Energy Consumption at Size Reduction of Lignocellulose Biomass for Bioenergy

In order to obtain bioenergy (biogas, biofuel) or pellets, different types of lignocellulosic biomass are subjected to a mechanical pretreatment, first by size reduction, then by separating, and ultimately by fracturing or bio-refining. Biomass processing mainly refers to a grinding process that occ...

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Veröffentlicht in:Sustainability 2019-05, Vol.11 (9), p.2477
Hauptverfasser: Moiceanu, Georgiana, Paraschiv, Gigel, Voicu, Gheorghe, Dinca, Mirela, Negoita, Olivia, Chitoiu, Mihai, Tudor, Paula
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container_end_page
container_issue 9
container_start_page 2477
container_title Sustainability
container_volume 11
creator Moiceanu, Georgiana
Paraschiv, Gigel
Voicu, Gheorghe
Dinca, Mirela
Negoita, Olivia
Chitoiu, Mihai
Tudor, Paula
description In order to obtain bioenergy (biogas, biofuel) or pellets, different types of lignocellulosic biomass are subjected to a mechanical pretreatment, first by size reduction, then by separating, and ultimately by fracturing or bio-refining. Biomass processing mainly refers to a grinding process that occurs until reaching certain limits. The size reduction process, such as grinding, is an operation that is executed with different levels of energy consumption, considering biomass mechanical characteristics and the necessary grinding level. This paper, illustrates a comparative analysis of experimental results obtained by grinding multiple types of vegetal biomass (Miscanthus, corn stalks, alfalfa, willow) used in the process of bio-refining and bio-fracturing. Experiments were realized using both a laboratory knife mill Grindomix GM200 (Retsch GmbH, Haan, Germany), and a 22 kW articulated hammer mill, using different grinding system speeds and different hammer mill sieves. Results have shown that biomass mechanical pre-processing grinding leads to supplementary costs in the overall process through bio-refining or bio-fracturing in order to obtain bio-products or bio-energy. So, specific energy consumption for grinding using a hammer mill can reach 50–65 kJ/kg for harvested Miscanthus biomass, and 35–50 kJ/kg for dried energetic willow, using a 10 mm orifice sieve, values which increase processing costs.
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subjects Alfalfa
Alternative energy sources
Biodiesel fuels
Biogas
Biomass
Cellulose
Chemicals
Climate change
Corn
Crops
Densification
Energy consumption
Environmental impact
Food
Grasses
Lignin
Lignocellulose
Miscanthus
Mountains
Particle size
Physical properties
Pressure
Raw materials
Size reduction
Sulfur
Sulfur content
Sustainability
Wheat
title Energy Consumption at Size Reduction of Lignocellulose Biomass for Bioenergy
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