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Non-Isothermal Kinetic Analysis of Oil Palm Empty
Fruit Bunch Pellets by Thermogravimetric Analysis
- Bemgba Bevan Nyakuma -
18th Conference of Process Integration, Modelling and Optimisation for Energy
Saving and Pollution Reduction (PRES Conference)
PRES’15 conference, 22-27 Aug 2015, Kuching, Malaysia.
2
Arshad Ahmad, Anwar Johari, Tuan A. T. Abdullah,
Olagoke Oladokun, Dodo Yakubu Aminu
Co-authors
• Introduction
• Experimental
• Results
• Conclusion
3
Contents
4
Introduction
5
• Malaysia >> 2nd largest producer & exporter of Palm Oil
with >> 400 palm oils mills and 4.5 million hectares of Oil
Palm (Elaeis guineensis).
• Palm oil production generates large quantities of Liquid
(POME) & Solid (Lignocellulosic) waste
• Solid Waste >> Empty Fruit Bunch (OPEFB), Palm Fronds
(OPF), Palm Kernel (OPK), Palm Fibre (OPMF).
Introduction
6
Source: http://www.slideshare.net/yongkangbirdnest/oil-
palm-industry-in-malaysia
Introduction
7
Fresh Oil Palm
Fruit Bunches
Pelletized Oil Palm Empty
Fruit Bunches (OPEFB)
Oil Palm Empty fruit
Bunches (OPEFB)
Introduction
8
Solution
9
• Current conversion technologies – open air burning,
incineration, land filling, boiler fuel & prod. steam
• inefficient, outdated, hazardous, unsustainable
• Valorization of OPW into clean energy fuels, power
generation  challenges of OPW accumulation.
• Biomass utilization  price volatility, dwindling reserves
& environmental pollution associated with fossil fuels
Solution
10
Challenges
11
• Biomass properties - high moisture, inhomogeneous sized,
high alkali content, and low energy density fuels
• Pre-treatment and Conditioning
• Drying, Densification, Pelletization, Mechanical
Fractionation, Hydrolysis & Torrefaction, Carbonization.
• To improve feedstock, thermochemical / physicochemical
properties, supply chain, logistics and storage
Challenges
12
Way Forward
13
• Fossil fuels  clean bioenergy fuels transition >> knowledge of
thermal degradation behaviour & decomposition kinetics.
• Mathematical models developed by Flynn-Wall (Flynn and Wall,
1966) and Ozawa (Ozawa, 1965)
• Analytical techniques >> thermogravimetric analysis (TGA) used
to investigate the thermal decomposition kinetics of biomass.
• Vital  feasibility, design and scaling up biomass thermal
conversion equipment & Optimizing yield & composition of
products of thermal conversion.
Way Forward
14
Study Objective
15
To examine the thermal degradation behaviour of oil palm
empty fruit bunches (OPEFB) pellets using TGA.
To determine the decomposition kinetics of the OPEFB pellets
using the Flynn-Wall-Ozawa (FWO) kinetic model.
Way Forward
16
Experimental
17
• Biomass Procurement >>
• Oil palm empty fruit bunches (OPEFB) pellets  Oil Palm Mill in
Johor, Malaysia.
• Biomass Characterization >>
• Elemental composition & Proximate analysis
• Bomb Calorimetry Analysis
• Thermal Analysis >>
• Thermogravimetric (TG) analyser (NetzschTM 209 F3),
• Nitrogen flow rate of 50 mL/min.
• 10 mg heated from 30 to 1000 °C
• Three (3) heating rates, β = 5, 10, 20 °C/min.
• Kinetic Analysis >>
• Flynn Wall Ozawa (FWO) model applied TG data to obtain;
• Activation energy, Ea, & Frequency factor, A at different
conversions, α.
Experimental
18
Experimental
19
Results
20
Results > Biomass Characterization
21
Figure 1: TG curves of Oil Palm Empty Fruit Bunch (OPEFB) pellets.
Results > Thermal Analysis
22
Results > Thermal Analysis
23
A – Drying ( < 100 °C); B – Active Pyrolysis (200-500 °C); C – Passive Pyrolysis ( > 500 °C)
Figure 2: DTG curves of Oil Palm Empty Fruit Bunch (OPEFB) pellets
Results > Thermal Analysis
A B C
24
Kinetic plots for OPEFB pellets using Flynn-Wall-Ozawa (FWO) model
Flynn-Wall-Ozawa (FWO) model >> In β against 1/T
Results > Kinetic Analysis
25
Ea - Activation energy >> Slope – 1.052Ea/R where R = 8.314 J/mol K;
A - Frequency factor >> In[AR/Ea)].
Results > Kinetic Analysis
26
• Average Ea OPEFB pellets (160.21 kJ/mol) << Cornstalk
(206.40 kJ/mol), Sawdust (232.60 kJ/mol), Oak (236.20
kJ/mol).
• Ea is the minimum energy requirement for reactants for
chemical reaction, high Ea values = Slower reactions.
• Lower Ea values for OPEFB pellets emphasizes its
suitability as a feedstock for thermal conversion processes.
Results > Kinetic Analysis
27
Conclusion
28
• Pyrolysis kinetics of OPEFB pellets pyrolysis was investigated using
TGA.
• The results indicate pyrolysis occurs 3 stages; drying, active
pyrolysis & passive pyrolysis.
• Flynn-Wall-Ozawa (FWO) model was applied to deduce the kinetic
parameters; Activation energy, Ea, & Frequency factor A.
• Average Ea & A values for OPEFB pellets >> 160.20 kJ/mol and
1.38 x 1024 min-1, respectively.
• Thermo-chemical and Pysico-chemical properties indicate OPEFB
pellets is a potentially suitable feedstock for biomass conversion.
Conclusion
29
Acknowledgement
30
The authors acknowledge the Ministry of Education (MOE) Malaysia
for the Long Research Grant Scheme (LRGS) VOT: 4L817.
The authors are grateful to S. L. Wong, and Muhamad Faizal B. A.
Halim of Universiti Teknologi MARA, Shah Alam for the TG
measurements.
Acknowledgement
31
Terima kasih
(Thank you)

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Non-Isothermal Kinetic Analysis of Oil Palm Empty Fruit Bunch Pellets by Thermogravimetric Analysis_Nyakuma et al., 2015

  • 1. Non-Isothermal Kinetic Analysis of Oil Palm Empty Fruit Bunch Pellets by Thermogravimetric Analysis - Bemgba Bevan Nyakuma - 18th Conference of Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction (PRES Conference) PRES’15 conference, 22-27 Aug 2015, Kuching, Malaysia.
  • 2. 2 Arshad Ahmad, Anwar Johari, Tuan A. T. Abdullah, Olagoke Oladokun, Dodo Yakubu Aminu Co-authors
  • 3. • Introduction • Experimental • Results • Conclusion 3 Contents
  • 5. 5 • Malaysia >> 2nd largest producer & exporter of Palm Oil with >> 400 palm oils mills and 4.5 million hectares of Oil Palm (Elaeis guineensis). • Palm oil production generates large quantities of Liquid (POME) & Solid (Lignocellulosic) waste • Solid Waste >> Empty Fruit Bunch (OPEFB), Palm Fronds (OPF), Palm Kernel (OPK), Palm Fibre (OPMF). Introduction
  • 7. 7 Fresh Oil Palm Fruit Bunches Pelletized Oil Palm Empty Fruit Bunches (OPEFB) Oil Palm Empty fruit Bunches (OPEFB) Introduction
  • 9. 9 • Current conversion technologies – open air burning, incineration, land filling, boiler fuel & prod. steam • inefficient, outdated, hazardous, unsustainable • Valorization of OPW into clean energy fuels, power generation  challenges of OPW accumulation. • Biomass utilization  price volatility, dwindling reserves & environmental pollution associated with fossil fuels Solution
  • 11. 11 • Biomass properties - high moisture, inhomogeneous sized, high alkali content, and low energy density fuels • Pre-treatment and Conditioning • Drying, Densification, Pelletization, Mechanical Fractionation, Hydrolysis & Torrefaction, Carbonization. • To improve feedstock, thermochemical / physicochemical properties, supply chain, logistics and storage Challenges
  • 13. 13 • Fossil fuels  clean bioenergy fuels transition >> knowledge of thermal degradation behaviour & decomposition kinetics. • Mathematical models developed by Flynn-Wall (Flynn and Wall, 1966) and Ozawa (Ozawa, 1965) • Analytical techniques >> thermogravimetric analysis (TGA) used to investigate the thermal decomposition kinetics of biomass. • Vital  feasibility, design and scaling up biomass thermal conversion equipment & Optimizing yield & composition of products of thermal conversion. Way Forward
  • 15. 15 To examine the thermal degradation behaviour of oil palm empty fruit bunches (OPEFB) pellets using TGA. To determine the decomposition kinetics of the OPEFB pellets using the Flynn-Wall-Ozawa (FWO) kinetic model. Way Forward
  • 17. 17 • Biomass Procurement >> • Oil palm empty fruit bunches (OPEFB) pellets  Oil Palm Mill in Johor, Malaysia. • Biomass Characterization >> • Elemental composition & Proximate analysis • Bomb Calorimetry Analysis • Thermal Analysis >> • Thermogravimetric (TG) analyser (NetzschTM 209 F3), • Nitrogen flow rate of 50 mL/min. • 10 mg heated from 30 to 1000 °C • Three (3) heating rates, β = 5, 10, 20 °C/min. • Kinetic Analysis >> • Flynn Wall Ozawa (FWO) model applied TG data to obtain; • Activation energy, Ea, & Frequency factor, A at different conversions, α. Experimental
  • 20. 20 Results > Biomass Characterization
  • 21. 21 Figure 1: TG curves of Oil Palm Empty Fruit Bunch (OPEFB) pellets. Results > Thermal Analysis
  • 23. 23 A – Drying ( < 100 °C); B – Active Pyrolysis (200-500 °C); C – Passive Pyrolysis ( > 500 °C) Figure 2: DTG curves of Oil Palm Empty Fruit Bunch (OPEFB) pellets Results > Thermal Analysis A B C
  • 24. 24 Kinetic plots for OPEFB pellets using Flynn-Wall-Ozawa (FWO) model Flynn-Wall-Ozawa (FWO) model >> In β against 1/T Results > Kinetic Analysis
  • 25. 25 Ea - Activation energy >> Slope – 1.052Ea/R where R = 8.314 J/mol K; A - Frequency factor >> In[AR/Ea)]. Results > Kinetic Analysis
  • 26. 26 • Average Ea OPEFB pellets (160.21 kJ/mol) << Cornstalk (206.40 kJ/mol), Sawdust (232.60 kJ/mol), Oak (236.20 kJ/mol). • Ea is the minimum energy requirement for reactants for chemical reaction, high Ea values = Slower reactions. • Lower Ea values for OPEFB pellets emphasizes its suitability as a feedstock for thermal conversion processes. Results > Kinetic Analysis
  • 28. 28 • Pyrolysis kinetics of OPEFB pellets pyrolysis was investigated using TGA. • The results indicate pyrolysis occurs 3 stages; drying, active pyrolysis & passive pyrolysis. • Flynn-Wall-Ozawa (FWO) model was applied to deduce the kinetic parameters; Activation energy, Ea, & Frequency factor A. • Average Ea & A values for OPEFB pellets >> 160.20 kJ/mol and 1.38 x 1024 min-1, respectively. • Thermo-chemical and Pysico-chemical properties indicate OPEFB pellets is a potentially suitable feedstock for biomass conversion. Conclusion
  • 30. 30 The authors acknowledge the Ministry of Education (MOE) Malaysia for the Long Research Grant Scheme (LRGS) VOT: 4L817. The authors are grateful to S. L. Wong, and Muhamad Faizal B. A. Halim of Universiti Teknologi MARA, Shah Alam for the TG measurements. Acknowledgement

Editor's Notes

  1. For every 1 kg of palm oil produced, 4 kg of waste is produced.
  2. For every 1 kg of palm oil produced, 4 kg of waste is produced.
  3. For every 1 kg of palm oil produced, 4 kg of waste is produced.
  4. The linear regression plots of In β vs 1/T for conversions α = 0.10 – 0.60 for OPEFB pellets are presented in Figure 3. The slope is given by -1.052 Ea/R while frequency factor A was deduced from the intercept of the plots using the relation In (AR/Ea) based on the assumption 2RT << Ea (Damartzis et al., 2011). Furthermore, the conversions α < 0.1 and α > 0.8 have been excluded due to the low correlation values (Damartzis et al., 2011).