Å, so it is

171

unstable to breaks. Cα gives a hydrogen atom to C5 and connects to Cβ with a short double bond

172

(1.2632 Å). Compound IM1 can further decompose into TS2a and TS2b through the hemolytic

173

cleavage of Cγ-Cβ bond with an energy barrier of 33.4 kcal/mol. The TS2a and TS2b convert into

174

Compound IM4 and P3 through a hydrogenation and a dehydrogenation, respectively. From Table

175

1, it can be seen that distance of Cγ-Cβ bond reaches 1.8811 Å and is highly possible to cracks. The

176

O34 atom loses a hydrogen atom and makes a connection to Cγ with a short double bond,

177

meanwhile Cβ absorbs the hydrogen atom to form IM4. The decomposition reaction takes an

178

energy of 10.3 kcal/mol. Compound IM4 tautomerize to form hydroxyphenyl-ethanone P2 via

179

TS7 with an energy barrier of 19.0 kcal/mol through intramolecular hydrogen, releasing an energy 9

ACCEPTED MANUSCRIPT 180

of 14.4 kcal/mol. The tautomerization reaction is exothermic and compound IM4 is more stable

181

than its isomers P2.

182

In Path 2, reactant R decomposes into TS3a and TS3b through the homolytic cleavage of the

183

Cα-Cβ bond with an energy barrier of 37.6 kcal/mol. TS3a and TS3b change to compound IM2 and

184

12-hydroxymethyl-phenol P3, respectively. It can be proved in Table 1 that bond distance of Cα-

185

Cβ bond is 1.8843 Å, and it is most likely to rupture. The decomposition reaction is supported by

186

an energy of 18.7 kcal/mol. Compound IM2 tautomerizes to form product P2 via TS7 with an

187

energy barrier of 44.1 kcal/mol through intramolecular hydrogen, releasing an energy of 14.1

188

kcal/mol. There is a transfer of a hydrogen atom from O26 to Cβ, and then product P5 is formed.

189

The tautomerization reaction is exothermic and the intermediate IM2 is more stable than its

190

isomers P5.

191

In Path 3, reactant R, similarly, decomposes into TS5a and TS5b through the homolytic

192

cleavage of the Cγ-Cβ bond (bond length 1.8874 Å) with an energy barrier of 35.2 kcal/mol. The

193

TS5a turns into intermediate IM3 through a hydrogenation, and the TS5b undergoes a

194

dehydrogenation to form product P1. The decomposition reaction absorbs an energy of 14.9

195

kcal/mol. Compound IM3 can further decompose into TS6a and TS6b through the hemolytic

196

cleavage of Cα-Cβ bond (bond length 1.8812 Å) with an energy barrier of 66.5 kcal/mol. These

197

two translate state species can be translated into product P6 and P7. The decomposition reaction

198

takes an energy of 36.2 kcal/mol.

199

In Path 4, reactant R decomposes into TS8a and TS8b through the homolytic cleavage of the

200

Cα-C12 bond (bond length 1.8804 Å)with an energy barrier of 40.8 kcal/mol. TS8a is conversion

201

into intermediate IM5 through a dehydrogenation, and TS8b can undergo a hydrogenation to form

202

product P8. The decomposition reaction absorbs an energy of 30.4 kcal/mol. Compound IM5 can

203

further decompose into TS9a and TS9b through the hemolytic cleavage of Cα-Cβ bond (bond

204

length 1.8846 Å) with an energy barrier of 73.9 kcal/mol. TS9a and TS9b convert into

205

intermediate IM2 and phenol P9 through a hydrogenation and a dehydrogenation, respectively.

206

The decomposition reaction takes an energy of 25.5 kcal/mol. Compound IM2 in Path 4 have a

207

same tautomerization reaction like Path 2, as well as bond length and energy barrier of the

208

reaction.

209

Comparing the energies barriers of each reaction step in the decomposition reactions such as 10

ACCEPTED MANUSCRIPT 210

homolytic cleavage of the Cγ-Cβ, Cα-Cβ, Cα-C12, and C5-Cβ bond, it is summarized that cleavage of

211

Cα-Cβ bond in Path 2 would be the optimal decomposition reaction without a competitive reaction.

212

Hence, the main products of β-5 type lignin dimer model compound in decomposition reaction are

213

5-hydroxyphenyl-acetaldehyde P5 and 12-hydoxymethyl-phenol P4. In reference[29], the

214

pyrolysis properties of lignin were studied by TG-FTIR method and Flynn-Wall-Ozawa

215

calculation method. The results showed that the activation energy of aromatic ring condensation

216

into carbon is much larger than the energy required for the fracture of the branched chain attached

217

to the benzene ring, which indicates that the benzene ring is more likely to break. 120

Path 1 Path 2 Path 3 Path 4

110 100

E0/(kcalmol-1)

90

TS4(100.0)

TS6(81.4)

80 70

TS2(57.8) IM2+P9(55.9)

60 50

TS8(40.8)

40

TS3(37.6)

30

TS5(35.2)

20

0

TS1(46.1)

TS7(62.1)

TS4(54.4) P6+P7(51.3) IM5+P8(30.4) IM1+P3(24.4)

IM4+P1(43.1)

P5(41.8) P2(28.7)

IM3+P1(14.9)

10

218 219

TS9(104.3)

R

IM2+P4(10.3) P5(-3.8)

-10

Fig.6. The potential energy profile along the decomposition reaction pathways

220

Fig. 7 shows the potential energy profile along subsequent reaction pathways. In Path 5, The

221

bonds of Cα-Cβ, Cα-C12, and H-OH in compound P2 are ruptured, meanwhile the Cα atom gets a

222

hydrogen atom and the Cβ attracts a functional group -OH. This hydrothermal reaction between P2

223

and water molecular, finally, forms CO, phenol and formaldehyde with an energies barrier of 15.9

224

kcal/mol and release an energy of 9.7 kcal/mol. In Path 6, Compound P4 and water molecular can

225

undergo a hydrothermal reaction to form CO2, phenol and double H2 with an energies barrier of

226

40.7 kcal/mol, absorbing an energy of 31.4 kcal/mol. In Path 7, the Cγ-Cβ and C5-Cβ bond in

227

compound P5 are broke in a hydrothermal reaction with water molecular. The reaction forms CO,

228

phenol and formaldehyde with an energies barrier of 11.9 kcal/mol, releasing an energy of 12.8

229

kcal/mol. In Path 8, the Cα-C12 bond in compound P6 is cracked, meanwhile a hydrogen atom is

230

transferred to C12 atom and a functional group -OH is attracted by Cα atom. Consequently the

231

reaction forms compounds of CO2, phenol and H2 with an energies barrier of 27.5 kcal/mol, 11

ACCEPTED MANUSCRIPT 232

releasing an energy of 20.8 kcal/mol.

233

Through comparisons of the activation energy of each subsequent reaction, it is concluded that

234

Path7 is the optimal reaction with a competitive reaction, i.e., Path 5. The main products of

235

subsequent reaction are CO, phenol and formaldehyde. 45 40 35 30

TS11(40.7)

Path 5 Path 6 Path 7 Path 8

TS13(27.5)

-1

E0 / (kcalmol )

25 20

TS10(15.9)

15 10 5 0

P3+H2+CO2(20.8)

TS12(11.9) R+ H20

-5

P3+CH3OH+CO(-9.7)

-10 -15

P3+CH3OH+CO(-12.8)

-20

236 237 238

P3+2H2+CO2(31.4)

Fig.7. The potential energy profile along the subsequent reaction pathways

4. Conclusions

239

In this paper, the gasification at high temperature steam mechanism and products formation of

240

lignin dimer with β-5 linkage was investigated by applying DFT method at B3LYP/6-31++G(d, p)

241

level. Four possible decomposition reaction pathways (homolytic cleavage of the Cγ-Cβ bond, and

242

Cα-Cβ bond, Cα-C12 bond, C5-Cβ bond) and four subsequent reaction pathways (hydrothermal

243

reaction of P2, P4, P5 and P6) were proposed. The ΔHθ and ΔGθ of each reaction and the effect of

244

temperature were studied. The activation energies of each reaction step were calculated. Here

245

below are the conclusions:

246

1.

From the ΔHθ calculation results, it is concluded that the four decomposition reaction are

247

endothermic below 1300 K, and exothermic above 1500 K. Furthermore, ΔHθ of each

248

reaction decrease with temperature increasing.

249

2.

Path 2 and Path 3 can occur spontaneously without temperature limited. Path 1 and Path 4,

250

however, are spontaneous reaction until temperature raised to 700 K. The calculation results

251

of the ΔGθ of each decomposition reaction give an order: Path 3
252

700 - 1100 K), and Path 3< Path 1
ACCEPTED MANUSCRIPT 253 254

pathways such as Path 5, Path 6, Path 7, Path 8 can not ensure to occur spontaneously. 3.

Path 2 is optimal decomposition reaction without a competitive reaction. The main products

255

in decomposition reaction are 5-hydroxyphenyl-acetaldehyde P5 and 12-hydoxymethyl-

256

phenol P4. Path7 is the optimal subsequent reaction with a competitive reaction, i.e., Path 5.

257

The main products in subsequent reaction are CO, phenol and formaldehyde.

258

Appendix

259

Table A1.

260

Thermodynamic parameters of reaction path 1, path2, path3 (unit: kcal/mol)

Path1 Path2 Path3 Path4 Path5 Path6 Path7 Path8

261 262

263

700K

900K

ΔHθ

36.8

35.4

ΔGθ

-13

ΔHθ ΔGθ ΔHθ ΔGθ ΔHθ

1100

1300K

1500K

1700K

33.3

27.4

21.7

11.1

-27.6

-40

-55.1

-65.5

-78.5

3.0

1.3

0.3

-2.4

-5.4

-12.1

-24.2

-33.4

-40.9

-50.6

-58.4

-64.1

10.6

6.7

4.6

2.2

0.6

-0.5

-56.0

-69.6

-83.0

-96.1

-108.5

-121.5

25.7

22.6

16.3

12.2

8.6

6.1

ΔGθ

-12.1

-21.9

-30.4

-41.8

-53.6

-63.7

ΔHθ

12.3

8.9

6.3

4.7

2.2

1.6

ΔGθ

6.0

5.1

4.5

3.8

3.2

2.6

ΔHθ

9.4

7.9

5.3

3.6

1.4

-1.1

ΔGθ

3.5

2.9

2.1

1.4

0.5

0.1

ΔHθ

15.4

11.4

8.5

4.6

3.1

2.2

ΔGθ

6.2

4.6

3.3

2.8

1.4

0.5

ΔHθ

8.2

6.6

4.7

2.6

1.3

-0.8

ΔGθ

2.5

1.3

0.6

0.5

0.2

0.1

K

Table A2. Total energy of species in gasification reaction paths(unit: kcal/mol ) Species

E0

Species

E0

Species

E0

Species

E0

R

- 553384.7

IM1

- 360474.2

IM2

- 288637.4

IM3

-481554.5

IM4

- 288640.2

IM5

- 360468.2

P1

-71815.3

P2

-288654.6

P3

-192886.1

P4

- 264737.0

P5

- 288651.5

P6

-264684.8

P7

- 216833.3

H20

-47949.9

H2

-717.1

CO

-71119.7

CO2

-118335.2

CH3OH

-72608.4

TS1

- 553338.6

TS2

- 360440.8

TS3

- 553347.1

TS4

- 288593.3

TS5

-553349.5

TS6

- 481488.0

TS7

-288621.2

TS8

- 553343.9

TS9

- 360394.3

TS10

-336588.6

TS11

-312646.2

TS12

-336589.5

TS13

-312607.2

Table note: Total energy of P8 and P9 are equal to P3 and P1, respectively.

13

ACCEPTED MANUSCRIPT 264

Acknowledgments

265

The authors thank the National Natural Science Foundation of China (No. 51276023) and Funds

266

for International Cooperation and Exchange of the National Natural Science Foundation of China

267

(No. 513101410) for supporting this work.

268

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