Slidepack_2.pdf from Professor Rajnish from IITM

as120311balbhadratub 7 views 34 slides Oct 22, 2025
Slide 1
Slide 1 of 34
Slide 1
1
Slide 2
2
Slide 3
3
Slide 4
4
Slide 5
5
Slide 6
6
Slide 7
7
Slide 8
8
Slide 9
9
Slide 10
10
Slide 11
11
Slide 12
12
Slide 13
13
Slide 14
14
Slide 15
15
Slide 16
16
Slide 17
17
Slide 18
18
Slide 19
19
Slide 20
20
Slide 21
21
Slide 22
22
Slide 23
23
Slide 24
24
Slide 25
25
Slide 26
26
Slide 27
27
Slide 28
28
Slide 29
29
Slide 30
30
Slide 31
31
Slide 32
32
Slide 33
33
Slide 34
34

About This Presentation

Biomass


Slide Content

Department of Chemical Engineering IIT Madras
Biomass characterization
Biochemical Analysis
Cellulose, Hemicellulose, Lignin, Proteins, Lipids,
ExtractivesProximate Analysis
Moisture, Volatile Matter, Fixed Carbon, Ash
Elemental Analysis
C, H, N, S, O
Calorific Value
HHV or GCV, LHV or NCV
40

Department of Chemical Engineering IIT Madras
Biomass analysis
methods
Vargas-Moreno et al., Renew. Sust. Energ. Rev. 16
(2012) 3065–3083 41

Department of Chemical Engineering IIT Madras
Proximate analysis by Thermogravimetry
Moisture
Volatile matter
Fixed carbon
Ash
42

Department of Chemical Engineering IIT Madras
For biomasses: Ambient to 110
o
C@ 50
o
C/min in N
2
(100 mL/min) hold for 5 min
110
o
Cto 900
o
C@ 80
o
C/min in N
2
(100 mL/min) hold for 15 min
Hold at 900
o
Cfor 45 min in air (100 mL/min)
43

Department of Chemical Engineering IIT Madras
Mechanism of cellulose pyrolysis
Lin et al. J. Phys. Chem. C 2009, 113, 20097-20107
Brewer et al. Environ. Prog. Sustainable Energy 2009, 28, 386-396
O
OH
O
CHn
44

Department of Chemical Engineering IIT Madras
Wang et al. Green Chem. 2014, 16, 727
45

Department of Chemical Engineering IIT Madras
Heating value / calorific value
Bomb calorimeter
HHV –Higher heating value
LHV –Lower heating value
HHV = LHV + H
v
(n
H
2
O,out
)
(n
fuel,in
)
H
v
= Heat of vaporization of water
46

Department of Chemical Engineering IIT Madras
Elemental Analysis -Basics
(Cu catalyst)
Thermal conductivity
detector
47

Department of Chemical Engineering IIT Madras
Proximate and Ultimate Analysis of Biomasses
High VM means biomass can ignite even at low temperatures. However, high
temperature needs to be maintained for a long time for completion of
combustion and emission control.
Greater the H+(C/O) of the fuel, better is its higher heating value (HHV)
48

Department of Chemical Engineering IIT Madras
Biomass
Prosopis
juliflora
Paddy
straw
Wheat
Straw
Finnish
pine
wood
Rice
husk
BagasseEFB
Spirulina
algae
Indian
Coal
Polypro
pylene
C 43.8735.9741.3047.1036.8031.3638.31 46.7558.0390.80
H 6.654.585.606.155.200.105.13 6.974.157.05
N 1.400.760.300.130.350.051.20 10.621.700.08
S 0.080.20.230.020.21-0.240.550.25-
O 48.058.7052.5746.0657.4468.4855.1235.1135.872.07
Moistur
e
9.45.004.787.729.146.709.847.67.22-
Volatile
matter
67.965.2076.7574.7756.5066.6266.0871.531.0593.73
Fixed
carbon
19.114.9014.4516.8014.8525.6316.5815.9341.936.27
Ash 3.614.904.020.7119.501.057.504.9719.80-
HHV
(MJ/kg)
17.4311.4514.1220.417.1017.9815.9420.7522.4346.68
Feedstock characteristics
49

Department of Chemical Engineering IIT Madras
Biochemical Composition (wt.%) of Biomass
BiomassCelluloseHemicelluloseLigninExtractivesAsh
Spruce 45.6 20 28.2 0.35.9
Pine 46.9 20.3 27.3 0.35.1
Birch 47 25.9 22 0.34.7
Beech 45 33 20 0.2 2
Fir 45 21 18 0.56.3
Corncob 37.6 31.6 20.8 3.28.1
Corn straw 43.1 31.8 11 0.813.3
Corn stalk 42.7 23.2 17.5 6.89.8
Corn stover35.3 28.9 19.9 4.66.6
Rice straw 41.2 30.7 12.2 1 14.9
Wheat straw38.9 21.1 18 9.75.5
Sugarcane 51.8 27.6 10.7 0.89.1
Miscanthus
giganteus
50.3 24.8 12 2.74.1
Extractives are the material in a biomass sample that is soluble in either water or ethanol during exhaustive extraction
50

Department of Chemical Engineering IIT Madras
Mean proximate composition of solid fuels
Vassilevet al. Fuel 2010, 89, 913-933
51

Department of Chemical Engineering IIT Madras
Mean ultimate composition of solid fuels
Vassilevet al. Fuel 2010, 89, 913-933
52

Department of Chemical Engineering IIT Madras
Biomass category Enriched inDepleted in
Wood and woodybiomass M, VM, CaO, MgO, MnA, N, S, Cl, SiO
2
, P
2
O
5
,
SO
3
Herbaceous and agriresidues FC, VM, O, K
2
O C, H, CaO
Grasses VM, O, K
2
O, SiO
2
C, H,Al
2
O
3
, CaO,
Na
2
O
Straws O, Cl, K
2
O, SiO
2
C, H, Na
2
O
Other residues
(almond hull, shell, coconut
shell, coffee husk, cotton husk, etc.)
FC, K
2
O, MgO, P
2
O
5
Cl
Animal biomass
(chicken litter, meat-bone
meal)
A, C, H, N, S, Cl, CaO,
Na
2
O, P
2
O
5
,SO
3
M, VM, O, Al
2
O
3
,
Fe
2
O
3
, Mn, MgO,
SiO
2
, TiO
2
Contaminatedbiomass
(shredded
currency, demolition/furniture waste, waste
paper, RDF, sewage sludge)
A, C, Cl, H N, S, Al
2
O
3
,
Fe
2
O
3
, TiO
2
FC, K
2
O, P
2
O
5
Characteristic enrichment and depletion trends
Vassilevet al. Fuel 89, 2010, 913-933
M –moisture, VM –volatile matter, FC –fixed carbon, A -ash
53

Department of Chemical Engineering IIT Madras
Correlations for predicting HHV
Dulong’sformula for coal and fossil fuels:
HHV (MJ/kg) = 0.336 [C] + 1.418 [H] + 0.094 [S] –0.145 [O]
Heat of combustion of the sample equals the heat of combustion of its elements
regardless of whether it passes through one or more oxidation states.
Other formulae:
Tillman (for wood): HHV (MJ/kg) = 0.437 [C] –1.67
Lloyd and Davenport (for fossil fuels):
HHV (MJ/kg) = 0.3578 [C] + 1.1357 [H] + 0.059 [N] + 0.1119 [S] –0.0845 [O]
Boie(for fossil fuels):
HHV (MJ/kg) = 0.3515 [C] + 1.1617 [H] + 0.06276 [N] + 0.1046 [S] –0.1109 [O]
Gas Technology Institute
HHV (MJ/kg) = 0.3417 [C] + 1.3221 [H] + 0.1232 [S] –0.1198 ([O]+[N]) –0.0153
[Ash]
54

Department of Chemical Engineering IIT Madras
55

Department of Chemical Engineering IIT Madras
56

Department of Chemical Engineering IIT Madras
57

Department of Chemical Engineering IIT Madras
Reference species
(Ranziand co-workers)
58

Department of Chemical Engineering IIT Madras
Reference species
(Ranziand co-workers)
59

Department of Chemical Engineering IIT Madras
Reference species
(Ranziand co-workers)
60

Department of Chemical Engineering IIT Madras
Reference species
Ranzi, E.; Faravelli, T.; Manenti, F. Pyrolysis, gasification and combustion of solid fuels. In: Van Geem, K. (ed.) Advances in Chemical Engineering: Thermochemicalprocess engineering, Vol.
49, Elsevier, U.K., 2016, http://dx.doi.org/10.1016/bs.ache.2016.09.001
61

62
Department of Chemical Engineering IIT Madras
Calonaciet al. Energy Fuels, DOI:10.1021/ef1008902

63
Department of Chemical Engineering IIT Madras
Elemental analysis of different ligninsand the equivalent composition
in terms of pseudo components / reference species
Faravelliet al., Biomass Bioenergy34 (2010) 290-301

64
Department of Chemical Engineering IIT Madras
Grate fired boiler for straw
Miles et al. Biomass Bioenergy1996, 10, 125-138
Unburntsand
clinkerization
Slagging
Fouling,
corrosion

65
Department of Chemical Engineering IIT Madras
Bubbling fluidized bed
Circulating fluidized bed →
Miles et al. Biomass Bioenergy1996, 10, 125-138

66
Department of Chemical Engineering IIT Madras
Illustration of a grate fired furnace

67
Department of Chemical Engineering IIT Madras
Processes involved in pulverized coal/biomass combustion

68
Department of Chemical Engineering IIT Madras
Typical problems with rice straw combustion
Bed ash and unburnts(5-20%)

69
Department of Chemical Engineering IIT Madras
Typical problems with rice straw combustion
Slaggingin furnace Low heat transfer efficiency

70
Department of Chemical Engineering IIT Madras
Typical problems with rice straw combustion
Fouling on super heater tubes Frequent shut down
for cleaning

71
Department of Chemical Engineering IIT Madras
Typical problems with rice straw combustion
Corrosion Loss of Capex

72
Department of Chemical Engineering IIT Madras

73
Department of Chemical Engineering IIT Madras
Characteristic superheaterdeposit profiles
Release of major ash constituents
Miles et al. Biomass Bioenergy1996, 10, 125-138