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Processing Lignins Guozhan Jiang

Processing Lignins

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Processing Lignins. Guozhan Jiang. Objectives. To find a method to convert Etek and Asian lignins into bio-oils. To characterise the products using PyGC/MS and other chromatographic or spectroscopic methods. To upgrade the bio-oils to valuable chemicals or transportation oils. . Outline. - PowerPoint PPT Presentation

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Page 1: Processing Lignins

Processing Lignins

Guozhan Jiang

Page 2: Processing Lignins

Objectives

• To find a method to convert Etek and Asian lignins into bio-oils.

• To characterise the products using PyGC/MS and other chromatographic or spectroscopic methods.

• To upgrade the bio-oils to valuable chemicals or transportation oils.

Page 3: Processing Lignins

Outline• Component determination• PyGC-MS work• Preliminary work for run on 150g/h rig• Alternative way to pyrolysis• Future work

Page 4: Processing Lignins

Component determination: wet chemistry method

Extractives: Extracted using: ethanol/toluene (6hrs)ethanol (4hrs)water (2hrs)

Lignin (Klason): 0.1M NaOH boiling 1hr72% H2SO4 treatment 4hrs

Cellulose: NaClO2 bleaching of holocellulose

Hemicellulose: 17.5% NaOH treatment of cellulose

Biomass

Page 5: Processing Lignins

ResultsEtek lignin Asian lignin

Extractive (%) 12.74 39.68

Lignin (%) 29.20 -

Cellulose (%) 45.70 -

Hemicellulose (%)

9.32 -

Page 6: Processing Lignins

Component determination

• The component of Etek lignin can be determined using this method.

• This method is not suitable for Asian lignin since the extractive free samples can be completely dissolved in 0.1M NaOH.

• Asian lignin must have a much less cross-linking density in its molecular structure.

Conclusions

Page 7: Processing Lignins

PyGC-MS work, 06-Sep-2007 + 20:02:03

1.50 11.50 21.50 31.50 41.50 51.50 61.50 71.50 81.50 91.50 101.50Time0

100

%

0

100

%

asian lignin 1 Scan EI+ 78+94

1.51e929.59

41.32

38.9035.14

33.52

41.39

52.4147.3543.66 50.24 60.5652.77

57.11

asian lignin 1 Scan EI+ TIC

2.06e1041.32

30.36

29.59

3.64

17.318.554.29 10.23 26.80

35.13

33.52

31.86

38.90

41.39

43.66

47.35

46.78 60.5650.24 52.41

57.11

53.1263.88

Species containing m/z =94 and 78

Asian lignin @600oC for 15s

Page 8: Processing Lignins

, 06-Sep-2007 + 23:52:10

1.50 11.50 21.50 31.50 41.50 51.50 61.50 71.50 81.50 91.50 101.50Time0

100

%

0

100

%

etek lignin 1 Scan EI+ 78+945.68e8

35.17

29.59

8.886.8630.37

41.35

38.89

35.66

46.79

42.37

44.68

49.97

52.76

57.2854.42

etek lignin 1 Scan EI+ TIC

1.71e1035.18

30.38

17.36

4.80

3.42

9.86

8.517.28

16.70

14.46

27.9523.02

19.68 25.73 33.34

56.5443.13

41.35

38.89

35.77

46.79

43.36 50.84

54.7757.28

Etek lignin species containing m/z = 94 and 78

Etek lignin@600oC for 15s

Page 9: Processing Lignins

, 06-Sep-2007 + 20:02:03

1.50 11.50 21.50 31.50 41.50 51.50 61.50 71.50 81.50 91.50 101.50Time0

100

%

0

100

%

asian lignin 1 Scan EI+ TIC

2.06e1041.32

30.36

29.59

3.64

17.318.554.29 10.23 26.80

35.13

33.52

31.86

38.90

41.39

43.66

47.35

46.78 60.5650.24 52.41

57.11

53.1263.88

asian lignin 400a Scan EI+ TIC

1.73e1041.27

3.68 17.27

30.2326.7438.80

60.4955.90

43.5347.57 55.08

50.7561.49

66.31

Asian lignin @400oC for 15s

Asian lignin@600oC for 15s

Page 10: Processing Lignins

, 06-Sep-2007 + 23:52:10

1.50 11.50 21.50 31.50 41.50 51.50 61.50 71.50 81.50 91.50 101.50Time0

100

%

0

100

%

etek lignin 1 Scan EI+ TIC

1.71e1035.18

30.38

17.36

4.80

3.42

9.86

8.517.28

16.70

14.46

27.9523.02

19.68 25.73 33.34

56.5443.13

41.35

38.89

35.77

46.79

43.36 50.84

54.7757.28

etek 400a Scan EI+ TIC

2.29e93.65

3.42

47.59

3.72

3.76

42.91

17.31

4.89

34.5830.26

19.6541.2738.82 46.72

87.2756.1150.46 54.71

Etek lignin 400 and 600

Etek lignin@400oC for 15s

Etek lignin @600oC for 15s

Page 11: Processing Lignins

PyGC-MS work

• The two lignins can not be pyrolysed effectively at 400oC.

• Asian lignin is a ‘real’ lignin.• Etek lignin has similar composition to

normal biomass.

Conclusions

Page 12: Processing Lignins

Preliminary work for run lignins on 150g/h rig

• The two lignins are difficult to feed continuously.

• Two approaches to be adopted for feeding properly (1) Modify feeding system, (2) Modify lignins.

• Modification of lignins is chosen in this work by pelitization.

Page 13: Processing Lignins

Pellitization

Alcohol extracted compounds as binders

Asian lignin

EthanolSuspension

Heating up

80oC“Dough” like

Drying

Pellet

Mixing

Page 14: Processing Lignins

Pelletization of Asian lignin

Before pelleting After pelleting

Page 15: Processing Lignins

Pellet

Page 16: Processing Lignins

Alternative to pyrolysis

Method % dissolved

0.1 M NaOH aqueous, 4hrs boiling, 10% 10.2

Ethanol + 0.1 M NaOH, 4hrs boiling, 10% 10.5

Isopropanol + 0.1M NaOH, 4hrs boiling, 10% 21.2

Isopropanol + 0.1M H2SO4 + Phenol (13.5% wt), 10% 28.3

Extracted using ethanol/toluene (6hrs), ethanol (4hrs) and water (2hrs), extractive free samples boiling in 0.1M NaOH, 2%

100

Asian lignin

Page 17: Processing Lignins

Alternative to pyrolysis

Extractive free sample dissolved in 0.1M NaOH,2%

Page 18: Processing Lignins

Future work• Run Asian and Etek lignins on 150 g/h rig for

pyrolysis • Hydrogenation of lignin pyrolytic products to

produce saturated phenol and phenol substitutes, which may be used to produce phenolic resin.

• Quantification of mass balance using Py-GC/MS.• Hydrogen, steam or alcohol assisted pyrolysis to

reduce char formation.

Page 19: Processing Lignins