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Transcript of 317 electo silva acv del biodiesel de palma incluyendo la utilización de residuos para...
ACV del biodiesel de palma incluyendo la utilización de
resíduos para la generación de electricidad
IV Congreso de Energias Renovables y Biocombustibles, UNAL, Lima, Perú
Prof. Dr. Electo Eduardo Silva Lora
NEST/IEM/UNIFEI
For references look at:
Zoneamiento agro-ambiental en
Brasil
ASPECTOS DE SOSTENIBILIDAD DE BIOCOMBUSTIBLES EN BRASIL: BIODIESEL
Anos de experiência na produção de etanol, incluindo o desarrolho de motores para o uso
de etanol puro.
Programa Nacional de Produção e Uso do Biodiesel: 2004
Capacidade atual de mais de 500 milhões de litros anuais
5
6
LIMITACIONES DEL ACV
• La metodologia ACV no es capaz de considerar/incluir todos los
impactos relevantes (uso de la tierra y del agua, cambios indirectos
en el uso de la tierra y la competición con los alimentos) .
• El ACV falla al considerar la reducción en el uso del suelo relacionada
con la utilización de co-productos. con la utilización de co-productos.
• Se necesita de un abordaje mas amplio (tal como la EAI - Evaluación
Ambiental Integrada ).
• Alto número de categorias de impactos ambientales, lo que dificulta
el proceso de toma de decisiones.
INCONSISTENCIAS DEL ACV
ABORDAJE DE LA CERTIFICACIÓN BASEADA EM LA SOSTENIBILIDAD ??????????
TODO EL MUNDO HABLA DE ESTO !!
Experiencia del NEST/UNIFEI en estudios de sostenibilidad utilizando el ACV.
Desde el año 2004 el NEST/UNIFEI ha realizado los
siguientes estudios utilizando la ACV:
• Biodiesel de palma,
• Tratamiento y disposición de vinazas de etanol,
• Metanol a partir del bagazo de caña.
• Aprovechamiento energético de los resíduos sólidos
urbanos.
C2
C3
C1
C1 C2 C3
Location in Colombia Eastern Region Northern Region Ce ntral Region
Palm area, Adults (ha) 1,200 3,436 4,675
Palm area, nursery (ha) 1,100 64 130
Crop Density (Palm trees ha-1)
145 143 143
FFB Production (ton FFB yr -1)
30,000 85,898 98,175
FFB Process
CHARACTERISTICS AND PARAMETERS OF THE THREE EVALUATED COMPANIES
FFB Process(ton yr -1)
101,324 85,898 154,352
Productivity (ton FFB ha-yr -1)
25 25 21
OER(Oil Extraction Rate, %)
19.8 21.1 20.4
Oil Yield(ton oil ha-yr -1)
4.95 5.27 4.28
Brief description of the energy supplies facilities
Isolated system using diesel
and biogas in engines
Purchase all electricity from
the grid
Electricity from the grid and low
efficiency cogeneration
del biodiesel de palmaEsquema del inventario de ciclo de vida
del biodiesel de palma
RESIDUOS DE
BIOMASA
EFB (20-23%)
CACHOS VACIOS FRESCOS -FFB
100 %
Fruto de la palma
Fibras (11-14%)
Cáscaras (5-7%)
124.8 GJ/ ha.year
ETAPA AGRÍCOLA
INPUTS DE ENERGIA EN LA ETAPA INPUTS DE ENERGIA EN LA ETAPA AGRÍCOLA
INPUTS DE ENERGIA DURANTE LA INPUTS DE ENERGIA DURANTE LA EXTRACCIÓN DEL ACEITE
PARTICIPATION OF LC STAGESIN TOTAL ENERGY CONSUMPTION
Inventario global del ciclo de vida del Inventario global del ciclo de vida del biodiesel de palma
Uso racional de Fertilizantes
Biometanol oetanol
FertilizantesVINAZAS ???
C2C3
RELACIÓN UTPUT/INPUT (renovable/fosil)
C1
Seven thermal cogeneration schemes for the palm oil industry were simulated by using Gatecycle software version 5.0.1, considering different sources and levels of biomass use with a condensing-extraction (CET) and back pressure turbines (BPT) with high pressure boilers (cases A, B, C, F, E F end G).
PERCENTAGE OF BIOMASS PRODUCED DURING OIL EXTRACTION PROCESS USED AS A FUEL
IN THE BOILER
Case Turbine
% of biomass used as a fuel in the boiler
Fiber Shell EFB Biogas
A BPT 75 75 -- --A BPT 75 75 -- --
B CET 100 50 -- --
C CET 100 100 -- --
D BPT 100 100 100 100
E CET 100 100 50 --
F CET 100 100 100 --
G CET 100 100 100 100
30 t FFB/h plant, steam parameters were 2 MPa and 350°C.
Fuel(MW)
Power(MW)
Heat Rate(MJ/kWh)
Effic. of Electricity Generation
* (%)
Generation Index
(kWh.kg -1. biodiesel)
A 21.013 1,74 39.10 9.21 0.2014
Electricity generation index of the cogeneration systems.
B 22.546 1,86 39.25 9.17 0.2153
C 28.010 2,84 32.04 11.24 0.3287
D 51.814 3,96 40.84 8.81 0.4583
E 38.698 4,98 24.55 14.66 0.5764
F 49.368 7,03 21.88 16.45 0.8136
G 51.814 7,55 21.42 16.80 0.8738
Output/Input relation for biodiesel production life cycle.
INPUT [MJ / kg Biodiesel] C1 C2 C3
Agricultural stage 3.20 4.23 2.63
Oil Extraction with Cogeneration
1.06 1.27 0.72
Oil Refining 0.98 0.98 0.98
Transesterification 5.01 5.01 5.01
Total Input 9.96 11.20 9.05
OUTPUT [MJ / kg Biodiesel]
C1 C2 C3Biodiesel]
C1 C2 C3
Fiber 0.85 0.72 0.66
Shell, 2.79 2.64 1.85
Biogas 0.05 0.05 0.05
Kernel cake 2.54 2.38 2.46
Kernel Oil 6.00 5.64 5.82
Glycerin 2.09 2.09 2.09
Fatty acids 1.27 1.27 1.27
Biodiesel 39.60 39.60 39.60
Total Output 55.22 54.42 53.83
O/I (using EFB as Fertilizer)
5.54 4.86 5.95
Case C2 (Without
Cogeneration) Case A Case G
Surplus Generation Index (kWh kg -1biodiesel)
0.00 0.201 0.979
INPUT (MJ/kg biodiesel)
Agricultural stage 3.93 3.93 4.23
Impact of cogeneration on input/output index
Oil Extraction 1.27 0.92 0.92
Oil Refining 0.98 0.98 0.98
Transesterification 5.01 5.02 5.02
Total Input 11.20 10.86 11.16
OUTPUT (MJ/kg biodiesel)
Biodiesel 39.60 39.60 39.60
Electricity - Cogeneration 0.00 0.70 3.05
Total Output 54.42 55.12 54.05
Output /Input 4.86 5.08 4.85
• The LCA for two cases (cases C2 and G) were carried out using the Simapro software and the results were compared with the fossil diesel production LCA indexes diesel production LCA indexes (at the refinery) through data available in the Simapro database.
Mid Point Categories C2/G In relation to C2, (%)
Carcinogens -2.41
Non-Carcinogens -0.67
Respiratory inorganics -4.50
Ionizing radiation -4.25
Ozone layer depletion -33.31
Respiratory organics -6.92
Aquatic ecotoxicity -4.15Aquatic ecotoxicity -4.15
Terrestrial ecotoxicity 0.23
Terrestrial acidification -1.20
Land use -148.11
Aquatic acidification -3.53
Aquatic eutrophication 3.32
Global warming -7.64
Non-renewable energy -16.62
Mineral extraction -11.63
Impact assessmentSingle scoreIMPACT 2002+ method.
C2 C2/G
Damage category Case C2 Case C2/G % Reduction
Total -5.85E-5 -7.925E-5 -35.457
Human Health 3.66E-5 3.517E-5 -4.068
Ecosystem Quality 1.153E-5 1.143E-5 -0.874
Climate Change -0.000152 -0.000164 7.643
Resources 4.53E-05 3.78E-5 -16.619
END
PO
INTS
CA
TEG
OR
IES
C2
FOSSIL DIESEL
C2/G
END
PO
INTS
CA
TEG
OR
IES
CONCLUSIONS AND REMARKS
• The potential for energy production from oil palm biomass residues is 124.8 GJ ha-1 year-1
• Transterification stage have the greater fossil energy input due to the methanol utilization. Efforts must be done for the commercial implementation of the methyl route seeking an increase of biodiesel LC sustainability.seeking an increase of biodiesel LC sustainability.
• The electricity generation index can reach 1.02 kWh per kg of biodiesel when the residues are fully used and a condensing steam turbine with high steam parameters is employed.
• The Output/Input energy ratio for the palm oil biodiesel reaches values as 5.08, almost 3.5 greater than other biodiesels from different vegetable oils.
CONCLUSIONS AND REMARKS
• Outpu/Input index is not able to accurately consider the
effect of cogeneration implementation as the energy
output of biomass residues is evaluated based on its
calorific value.
• In relation to the conventional process, the case with • In relation to the conventional process, the case with
cogeneration presents a very high positive impact on
Land occupation (-148%), Ozone layer depletion (-33%)
and non-renewable energy consumption (-16.62 %).
• Life cycle equivalent CO2 emissions were also reduced
from -0.5346 to -1.4053 kg for biodiesel with and without
cogeneration, respectively.
ESTUDIO DE ACV – Tratamiento de lasESTUDIO DE ACV – Tratamiento de lasvinazas del etanolvinazas del etanolvinazas del etanol
FCDCC- Fertirrigación “in natura”
SCDTT - Concentración de vinazas hasta 40 % y fertirrigación
ABDCC - DIGESTIÓN ANAERÓBIA
SCCBA - CONCENTRACIÓN Y COMBUSTIÓN DE VINAZAS
CONCLUSIONESCONCLUSIONES
• La evaluación de la sostenibilidad es un problema multicriterial.
• La eficiencia energética atraves de la cogeneración baseada en sub-productos y la reducción del consumo de energia en lasdiferentes etapas del ciclo de vida deven ser considerada.
• La metodologia ACV debe ser mejorada y normalizada. Incertezas a resolver: volatilizacion de los componentes de los fertilizantes, asignación de co-productos e impactos del uso de la tierra.
• La certificación baseada en la reducción de las emisiones de GEI, utilizando como herramienta la ACV es actual y debemossaber utilizarla a nuestro favor.
ACKNOWLEDGEMENTS
• The authors are very grateful to the Oil Palm Research Center of Colombia -CENIPALMA and the palm oil mills for providing all the information, so that this providing all the information, so that this study could be carried out.
• Also to the Science Foundation of the Minas Gerais State – FAPEMIG and the National Research Council CNPq for the finantial support and grants.
Prof. Dr.Electo Silva Lora