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A versatile twin-screw extrusion process to provide an efficient thermo-mechano-chemical pretreatment on lignocellulosic biomass was developed, which leads to an increased average fiber aspect ratio. A natural binder can also be added continuously after fiber refining, leading to bio-based fiberboards with improved mechanical properties after hot pressing of the obtained extruded material.
A versatile twin-screw extrusion process to provide an efficient thermo-mechano-chemical pre-treatment on lignocellulosic biomass before using it as source of mechanical reinforcement in fully bio-based fiberboards was developed. Various lignocellulosic crop by-products have already been successfully pre-treated through this process, e.g., cereal straws (especially rice), coriander straw, shives from oleaginous flax straw, and bark of both amaranth and sunflower stems.
The extrusion process results in a marked increase in the average fiber aspect ratio, leading to improved mechanical properties of fiberboards. The twin-screw extruder can also be fitted with a filtration module at the end of the barrel. The continuous extraction of various chemicals (e.g., free sugars, hemicelluloses, volatiles from essential oil fractions, etc.) from the lignocellulosic substrate, and the fiber refining can, therefore, be performed simultaneously.
The extruder can also be used for its mixing ability: a natural binder (e.g., Organosolv lignins, protein-based oilcakes, starch, etc.) can be added to the refined fibers at the end of the screw profile. The obtained premix is ready to be molded through hot pressing, with the natural binder contributing to fiberboard cohesion. Such a combined process in a single extruder pass improves the production time, production cost, and may lead to reduction in plant production size. Because all the operations are performed in a single step, fiber morphology is better preserved, thanks to a reduced residence time of the material inside the extruder, resulting in enhanced material performances. Such one-step extrusion operation may be at the origin of a valuable industrial process intensification.
Compared to commercial wood-based materials, these fully bio-based fiberboards do not emit any formaldehyde, and they could find various applications, e.g., intermediate containers, furniture, domestic flooring, shelving, general construction, etc.
Extrusion is a process during which a flowing material is forced through a hot die. Extrusion, therefore, permits the forming of preheated products under pressure. The first industrial single-screw extruder appeared in 1873. It was used for the manufacture of metallic continuous cables. From 1930 onwards, single-screw extrusion was adapted to the food industry to produce sausages and past. Conversely, the first twin-screw extruder has first been used for developments in the food industry. It did not appear in the field of synthetic polymers until the 1940s. For this purpose, new machines were designed, and their operation was also modeled1. A s....
1. Prepare the raw materials
During the fiber refining of oleaginous flax shives using configuration (step 3.1.1), water was deliberately added at a liquid/solid ratio equal to 1.0. According to previous works25,26,27, such a liquid/solid ratio better preserves the length of the refined fibers at the twin-screw extruder outlet than lower ratios, which simultaneously contributes to an increase in their average aspect ratio. Furthermore, the amount of water a.......
The protocol outlined here describes how to process the extrusion-refining of lignocellulosic fibers before using them as mechanical reinforcement in renewable boards. Here, the twin-screw extruder used is a pilot scale machine. With screws of 53 mm in diameter (D), it is equipped with eight modules, each 4D in length, except for module 1 that has an 8D length, corresponding to a 36D total length (i.e., 1,908 mm) for the barrel. Its length is long enough to apply to the processed material the succession of several elemen.......
The authors have nothing to disclose.
The authors would like to express their sincere gratitude to Région Occitanie (France) that funded this research through ERDF (GEOFIBNET project, grant number MP0013559).
....Name | Company | Catalog Number | Comments |
Analogue durometer | Bareiss | HP Shore | Device used for determining the Shore D surface hardness of fiberboards |
Ash furnace | Nabetherm | Controller B 180 | Furnace used for the mineral content determinations |
Belt dryer | Clextral | Evolum 600 | Belt dryer used for the continuous drying of extrudates at the exit of the twin-screw extruder |
Cold extraction unit | FOSS | FT 121 Fibertec | Cold extractor used for determining the fiber content inside solid materials |
Densitometer | MA.TEC | Densi-Tap IG/4 | Device used for determining apparent and tapped densities of extrudates once dried |
Double-helix mixer | Electra | MH 400 | Mixer used for preparing the solid mixture made of the raw shives and the plasticized linseed cake for producing board number 12 |
Fiber morphology analyzer | Techpap | MorFi Compact | Analyzer used for determining the morphological characteristics of extrusion-refined shives |
Gravimetric belt feeder | Coperion K-Tron | SWB-300-N | Feeder used for the quantification of the oleaginous flax shives |
Gravimetric screw feeder | Coperion K-Tron | K-ML-KT20 | Feeder used for the quantification of the plasticized linseed cake |
Hammer mill | Electra | BC P | Crusher used for the grinding of granules made of plasticized linseed cake |
Heated hydraulic press | Pinette Emidecau Industries | PEI 400-t | Hydraulic press used for molding the fiberboards through hot pressing |
Hot extraction unit | FOSS | FT 122 Fibertec | Hot extractor used for determining the water-soluble and fiber contents inside solid materials |
Image analysis software | National Institutes of Health | ImageJ | Software used for determining the morphological characteristics of raw shives |
Oleaginous flax straw | Ovalie Innovation | N/A | Raw material supplied for the experimental work |
Piston pump | Clextral DKM | Super MD-PP-63 | Pump used for the water quantification and injection |
Scanner | Toshiba | e-Studio 257 | Scanner used for taking an image of raw shives in gray level |
Side feeder | Clextral | E36 | Feeder used to force the introduction of the plasticized linseed cake inside the barrel (at the level of module 5) for configuration (b) |
Thermogravimetric analyzer | Shimadzu | TGA-50 | Analyzer used for conducting the thermogravimetric analysis of the solids being processed |
Twin-screw extruder | Clextral | Evolum HT 53 | Co-rotating and co-penetrating pilot scale twin-screw extruder having a 36D total length (D is the screw diameter, i.e., 53 mm) |
Universal oven | Memmert | UN30 | Oven used for the moisture content determinations |
Universal testing machine | Instron | 33R4204 | Testing machine used for determining the bending properties of fiberboards |
Ventilated oven | France Etuves | XL2520 | Oven used for the discontinuous drying of extrudates at the exit of the twin-screw extruder |
Vibrating sieve shaker | RITEC | RITEC 600 | Sieve shaker used for the sieving of the plasticized linseed cake |
Vibrating sieve shaker | RITEC | RITEC 1800 | Sieve shaker used for removing short bast fibers entrapped inside the oleaginous flax shives |
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