 Open Access Article
 Open Access Article
      
        
          
            Anqi 
            Ji
          
        
       ab, 
      
        
          
            Samarthya 
            Bhagia
ab, 
      
        
          
            Samarthya 
            Bhagia
          
        
       c, 
      
        
          
            Nara 
            Han
c, 
      
        
          
            Nara 
            Han
          
        
       a, 
      
        
          
            Kwang Ho 
            Kim
a, 
      
        
          
            Kwang Ho 
            Kim
          
        
       d, 
      
        
          
            Gyu 
            Leem
d, 
      
        
          
            Gyu 
            Leem
          
        
       e, 
      
        
          
            Nidia C. 
            Gallego
          
        
      f, 
      
        
          
            Shuyang 
            Zhang
e, 
      
        
          
            Nidia C. 
            Gallego
          
        
      f, 
      
        
          
            Shuyang 
            Zhang
          
        
       g, 
      
        
          
            Kai 
            Li
g, 
      
        
          
            Kai 
            Li
          
        
       h, 
      
        
          
            Soydan 
            Ozcan
          
        
      i, 
      
        
          
            Arthur J. 
            Ragauskas
h, 
      
        
          
            Soydan 
            Ozcan
          
        
      i, 
      
        
          
            Arthur J. 
            Ragauskas
          
        
       *cgjk and 
      
        
          
            Chang Geun 
            Yoo
*cgjk and 
      
        
          
            Chang Geun 
            Yoo
          
        
       *a
*a
      
aDepartment of Chemical Engineering, State University of New York, College of Environmental Science and Forestry, Syracuse, NY 13210, USA. E-mail: cyoo05@esf.edu
      
bDepartment of Chemical Engineering, Howard University, Washington, DC 20059, USA
      
cBiosciences Division, Oak Ridge National Laboratory, TN 37831, USA
      
dDepartment of Wood Science, University of British Columbia, Vancouver, BC V6T 1Z4, Canada
      
eDepartment of Chemistry, State University of New York, College of Environmental Science and Forestry, Syracuse, NY 13210, USA
      
fChemical Sciences Division, Oak Ridge National Laboratory, Oak Ridge, TN 37830, USA
      
gDepartment of Chemical and Biomolecular Engineering, University of Tennessee Knoxville, Knoxville, TN 37996, USA. E-mail: aragausk@utk.edu
      
hBuildings and Transportation Science Division, Oak Ridge National Laboratory, Oak Ridge, TN 37831, USA
      
iManufacturing Sciences Division, Oak Ridge National Laboratory, Oak Ridge, TN 37830, USA
      
jCenter for Bioenergy Innovation, University of Tennessee-Oak Ridge National Laboratory Joint Institute for Biological Science, Knoxville, TN 37831, USA
      
kDepartment of Forestry, Wildlife and Fisheries, Center for Renewable Carbon, University of Tennessee Knoxville, Institute of Agriculture, Knoxville, TN 37996, USA
    
First published on 3rd September 2025
Lignocellulosic biomass has been well-acknowledged as a filler for making 3D printed composites. The technical performances of composites were influenced by the characteristics of the components. The correlations between poplar biomass properties and the mechanical and thermal performances of the 3D printed poplar-plastic composites were investigated. The characteristics of poplar were modified by different pretreatment methods, including using hot water, dilute acid, and organic solvent (organosolv), and each treated poplar biomass was applied as a filler in a polylactic acid (PLA) polymer matrix to produce eco-friendly materials. These solvent pretreatments increased the hydrophobicity and surface area of poplar. Organosolv treated poplar showed the highest cellulose content and significantly increased Young's modulus of its biocomposites. Principal component analysis revealed that the specific surface area and water contact angle of biomass contributed to the thermal stability of biocomposites. Additionally, the degree of polymerization of cellulose and xylan content within the biomass correlated with the biocomposites' break stress. Notably, the crystallinity of biocomposites impacted the modulus of these materials. The reported relationships between biomass characteristics and 3D printed composite behaviors provide guidance for optimizing biomass processing in biocomposite applications.
| Sustainability spotlightThe heavy use of petroleum-based plastics has led to a global energy and environmental crisis. To address this problem, researchers shifted towards green, renewable, and environmentally friendly biopolymers and their composites. Lignocellulosic biomass has been applied to reinforce a variety of bioplastics. However, the complexity and heterogeneity of biomass limit their composite applications. This study investigates how the physicochemical properties of woody biomass, modified through various processing methods, affect the performance of 3D printed wood-reinforced PLA composites. Our findings highlight the relationship between biomass characteristics and 3D printed composite behavior, offering guidance for optimizing biomass processing in biocomposite applications. By demonstrating the potential to replace conventional plastics with biomass-based composites in 3D printing, the results in this study support the advancement of sustainable manufacturing practices in line with the United Nations Sustainable Development Goal 9: Industry, Innovation, and Infrastructure. | 
Commercially available thermoplastic materials such as acrylonitrile butadiene styrene (ABS), polypropylene (PP), polycarbonate (PC), polylactic acid (PLA), and polyetherimide (PEI) are commonly used in the FDM process. Among them, PLA is a renewable and biocompostable thermoplastic. Its monomer, lactic acid, is a biomass-derived platform chemical obtained through fermentation of carbohydrates. Due to the depletion of fossil fuels and the increasing environmental issues, lignocellulosic biomass has been a well-acknowledged alternative resource in many applications, such as bio-based fuels, chemicals, and materials.
In recent years, researchers have focused on biomass applications via 3D printing technology.4 Previous studies reported that the addition of wood to plastic polymers increased their stiffness and bending properties.5,6 Incorporating biomass as a reinforcing agent in biocomposite materials offers a promising strategy for reducing the environmental impact of 3D printed products. For example, Oh et al. demonstrated that even unconventional food-derived biomass, such as recycled tempura powder debris, can be successfully incorporated into biodegradable polymers for 3D printing, supporting the broader vision of sustainable additive manufacturing through biomass utilization.7 Biomass is typically degraded more rapidly compared to the current plastic resins; thus, its addition shortens the degradation time of end-of-life products, leading to sustainable waste management practices.8 However, the relatively low compatibility between biomass and typical commercial plastic resins often results in insufficient mechanical performance.9 Additionally, the complexity and variability of biomass structure and composition, along with its physicochemical properties such as infusibility and insolubility in common solvents, limit its use in 3D printing.10
In recent years, significant efforts have been made to incorporate wood into PLA to fabricate sustainable and compostable composites with enhanced mechanical and thermal performance. However, most studies have been conducted with a single pretreatment method or randomly selected feedstock, which are not directly comparable to explain how various chemical or physical treatments impact both biomass properties and composite performance. In this study, to elucidate the impacts of biomass characteristics such as chemical composition, surface properties, hydrophobicity, and structural properties on the printed biocomposite materials, three chemical modification methods: liquid hot water (LHW),11 dilute acid (DA),12 and organosolv13,14 pretreatments were applied to modify the biomass. Such a modification has not been carried out on biomass for the purpose of manufacturing 3D printed composites. Previous studies have shown that both LHW and DA selectively removed hygroscopic hemicellulose and increased the surface area, while organosolv pretreatment effectively removed amorphous components such as hemicellulose and lignin. The treated poplar was then used as a reinforcing filler in a PLA matrix, followed by extrusion and fabrication of 3D printed specimens via the FDM method. Also, we applied principal component analysis (PCA) to correlate these biomass characteristics with the mechanical and thermal properties of the resulting PLA composites. This multivariate statistical approach enables a more comprehensive understanding of structure–property–performance relationships, which have not been extensively explored in previous PLA/wood composite studies.
![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) :
:![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 8 (w/w) ratio at room temperature. The well-mixed sample was kept in a vacuum oven at 80 °C for 8 h in order to remove moisture. A filament extruder (Filabot EX2, Filabot, Barre, VT) equipped with an air-path and spooler and Lulzbot TAZ Workhorse 3D printer with a 0.5 mm SE Tool Head (FAME 3D, Fargo, ND) were used for filament formation and 3D printing. A Filabot EX2 single-screw extruder (length/diameter ratio of 12, 1.5875 cm screw diameter, 1.27 pitch, compression ratio of 2.5
8 (w/w) ratio at room temperature. The well-mixed sample was kept in a vacuum oven at 80 °C for 8 h in order to remove moisture. A filament extruder (Filabot EX2, Filabot, Barre, VT) equipped with an air-path and spooler and Lulzbot TAZ Workhorse 3D printer with a 0.5 mm SE Tool Head (FAME 3D, Fargo, ND) were used for filament formation and 3D printing. A Filabot EX2 single-screw extruder (length/diameter ratio of 12, 1.5875 cm screw diameter, 1.27 pitch, compression ratio of 2.5![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) :
:![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 1) was used to extrude the PLA/biomass filaments at 210 °C. Pure 2 mm knife-milled PLA was extruded to clean the extruder before starting each different extrusion run. After cleaning, the PLA/poplar mixture was loaded into the loading chute. The filament was then manually guided with no applied force and fan cooling. The filament produced by the first extrusion was then cut into ∼1 cm long cylindrical pellets and knife-milled through a 2 mm screen (mini Wiley mill, Thomas Scientific). Milled powder was kept in a vacuum oven under the same conditions mentioned above. After 8 h of drying, the powder then underwent extrusion for the second time (the exact same way as the first extrusion) to produce a filament 1.6 mm in diameter for 3D printing. In order to avoid cross-contamination by the leftover from previous materials in the extruder barrel, a 1.5 m length of the initial filament was discarded.
1) was used to extrude the PLA/biomass filaments at 210 °C. Pure 2 mm knife-milled PLA was extruded to clean the extruder before starting each different extrusion run. After cleaning, the PLA/poplar mixture was loaded into the loading chute. The filament was then manually guided with no applied force and fan cooling. The filament produced by the first extrusion was then cut into ∼1 cm long cylindrical pellets and knife-milled through a 2 mm screen (mini Wiley mill, Thomas Scientific). Milled powder was kept in a vacuum oven under the same conditions mentioned above. After 8 h of drying, the powder then underwent extrusion for the second time (the exact same way as the first extrusion) to produce a filament 1.6 mm in diameter for 3D printing. In order to avoid cross-contamination by the leftover from previous materials in the extruder barrel, a 1.5 m length of the initial filament was discarded.
        The ASTM D638 Type V15 3D printed test specimens were designed in FreeCAD 0.18.4. G-code and produced in Cura 3.6.21 Lulzbot Edition for a Lulzbot TAZ Workhorse (0.5 mm SE tool head and glass/PEI print surface using only perimeter filling (0% infill), 0.3 mm layer height, 0.6 mm line width, 230 °C printing temperature, 20 mm s−1 print speed, constant 40 °C build plate temperature, 160 °C probe, soften and wipe temperature, 3 mm s−1 retraction speed, 1 mm retraction distance, 10 mm s−1 nozzle switch retraction speed, 100% flow rate, 175 mm s−1 travel speed, 15 mm s−1 skirt speed with 3 skirts, no print cooling, 35 °C part removal temperature). The printing layer was started at the corner of the tensile shape grip end and printed one sample at a time with each PLA/poplar sample in triplicate. All extrusion and 3D printing parameters, including extrusion temperature, printing temperature, bed temperature, printing speed, and layer height, were kept constant for all samples to ensure consistency in processing conditions. Further detailed manufacturing and 3D printing information is available in the previous study.16
Morphological properties of the biomass powder prior to ball-milling were analyzed using Scanning Electron Microscopy (SEM, JEOL-JSM-IT100LA). The sample was vacuum dried, mounted on an aluminum stub with carbon tape and sputter coating with gold/palladium prior to the analysis. The particle size of ball-milled biomass was measured by using a laser diffraction analyzer (Malvern S3500). Each sample was measured in triplicate, using a reflecting particle setting, irregular shape, and 20 s ultrasonication. The Brunauer–Emmett–Teller (BET) specific surface area of the ball-milled biomass was measured by using an Autosorb Station (Quantachrome Instruments) under vacuum drying at 40 °C and an outgas time of 12 h using nitrogen. Water contact angle measurements were carried out on a Drop Shape Analyzer (Kruss Scientific) by the sessile drop method at 23 °C.
Cellulose Degree of Polymerization (DP) of the biomass was measured by using a gel permeation chromatography (GPC) SECurity 1200 system. α-cellulose was isolated from the biomass based on the previous studies.18 The weight-average degree of polymerization (DPw) of cellulose and number-average degree of polymerization (DPn) of cellulose were calculated from the measured cellulose molecular weight divided by the tricarbanilated cellulose repeating unit (519 g mol−1). Fourier transform infrared spectroscopy (FTIR) analysis of untreated and treated poplar was conducted using a Spectrum One FTIR Spectrometer (PerkinElmer, Wellesley, MA, USA) equipped with a universal attenuated total reflection (ATR) accessory. The spectra were measured between 4000 cm−1 and 600 cm−1 with an average of 16 scans per sample. Thermogravimetric analysis (TGA) was performed from room temperature to 600 °C at 10 °C min−1 on a Q500 (TA Instruments) under an airflow of 40 mL min−1. The onset temperature (decomposition temperature) of the sample was obtained from the curve based on ASTM E2550.19
The morphological properties of the 3D printed specimens were also characterized by SEM (JEOL-JSM-IT100LA) as described above. The water contact angle of the 3D printed specimens was investigated on a Drop Shape Analyzer (Kruss Scientific) as described above. Differential scanning calorimetry (DSC) analysis was performed in the heat/cool/heat mode on a Q200 instrument (TA Instruments). The testing specimens were ramped from 0 °C to 180 °C, followed by cooling to 0 °C and then heated up back to 180 °C at a ramping rate of 10 °C min−1. The glass transition temperature (Tg), cold crystallization temperature (Tcc), and melting temperature (Tm) were determined from the second heating curve. The degree of crystallinity (Xc)20 was calculated using eqn (1):
|  | (1) | 
TGA was performed from room temperature to 600 °C at 10 °C min−1 on a Q500 (TA Instruments) under an airflow of 40 mL min−1. The onset temperature (decomposition temperature) of the sample was obtained from the curve based on ASTM E2550.19
Table 1 shows the SSA and mean particle size of the ball-milled untreated, LHW treated, DA treated, and organosolv treated poplar. The untreated poplar had an SSA of 3.56 m2 g−1 and a particle size of 39.49 μm. LHW pretreatment increased the SSA of poplar to 4.12 m2 g−1 and decreased the particle size of biomass to 17.11 μm. A similar trend was observed by DA pretreatment, which resulted in a further increased SSA of 4.35 m2 g−1 and a slightly smaller particle size of 16.72 μm. In contrast, the organosolv treated poplar showed an SSA of 3.90 m2 g−1 and a larger particle size of 28.19 μm. The results indicated that all pretreatments decreased poplar particle size and increased SSA, which is consistent with the previous studies.28–30 Compared to other treated poplars, organosolv treated poplar showed lower SSA and higher particle size mean. As mentioned previously, the ball-milling process was conducted after the pretreatment processes. The organosolv pretreatment led to a higher cellulose fraction, which has a more crystalline structure, possibly resulting in larger particle sizes in the ball-milling process. Compared to the amorphous components such as lignin and hemicellulose in poplar, which are more readily fractured, cellulose resists further size reduction during the ball-milling process due to its resilient nature.31,32
| Sample | BET specific surface area (m2 g−1) | Particle size mean (μm) | 
|---|---|---|
| Untreated | 3.56 | 39.49 | 
| LHW | 4.12 | 17.11 | 
| DA | 4.35 | 16.72 | 
| Organosolv | 3.90 | 28.19 | 
![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) O stretching vibrations in hemicellulose and lignin, was reduced in treated biomass samples compared to that in untreated poplar, primarily due to the hemicellulose and/or lignin removals, as described in chemical composition results (Fig. 2). Among the pretreatments, the organosolv treated sample had the most significant reduction at peak 2, indicating high delignification and hemicellulose removal. The peak at 1610 cm−1 (peak 3), corresponding to asymmetric stretching of the carboxyl group of glucuronic acid in hemicellulose and C
O stretching vibrations in hemicellulose and lignin, was reduced in treated biomass samples compared to that in untreated poplar, primarily due to the hemicellulose and/or lignin removals, as described in chemical composition results (Fig. 2). Among the pretreatments, the organosolv treated sample had the most significant reduction at peak 2, indicating high delignification and hemicellulose removal. The peak at 1610 cm−1 (peak 3), corresponding to asymmetric stretching of the carboxyl group of glucuronic acid in hemicellulose and C![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) O stretching in conjugated carbonyl of lignin, became more obvious in the spectra of LHW and DA treated biomass, which could be explained with the relatively increased lignin content in the treated biomass by the removal of hemicellulose. In contrast, the spectrum of organosolv treated biomass showed a major decrease in this peak, indicating substantial lignin removal. Additional lignin-specific peaks at 1508 cm−1 (C
O stretching in conjugated carbonyl of lignin, became more obvious in the spectra of LHW and DA treated biomass, which could be explained with the relatively increased lignin content in the treated biomass by the removal of hemicellulose. In contrast, the spectrum of organosolv treated biomass showed a major decrease in this peak, indicating substantial lignin removal. Additional lignin-specific peaks at 1508 cm−1 (C![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) C–C aromatic ring stretching and vibration, peak 4) and 1457 cm−1 (C–H deformation in methyl and methylene, peak 5) were significantly lower in the spectrum of organosolv treated biomass, confirming its high delignification efficiency. Moreover, the peaks at 1160 cm−1 (peak 6) and 896 cm−1 (peak 7), attributed to C–O–C stretching in both cellulose and hemicellulose, became sharper and more intense with the organosolv treated biomass sample, reflecting an increased relative cellulose content and possibly enhanced crystallinity of poplar due to the removal of amorphous components like lignin and hemicellulose.38
C–C aromatic ring stretching and vibration, peak 4) and 1457 cm−1 (C–H deformation in methyl and methylene, peak 5) were significantly lower in the spectrum of organosolv treated biomass, confirming its high delignification efficiency. Moreover, the peaks at 1160 cm−1 (peak 6) and 896 cm−1 (peak 7), attributed to C–O–C stretching in both cellulose and hemicellulose, became sharper and more intense with the organosolv treated biomass sample, reflecting an increased relative cellulose content and possibly enhanced crystallinity of poplar due to the removal of amorphous components like lignin and hemicellulose.38
          ![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) O) in PLA can enhance interfacial adhesion and load transfer.39,40 The enhanced compatibility and interfacial reactions of biomass in the composites ensure a more uniform distribution of stress across the biocomposite, enhancing its mechanical properties. Thus, this strategy leverages the multifunctional role of biomass to overcome inherent weaknesses of PLA and broaden its utility in sustainable composite manufacturing.
O) in PLA can enhance interfacial adhesion and load transfer.39,40 The enhanced compatibility and interfacial reactions of biomass in the composites ensure a more uniform distribution of stress across the biocomposite, enhancing its mechanical properties. Thus, this strategy leverages the multifunctional role of biomass to overcome inherent weaknesses of PLA and broaden its utility in sustainable composite manufacturing.
          Fig. 5 summarizes the ultimate tensile stress, break stress, and Young's modulus of the composites. Pure PLA had the highest tensile stress of 59.0 MPa and break stress of 53.1 MPa, with a Young's modulus of 2.8 GPa, which were comparable values with the results in Zhao et al.'s study.5
Compared to pure PLA composites, the introduction of untreated poplar into PLA composites slightly reduced tensile stress (49.8 MPa) and break stress (49.7 MPa), likely due to poor interfacial adhesion between hydrophilic biomass and the hydrophobic PLA matrix. However, the composite stiffness increased significantly, with Young's modulus increasing to 3.3 GPa, mainly due to the high crystallinity and aspect ratio of cellulose enhancing the stiffness of biocomposites. The PLA/LHW and DA treated poplar composites showed further decreased tensile stress, 49.4 MPa for the PLA/LHW composite and 49.6 MPa for the PLA/DA one, and break stresses, 47.3 MPa for the PLA/LHW one and 47.2 MPa for the PLA/DA one, while maintaining a similar Young's modulus to the untreated biocomposites (PLA/LHW at 3.3 GPa and PLA/DA at 3.1 GPa). This suggests that although these pretreatments improved the hydrophobicity of poplar and reduced hemicellulose content, which could potentially aid dispersion,41 these changes did not translate into improved load-bearing capacity. For instance, pseudo-lignin formed after DA pretreatment improved the hydrophobicity of poplar, but it may not have a strong interfacial bonding with structural biomass components like cellulose, leading to a reduction in tensile stress.
However, the PLA/organosolv treated poplar composite exhibited a significant increase in Young's modulus to 3.7 GPa (34% improvement compared to that of pure PLA composite) with comparable tensile (48.8 MPa) and break stress (47.7 MPa) to other composites. The enhanced stiffness could be attributed to synergistic factors: (i) higher cellulose content (78.8%), which increased the crystallinity of the PLA matrix as a nucleating agent; and (ii) a more rigid fiber structure due to the removal of amorphous components such as hemicellulose and lignin. These structural advantages allowed the PLA/organosolv treated poplar composite to resist deformation more effectively, thereby enhancing the modulus without compromising strength.
Overall, all biomass composites showed a higher Young's modulus than pure PLA composites, which indicated that the addition of biomass as a filler improved the stiffness of the biocomposite, which was also observed in the previous study.16 However, no significant difference was found among PLA/poplar biocomposites in tensile stress and break stress, indicating that the effect of pretreatment was not significant on the tensile stress of the biocomposites. For Young's modulus, the PLA/organosolv treated poplar composites showed the highest modulus. This result was attributed to higher cellulose content because its crystalline structure provided stiffness to biocomposites. In the previous study, the cellulose fibers enhanced Young's modulus of biocomposites by providing a crystalline structure that resists deformation.42 The high aspect ratio of cellulose fibers also allows for effective load transfer from the PLA matrix to the cellulose fibers, thereby improving the overall stiffness of the composite.43 These previous observations align with the results in this study, suggesting that cellulose content in biomass significantly affected Young's modulus of the biocomposite.
Although the increased hydrophobicity of biomass through pretreatment could improve stress transfer between the particles and the matrix, the tensile stress and break stress were not improved. Thus, the tensile stress of PLA/poplar composites appeared to be dependent on the content of biomass in PLA rather than lignin modification.16 Hence, the hydrophobicity of biomass was not as significant as we hypothesized in the determination of the mechanical performance of the 3D printed biomass reinforced PLA composites. Instead, organosolv treated biomass addition led to better stiffness of PLA/biomass biocomposites than those of LHW and DA treated biomass.
In summary, the pretreatments (LHW, DA, and organosolv) enhanced the surface properties of poplar (more hydrophobic and hemicellulose removal) but did not significantly improve tensile stress or break stress compared to PLA/untreated poplar composites. However, the Young's modulus of the PLA/organosolv treated composite was significantly increased (3.8 GPa), highlighting the potential of pretreatment to enhance stiffness through improved crystallinity and cellulose content. Notably, PLA/untreated poplar composites exhibited comparable mechanical properties and even slightly higher tensile and break stress than PLA/treated poplar composites. These findings indicated that untreated poplar also has promising potential as a filler in biocomposites without additional chemical modification, potentially reducing processing costs and simplifying production.
On the other hand, biomass pretreatment remains a valuable strategy for modifying filler characteristics. As demonstrated by organosolv treated biocomposites, tuning parameters such as cellulose content and morphological properties can enhance specific properties like stiffness (modulus). Therefore, by strategically altering biomass composition and structure, the performance of biocomposites can be further optimized for specific applications. Since the characteristics and behaviors of biocomposites can be tailored through pretreatment parameters such as severity, future studies focused on fine-tuning pretreatment conditions, fiber size, and filler loading will be essential to fully investigate the potential of PLA/biomass biocomposites across diverse applications.
To investigate the impact of cellulose on the mechanical properties of the biocomposites, cellulose DP of untreated and treated poplar was analyzed. Fig. 6 shows the weight-average degree of polymerization (DPw) of cellulose, the number-average degree of polymerization (DPn) of cellulose, and the dispersity (Đ). The cellulose in untreated poplar showed a DPn of 1199 and DPw of 12![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 213, resulting in a Đ of 10.20, which indicated a relatively broad molecular weight distribution. However, the chemical pretreatment significantly reduced these values: the cellulose in LHW treated poplar had a DPn of 190, DPw of 1164, and Đ of 6.13; the DA treated poplar showed a DPn of 121, DPw of 2778, and Đ of 23.03; and the organosolv treated one showed a DPn of 336, a DPw of 3311, and a Đ of 9.88. The difference in cellulose DP and dispersity between LHW and DA treatments can be attributed to both the chemical severity and reaction conditions of the two pretreatments.44 LHW pretreatment was conducted at 200 °C for 20 minutes, selectively hydrolyzing hemicellulose while largely preserving cellulose.45 This mild, non-acidic process resulted in moderate DP values and a relatively narrow Đ, indicating uniform chain lengths. In contrast, DA pretreatment was performed at a lower temperature of 160 °C but with 0.5 wt% H2SO4, which not only removed hemicellulose but also partially degraded cellulose,46 leading to shorter cellulose chains and a broader molecular weight distribution. According to the results, there was no significant or direct correlation observed between cellulose DP and the mechanical properties of the PLA/poplar composites among the three different pretreatment methods. Although substantial changes in cellulose DP and dispersity in each pretreatment were observed, they were not involved in the enhancement of the mechanical properties of the biocomposites. However, it is worth noting that LHW and DA treated poplar showed similar chemical compositions but significantly different cellulose DP and Đ values. Despite DA treated poplar having a higher DPw and much broader Đ, the mechanical performance of its composite was similar to that of PLA/LHW treated poplar composites. This comparison suggests that cellulose DP may influence composite properties, but its effect is secondary to other factors such as interfacial adhesion and filler dispersion.
213, resulting in a Đ of 10.20, which indicated a relatively broad molecular weight distribution. However, the chemical pretreatment significantly reduced these values: the cellulose in LHW treated poplar had a DPn of 190, DPw of 1164, and Đ of 6.13; the DA treated poplar showed a DPn of 121, DPw of 2778, and Đ of 23.03; and the organosolv treated one showed a DPn of 336, a DPw of 3311, and a Đ of 9.88. The difference in cellulose DP and dispersity between LHW and DA treatments can be attributed to both the chemical severity and reaction conditions of the two pretreatments.44 LHW pretreatment was conducted at 200 °C for 20 minutes, selectively hydrolyzing hemicellulose while largely preserving cellulose.45 This mild, non-acidic process resulted in moderate DP values and a relatively narrow Đ, indicating uniform chain lengths. In contrast, DA pretreatment was performed at a lower temperature of 160 °C but with 0.5 wt% H2SO4, which not only removed hemicellulose but also partially degraded cellulose,46 leading to shorter cellulose chains and a broader molecular weight distribution. According to the results, there was no significant or direct correlation observed between cellulose DP and the mechanical properties of the PLA/poplar composites among the three different pretreatment methods. Although substantial changes in cellulose DP and dispersity in each pretreatment were observed, they were not involved in the enhancement of the mechanical properties of the biocomposites. However, it is worth noting that LHW and DA treated poplar showed similar chemical compositions but significantly different cellulose DP and Đ values. Despite DA treated poplar having a higher DPw and much broader Đ, the mechanical performance of its composite was similar to that of PLA/LHW treated poplar composites. This comparison suggests that cellulose DP may influence composite properties, but its effect is secondary to other factors such as interfacial adhesion and filler dispersion.
| Sample | T onset (°C) | T g (°C) | T cc (°C) | T m (°C) | X c (%) | 
|---|---|---|---|---|---|
| Pure PLA | 301.1 | 61.0 | — | 150.9 | 1.9 | 
| PLA/untreated poplar | 290.2 | 60.7 | 125.2 | 150.2 | 4.4 | 
| PLA/LHW treated poplar | 296.4 | 60.4 | 125.6 | 150.3 | 5.0 | 
| PLA/DA treated poplar | 294.7 | 60.7 | 125.7 | 150.1 | 4.7 | 
| PLA/organosolv treated poplar | 291.1 | 60.4 | 124.9 | 150.0 | 7.3 | 
Despite the similar Tg and Tm among the composites with untreated and treated poplar, the melting enthalpy and degree of crystallinity significantly increased by the addition of those poplar samples. In addition, the presence of a cold crystallization peak was observed with the addition of untreated and treated poplar. Cold crystallization occurs when crystallization happens during the heating process and above Tg due to the molecular chains regaining mobility, while below Tg, there will be a significant restriction.49 This observation showed that the additional loading of biomass could increase the crystallinity of the 3D printed composites and suggested that the biomass fillers could act as nucleating agent inducing the crystallization of PLA. Similar to traditional petroleum-based nucleating agents, with the addition of small molecular biomass into the PLA matrix, the biomass molecules could be dispersed in the matrix and increase the crystallization sites of PLA and nucleation density. As a result, the nucleation of PLA can occur at the site of small-molecule biomass, thereby shortening nucleation time. Consequently, this leads to an accelerated crystallization rate and increases the crystallinity of PLA.50 A simliar observation was also in Silva et al.'s study. They investigated the non-isothermal cold crystallization behavior of pure PLA and cork–polymer composites (CPC) using DSC at different heating rates. The results showed that Tcc significantly decreased with the addition of cork, and the authors concluded that cork can act as a nucleating agent during the non-isothermal cold crystallization process by increasing the crystallization rate of the PLA matrix.51
To study the effects of thermochemical pretreatments on the thermal properties of biomass and biocomposites, TGA was carried out. One onset temperature (Tonset) was observed from TGA chromatography. The TGA results provide the thermal stability of untreated and treated poplar samples (Fig. 8). The thermal degradation temperatures for untreated, LHW, DA, and organosolv treated poplar were 303.1 °C, 331.6 °C, 325.4 °C, and 322.8 °C, respectively. Untreated poplar showed a typical thermal degradation onset for lignocellulosic biomass due to the combined effects of cellulose, hemicellulose, and lignin. Among the treated samples, LHW treated poplar exhibited the highest thermal degradation onset temperature, indicating improved thermal stability, possibly due to the effective removal of hemicellulose, resulting in a residue with higher cellulose and lignin contents. Similarly, DA treated poplar and organosolv treated poplar had enhanced thermal stability compared to the untreated sample, which was due to the effective removal of hemicellulose, leading to a higher cellulose content.52 Although LHW and DA pretreatments resulted in similar chemical compositions, their thermal degradation behaviors were different. LHW treated poplar had a slightly higher onset temperature but lower residual mass compared to DA treated poplar, which is likely due to differences in the structural and chemical modifications induced by the two pretreatments. LHW pretreatment primarily hydrolyzed hemicellulose and partially solubilized low-molecular-weight fractions, producing a more thermally stable residue rich in cellulose and lignin. In contrast, DA pretreatment led to the formation of pseudo-lignin – a thermally stable, carbon-rich substance that is generated through acid-catalyzed dehydration of carbohydrates to furfural and 5-hydroxymethylfurfural (5-HMF) followed by their condensation and polymerization into aromatic structures.35,53 Pseudo-lignin was deposited on the fiber surface and contributes to the higher residual mass observed in DA treated samples, while potentially interfering with the overall thermal decomposition pathway. Overall, the TGA results indicated that pretreatment methods significantly impacted the thermal stability of poplar biomass, with LHW treatment providing the highest stability, followed by DA and organosolv treatments. These findings are essential for understanding how pretreatments affect the thermal properties of the biomass, which in turn impacts the performance of the resulting biocomposites.
These differences in the thermal stability of untreated and treated biomass were also reflected in the thermal behavior of the corresponding 3D printed biocomposites. As shown in Table 2, pure PLA exhibits the highest decomposition onset temperature at 301.1 °C, suggesting good thermal stability. The addition of untreated poplar decreases the decomposition onset temperature of the composite to 290.2 °C, indicating that the incorporation of poplar affected the thermal performance of composites. The PLA/LHW treated poplar composites demonstrate a slightly higher Tonset of 296.4 °C compared to other chemical pretreatments. The DA pretreatment resulted in a Tonset of 294.7 °C, while the PLA/organosolv treated poplar composite displays the lowest decomposition onset temperature at 291.1 °C among the chemical pretreatments. As a result, with the addition of untreated and treated poplar, the decomposition temperature of composites was decreased compared to that of pure PLA which was mainly due to the low decomposition temperature of poplar. However, with the highest xylan and lignin removals, the PLA/organosolv treated poplar composite had the lowest decomposition temperature, while the PLA/LHW treated poplar composite having more lignin content showed the highest decomposition temperature among the PLA/treated poplar composites. This observation suggested that the chemical composition in the biomass can greatly impact the thermal stability of polymer composites due to lignin having higher decomposition temperatures compared to hemicellulose and cellulose.54 Additionally, it is important to acknowledge that the varying molecular weights of biomass components also contribute to differences in their respective decomposition temperatures.55
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| Fig. 10 Biplots of the first principal component (PC1) and second principal component (PC2) from a PCA analysis. | ||
First, the SSA and WCA, representing the surface characteristics of the biomass, were shown to have a relationship with the thermal decomposition behavior of the composites. SSA represents the total surface area per unit mass of the material. In biomass, higher SSA means a larger surface area, which could impact the rate of thermal degradation.58 High SSA also led to extensive interfacial interactions between the biomass and the polymer matrix, enhancing the thermal stability of biocomposites by promoting better stress distribution and heat dissipation throughout the material.59,60 Additionally, the particle size of biomass was found to have a negative correlation with SSA, suggesting that finer particles with higher surface area enhance interfacial adhesion, thereby improving composite thermal stability. WCA also affected the interactions between the biomass particles and the polymer matrix during the thermal decomposition process. For example, if the biomass is hydrophilic (low WCA), it may not bond well with hydrophobic polymers, which could lead to degradation at lower temperatures. On the other hand, if the biomass is hydrophobic (high WCA), it can interact more strongly with the polymer matrix, potentially improving the thermal stability of the biocomposite. Hence, the WCA affects the interfacial bonding between biomass and the polymer matrix, further impacting the thermal stability.61,62 In our study, DA treated poplar exhibited the highest WCA (76 ± 3°), and the corresponding composites showed higher onset degradation temperature (294.7 °C) than the untreated one (290.2 °C), indicating enhanced interfacial compatibility and thermal resistance. However, the lignin content of biomass was oriented in the same direction as the decomposition temperature of biocomposites but in the opposite direction from the modulus of biocomposites, implying a positive correlation with thermal stability but a negative correlation with stiffness. Although lignin is thermally stable, its complex and amorphous structure may interfere with PLA crystallization and interfacial compatibility, potentially reducing the rigidity of the biocomposites.63
For mechanical properties, the cellulose DPs and xylan content in the biomass appear to be correlated with the break stress of the biocomposites. Longer cellulose chains (high DP) are generally associated with improved mechanical properties due to their capacity to entangle more effectively, hence distributing applied stress more evenly. Thus, biocomposites with a higher cellulose DP in the biomass can have a better ability to sustain load up to the point of fracture.64,65 For instance, the PLA/untreated poplar composites contained cellulose with the highest DP (DPn of 1199 and DPw of 12![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 213), exhibited higher break stress compared to the PLA/treated biomass composites, further supporting the correlation between the cellulose chain length and stress-bearing capacity. Moreover, xylan, as an amorphous polysaccharide, can impact the properties of biocomposites differently. The removal of xylan may enhance the dispersion of cellulose fibers, thus improving the uniformity and tensile stress of the composites. However, in some cases, small amounts of amorphous xylan can act as “glue” to facilitate better stress transfer between the biomass filler and the polymer matrix by improving compatibility or adhesion at the interface, which could positively impact the break stress.66,67 In our study, the PLA/untreated poplar composite with relatively high xylan content in untreated poplar demonstrated break stress values (49.7 MPa) similar to those of treated samples, suggesting that retained xylan may contribute positively to stress transfer in some cases.
213), exhibited higher break stress compared to the PLA/treated biomass composites, further supporting the correlation between the cellulose chain length and stress-bearing capacity. Moreover, xylan, as an amorphous polysaccharide, can impact the properties of biocomposites differently. The removal of xylan may enhance the dispersion of cellulose fibers, thus improving the uniformity and tensile stress of the composites. However, in some cases, small amounts of amorphous xylan can act as “glue” to facilitate better stress transfer between the biomass filler and the polymer matrix by improving compatibility or adhesion at the interface, which could positively impact the break stress.66,67 In our study, the PLA/untreated poplar composite with relatively high xylan content in untreated poplar demonstrated break stress values (49.7 MPa) similar to those of treated samples, suggesting that retained xylan may contribute positively to stress transfer in some cases.
Finally, the PCA result showed that the modulus of biocomposites was closely related to the degree of crystallinity, while the glucan content is positioned in a similar direction as Xc, indicating a positive correlation. This suggests that higher glucan content in biomass contributes to increased crystallinity in the composite, since most glucan in biomass is from cellulose. As the Xc of biocomposites increases, so does the stiffness, leading to a higher Young's modulus. This enhancement of stiffness suggested that the biomass fillers can act as nucleating agents to promote the crystallization of PLA, thereby improving the rigidity of the biocomposite material.68,69 For example, the organosolv treated biocomposite showed the highest crystallinity (Xc = 7.3%) and also exhibited the highest Young's modulus (3.7 GPa), clearly demonstrating this relationship. In contrast, cellulose dispersity of biomass was oriented in the opposite direction from both Xc and modulus of biocomposites in the PCA plot, implying a negative correlation. This indicates that broader molecular weight distributions may hinder the uniform chain packing and reduce the efficiency of PLA crystallization. As a result, higher cellulose dispersity could compromise the stiffness of the resulting biocomposites, further emphasizing the importance of uniform cellulose chain length in optimizing mechanical properties. For example, although DA treated poplar and LHW treated poplar had similar chemical composition, the DA treated biomass exhibited a much higher cellulose dispersity (Đ = 23.03) compared to LHW treated biomass (Đ = 6.13). This broader molecular weight distribution in DA treated cellulose is consistent with a lower Young's modulus (3.1 GPa) in the corresponding composite compared to the LHW treated one (3.3 GPa), suggesting that high cellulose dispersity may limit stiffness enhancement despite comparable cellulose content.
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