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Stand-alone and Biorefinery ways to produce bioenergy from solid biodiesel wastes in Colombia
Carlos A. García V., Valentina Aristizábal M., Carlos A. Cardona A.Instituto de Biotecnología y Agroindustria, Departamento de Ingeniería Química
Universidad Nacional de Colombia sede Manizales, [email protected], [email protected], [email protected]
IntroductionMethodologyResults and DiscussionConclusionsAcknowledgementsReferences
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Outline
2
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Introduction
3
Oil sources are
decreasing
Environmental
concerns
Uncertainty of oil prices
Policy for energy security
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Introduction
4
Alternative feedstocks
Alternative fuels
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Introduction
6
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Introduction
5
Palm Oil and Empty Fruit Bunches
Colombia is the fifth producer of palm oil in the world and the fourth world producer of oil palm due to its favorable agro-ecological conditions. Oil from palm and all the supply chain
RESIDUES should be considered as potential sources of products having an economic potential.
ColombianRaw
materials
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Introduction
7
Empty fruit bunches
Butanol Hydrogen Biogas
Palm oil
BiodieselEthanolC1 to C2
Second generation feedstockFirst generation feedstock
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Methodology
8
Extractives content
NREL/TP-510-42619
Ash contentNREL/TP-510-
42622
Holocellulose content
ASTM Standard D1104
Lignin contentmodified version of
TAPPI T222 acid-insoluble lignin in
wood and pulp
Raw Material Characterization Methods and Simulation Procedure
• Calculated using Aspen Process
Economic Analyzerat the Colombian
conditions
Economic Analysis
• Generated in Aspen Plus V8.0
(AspenTech) after flowsheet modelling
Mass and Energy Balances
• Process synthesis. knowledge-based
approach (Hierarchy, sequence and
integration concepts)
Methodological Approach
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Methodology
9
Description of Technologies
Butanol(1) Enzymatic hydrolysis
of cellulose, (2) ABE fermentation of glucose
using Clostridium beijerinckii
Hydrogen(1) Enzymatic hydrolysis
of cellulose, (2) Dark fermentation of glucose
using Anaerobic Digestion Model (ADM1)
Biogas Remaining material
submitted to anaerobic digestion
Empty fruit bunches
Palm oilBiodiesel
Transesterificationreaction with methanol and catalyzed by NaOH
Ethanol Glycerol as residue of
biodiesel production by fermentation using Escherichia coli
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Methodology
10
Process Simulation Description
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Results and Discussion
11
Experimental Characterization EFB
Component Content (wt %)Cellulose 13.75±0.44Hemicellulose 12.79±0.40Lignin 7.79±0.08Ash 0.63±0.04Moisture 65.04±1.80
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Results and Discussion
12
stand-alone biorefinery
Product YieldHydrogen 0.008 kg/kg EFB
Butanol 0.027 kg/kg EFB
Biogas 0.018 kg/kg EFB
Biodiesel 1.14 kg/kg palm oil*
Ethanol 0.31 kg/kg palm oil
Product YieldHydrogen 0.003 kg/kg EFB
Butanol 0.04 kg/kg sugars
Biogas 0.3 kg/kg EFB
Biodiesel 1.007 kg/kg palm oil*
Ethanol 0.27 kg/kg palm oil
*change for methanol or Ethanol
*Methanol
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Results and Discussion
13
Economic Analysis
0,00
10,00
20,00
30,00
40,00
50,00
60,00
70,00
Shar
e (%
)
HydrogenButanolBiogasBiodieselEthanol
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Results and Discussion
14
Economic Analysis of the biorefinery
-2,50E+07
-2,00E+07
-1,50E+07
-1,00E+07
-5,00E+06
0,00E+00
5,00E+06
1,00E+07
1,50E+07
0 2 4 6 8 10
NPV
Year
NPV (M. USD/year): 96.54
Payout Period (Years): 6.83
Production costs
Product Value Unit
Biodiesel 0.74 USD/kg
Hydrogen 1.35 USD/kg
Biogas 0.76 USD/kg
Butanol 1.41 USD/kg
Ethanol 0.56 USD/kg
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Conclusions
15
According to the results, a biorefinery to produce different energy carriers is seen as a clear idea for the integral utilization of raw materials such as EFB from biodiesel supply chain for the production of
biofuels.
The use of biomass as raw materials for bioenergy and biochemical production is encouraged by a reduction of fossil CO2 emissions, the need for a secure energy supply, and a revitalization of rural areas.
A key driver for the development and implementation of energy biorefineries is the growth in demand for energy and fuels.
The stand-alone option is weak when comparing it to a biorefinery that produces different energy carriers by the integral utilization of raw materials such as palm for the production of bioenergy.
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
Acknowledgments
16
The authors express their acknowledgments to the Universidad Nacional de Colombia at Manizales andresearch group on Procesos Químicos, Catalíticos y Biotecnológicos.
The authors express their acknowledgments to the Programa Nacional de Apoyo a Estudiantes dePosgrado para el Fortalecimiento de la Investigación, Creación e Innovación de la UniversidadNacional de Colombia 2013-2015.
The authors express their acknowledgments to the Convocatoria Nacional Jóvenes Investigadores eInnovadores 645 año 2014 of Departamento Administrativo de Ciencia, Tecnología e Innovación -Colciencias-.
R. Borja, a. Martín, E. Sánchez, B. Rincón, and F. Raposo, “Kinetic modelling of the hydrolysis, acidogenic andmethanogenic steps in the anaerobic digestion of two-phase olive pomace (TPOP),” Process Biochem., vol.40, no. 5, pp. 1841–1847, Apr. 2005.
R. Maria, D. B. Alves, C. Augusto, J. F. O. Granjo, B. P. D. Duarte, and M. C. Oliveira, Kinetic Models for theHomogeneous Alkaline and Acid Catalysis in Biodiesel Production, vol. 27, no. 1999. Elsevier Inc., 2009, pp.483–488.
V. Gadhamshetty, Y. Arudchelvam, N. Nirmalakhandan, and D. C. Johnson, “Modeling dark fermentation forbiohydrogen production: ADM1-based model vs. Gompertz model,” Int. J. Hydrogen Energy, vol. 35, no. 2, pp.479–490, Jan. 2010.
N. Chaudhary, M. O. Ngadi, B. K. Simpson, and L. S. Kassama, “Biosynthesis of Ethanol and Hydrogen byGlycerol Fermentation Using Escherichia coli,” vol. 2011, no. July, pp. 83–89, 2011.
L. E. Rincón, J. Moncada, and C. A. Cardona, “Analysis of potential technological schemes for the developmentof oil palm industry in Colombia: A biorefinery point of view,” Ind. Crops Prod., vol. 52, pp. 457–465, Jan. 2014.
L. E. Rincón, V. Hernández, and C. A. Cardona, “Analysis of technological schemes for the efficient production ofadded-value products from Colombian oleochemical feedstocks,” Process Biochem., vol. 49, no. 3, pp.474–489, Mar. 2014.
F. Cherubini, “The biorefinery concept: Using biomass instead of oil for producing energy and chemicals,” EnergyConvers. Manag., vol. 51, no. 7, pp. 1412–1421, Jul. 2010.
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales
References
17
Grupo de Investigación Procesos Químicos, Catalíticos y BiotecnológicosUniversidad Nacional de Colombia sede Manizales 18
Thank you for your attention
Carlos A. García V., Valentina Aristizábal M., Carlos A. Cardona A. Instituto de Biotecnología y Agroindustria, Departamento de Ingeniería Química
Universidad Nacional de Colombia sede Manizales, [email protected], [email protected], [email protected]