Open Access Article
Asuka Yanagawa
a,
Asami Suzukia,
Anri Watanabe
a,
Takashi Makino
a,
Yuichiro Otsuka
b and
Kazuhiro Shikinaka
*a
aResearch Institute for Chemical Process Technology, National Institute of Advanced Industrial Science and Technology (AIST), Nigatake, 4-2-1, Miyagino-ku, Sendai 983-8551, Japan. E-mail: kaz.shikinaka@aist.go.jp
bForestry and Forest Products Research Institute, Matsunosato, 1, Tsukuba 305-8687, Japan
First published on 10th February 2026
In this work, the film forming abilities, gas barrier properties, and ultraviolet (UV) barrier properties of composite films composed of lignin derivatives and polyethyleneimine (PEI) were investigated. Three types of lignin derivatives were employed, namely SESC lignin (SESC) obtained by simultaneous enzymatic saccharification and comminution, along with lignosulfonate (LS) and soda lignin (Soda), which were obtained through pulping processes. All three lignin derivatives produced uniform films under appropriate conditions through the formation of polyion complexes (PICs) with PEI, which occurred via ionic interactions. The gas and UV barrier properties of the resulting films were tunable depending on the type of lignin derivative, the molecular weight of PEI, and the mixing ratio. Notably, the films composed of SESC and PEI exhibited excellent barrier properties while maintaining high transparency. Since these composite films can be produced in aqueous systems without the use of organic solvents, they offer potential for application in environmentally friendly packaging materials.
Lignin, which is the most abundant aromatic polymer in nature, is the second most prevalent natural polymer after cellulose.7,8 Although approximately 100 million tons of lignin are produced annually, roughly 98% is discarded as a by-product of the paper industry, and only around 2% is actually utilized.9 Furthermore, conventional lignin extraction methods (including Kraft, sulfite, alkaline, organosolv, steam explosion, and hydrolysis processes)10 often involve high temperatures, pressures, and the use of organic solvents, resulting in a high environmental impact and degradation of the lignin structure.
To overcome these issues, our group previously reported a novel lignin extraction method, namely simultaneous enzymatic saccharification and comminution (SESC process).11,12 This technique facilitates the isolation of polysaccharides as a sugar solution and lignin as an aqueous dispersion under conditions that minimize the environmental impact. Additionally, composite materials incorporating a lignin derivative from the SESC process (hereafter referred to as SESC lignin), together with polymers and clays, have demonstrated effective ultraviolet (UV) absorption in a poly(vinyl alcohol) matrix,13 as well as exhibiting gas barrier properties when combined with polymers and clays.14 These observations suggest that such composites could exhibit gas barrier properties while retaining the UV barrier properties of lignin derivatives.
The preparation of composite films by mixing lignin derivatives and polyethyleneimine (PEI) is therefore desirable to provide films with gas barrier properties. PEI is a cationic polymer containing primary, secondary and tertiary amines, and is known to form complexes with anionic polymers, such as lignin. Thin films composed of lignin derivative and PEI have been prepared via a layer-by-layer (LbL) approach, and multi-layered structures have been applied to bio-based coatings and nanofiltration membranes.15 Additionally, Shi et al. reported that composite materials consisting of a double-hydrophilic diblock copolymer and sodium lignosulfonate, formed polyion complexes (PICs) through electrostatic attractions.16 Such PICs effectively reduce gas permeability by densifying the structures of the composite films. The use of PICs also enables film formation via simple solution casting without the requirement for multiple steps, such as those employed in the conventional LbL approach, thereby providing a simpler and more practical process. However, to the best of our knowledge, the PIC-based preparation of films exhibiting gas-barrier properties using lignin derivative and PEI has not yet been investigated.
The aim of the present study is therefore to prepare composite films by solution casting through the formation of PICs between lignin derivatives and PEI, and to investigate the effect of the lignin derivative type on the gas and UV barrier properties. For this purpose, PEI is mixed with three types of lignin derivatives, namely SESC lignin and two representative lignin derivatives extracted by steam cooking, i.e., lignosulfonate (LS) and soda lignin (Soda) (Fig. 1). Subsequently, the effects of different lignin species and the PEI molecular weight on the resulting gas barrier properties are investigated using helium as a model gas due to its small kinetic diameter and similar permeability to hydrogen.17 The ability of the aromatic structure of lignin to impart UV protection properties to the composite films is investigated. Such films could potentially protect polymeric materials from UV-induced degradation, rendering them suitable for use in packaging applications.
000) and the polyethyleneimine solution (50 wt% in H2O, Mw = 70
000) were purchased from Wako Pure Chemical Industries, Ltd, Japan and Sigma-Aldrich Co., USA, respectively. Ethanol (>99.5%, Wako Pure Chemical Industries, Ltd, Japan) was used as received without additional purification. Ultrapure water obtained from a water purification system (Milli-Q® Advantage A10® system, Millipore, Germany), was used throughout the experiments.
To obtain SESC lignin, cedar powder, an equal amount of OPTIMASH XL (containing cellulase and xylanase) and OPTIMASH BG (containing xylanase and β-glucosidase) from DuPont™ Genencor® Science, and 100 mM phosphate buffer (pH 6.0) were processed by grinding using zirconia beads and bead milling (Labstar® LMZ015, Ashizawa Finetech Ltd, Japan) at 50 °C under a peripheral velocity of 14.0 m s−1. The inner wall of the LMZ015 instrument was covered with ceramic to prevent enzyme degradation during the process. After 2 h, the resulting mixture was subjected to centrifugation at 10
000×g for 30 min. The precipitate was then milled again under the same enzyme and buffer conditions. Subsequently, the slurry was subjected to centrifugation under the conditions described above, and the precipitate was washed twice with an equal volume of ultrapure water. Centrifugation was repeated once again under the same conditions to afford the brown SESC lignin as a residue.
000), films were generated across broad lignin/PEI ratios ranging from 10
:
90 to 67
:
33, although a ratio of 10
:
90 led to a slightly viscous film due to the excess PEI. On the other hand, no film was formed at a lignin/PEI ratio of 75
:
25, where lignin was in excess. At lignin contents >75 wt%, a precipitated formed during mixing, preventing uniform dispersion. This was attributed to microparticle aggregation/precipitation, which was caused by an increased anion ratio within the PICs formed between the anionic lignin21 and the cationic PEI22 (Fig. 2C1, c1). In the presence of excess lignin, the limited amount of PEI restricts the formation of PICs. Consequently, the generated PICs grow into secondary complexes by adsorbing excess lignin derivative from the solution, leading to the formation of microparticles.23 No film formation was observed when the low-molecular-weight PEI (Mw = 600 or 1800) was employed at a lignin/PEI ratio of 17
:
83 for any of the lignin types. This was attributed to the insufficient interactions between the lignin derivative and the short PEI chains, as well as the high content of the liquid PEI. In the cases of SESC and soda systems, film formation became possible when using the higher-molecular-weight PEI (Mw = 10
000 or 70
000). For these lignin derivatives, even under excess PEI conditions, film formation was possible due to the weak hydrogen bonding of the lignin –OH groups without aggregation. On the other hand, when LS was used, film formation was not observed at a lignin/PEI ratio of 17
:
83, whereas it became possible at a 50
:
50 ratio. At lignin/PEI ratios of 17
:
83 and 50
:
50, the particle sizes in the dispersions were determined to be 4.0 and 4.3 nm (Fig. 2A2, a2), respectively. Although the particle size was maintained even after film formation using a lignin/PEI ratio of 17
:
83, a ratio of 50
:
50 produced an increased in particle size (several tens to hundreds of nanometers), indicating the formation of PICs (Fig. 2B2, b2). Since LS possesses strong anionic character due to its sulfonic acid (–SO3−) groups, it is expected to interact strongly with PEI via electrostatic interactions. However, the high hydrophilicity of LS stabilizes its hydrated state in the dispersion, thereby suppressing the growth of PICs. Using a lignin/PEI ratio of 50
:
50, the charge balance between the anionic and cationic groups became more favorable for PIC formation compared with that achieved using a 17
:
83 ratio. Moreover, water removal during the film formation process promoted the generation of PICs, which ultimately enabled successful film formation. The formation of PICs was further supported by FTIR analysis (Fig. S1). In all composite materials, peak broadening was observed in the range of 3300–3400 cm−1 was observed. This peak was attributed to the O–H stretching vibrations of the phenolic hydroxyl groups in lignin derivatives, and its broadening extended to the N–H stretching vibration of PEI at 3275 cm−1. Similarly, the characteristic peaks of PEI assigned to N–H scissoring bending vibrations (1584 and 1457 cm−1). It seems that C–N stretching vibrations of the aliphatic amines (1105 and 1044 cm−1) exhibited decreasing intensity or shifting peak. These spectral changes collectively suggest the presence of interactions between the phenolic hydroxyl groups in lignin derivatives and the amine groups of PEI. The zeta potentials of the lignin derivatives were −26.50, −33.90, and −33.29 mV for SESC, LS, and soda lignin, respectively, reflecting differences in their anionic character arising from the contents and acidities of their acidic functional groups (Table S1). The zeta potentials of lignin/PEI dispersions ranged from −2.69 to 1.54 mV, suggesting that charge neutralization occurred in the lignin/PEI systems. However, no clear correlation with lignin type or mixing ratio was observed. This is likely because changes in lignin species and composition induce the formation of insoluble fractions and aggregates, so that the measured zeta potentials do not simply reflect the surface charge of dispersed particles.
| Lignin | Lignin/PEI ratio | PEI Mw | |||
|---|---|---|---|---|---|
| 600 | 1800 | 10 000 |
70 000 |
||
| SESC | 0/100 | — | — | ✗ | — |
| 10/90 | — | — | ○ | — | |
| 17/83 | ✗ | ✗ | ○ | ○ | |
| 25/75 | — | — | ○ | — | |
| 33/67 | — | — | ○ | — | |
| 50/50 | ○ | ○ | ○ | ○ | |
| 67/33 | — | — | ○ | — | |
| 75/25 | — | — | ✗ | — | |
| LS | 17/83 | ✗ | ✗ | ✗ | ✗ |
| 50/50 | ○ | ○ | ○ | ○ | |
| Soda | 17/83 | ✗ | ✗ | ○ | ○ |
| 50/50 | ○ | ○ | ○ | ○ | |
000, the lowest helium gas permeability (1.7 × 10−16 mol·m m−2 s−1 Pa−1) was observed at a lignin/PEI ratio of 17
:
83.
| PEI Mw | Lignin/PEI ratio | He permeability (×10−16 mol m m−2 s−1 Pa−1) |
|---|---|---|
| 600 | 50/50 | 4.6 |
| 1800 | 50/50 | 5.5 |
10 000 |
10/90 | 2.5 |
| 17/83 | 1.7 | |
| 25/75 | 2.4 | |
| 33/67 | 3.4 | |
| 50/50 | 1.9 | |
| 67/33 | 5.1 | |
70 000 |
17/83 | 3.2 |
| 50/50 | 4.8 |
Notably, this was the lowest helium gas permeability obtained in the current study, suggesting that the charge balance at this ratio favors PIC formation to the greatest extent, leading to a high density and a continuous PIC structure that effectively suppressed gas permeation. This value is also lower than those of the uncoated PET sheet (5.4 × 10−16 mol·m m−2 s−1 Pa−1) and those of typical polymeric membranes,24 indicating that the SESC-PEI film provided a superior barrier performance. However, this value was higher than that reported for a composite membrane based on clay and modified lignin derivative,25 while also being higher than that of a clay/SESC combination.14 This difference in permeability was attributed to variations in the membrane structure. In previous studies, low permeability was achieved through the formation of an ordered layered structure by clay. In contrast, the membrane fabricated via PIC in this study does not exhibit a fully ordered layered structure, likely accounting for its relatively higher gas permeability. Based on these results, the lignin/PEI ratio was fixed at 50
:
50 and the Mw of PEI was varied. Consequently, the lowest gas permeability (1.9 × 10−16 mol·m m−2 s−1 Pa−1) was observed for a PEI Mw of 10
000. In the case of low-molecular-weight PEI (Mw = 600 or 1800), PIC formation was limited due to insufficient interactions with lignin, resulting in a reduced gas barrier performance.26 Conversely, when the Mw of PEI reached 70
000, numerous large aggregates were visible on the film surface (Fig. S2). This caused the film to lose its uniformity, preventing the formation of a continuous structure, and ultimately reducing the gas barrier performance.
000 and 70
000. Using PEI with a Mw of 10
000 in combination with a lignin/PEI ratio of 50
:
50, the resulting film exhibited a UVA transmittance of 15%, UVB transmittance of 0.10%, Tt of 83%, and haze value of 1.5%. These results indicate that the film demonstrated efficient UV protection while a maintaining high transparency. No significant change in the UV protection property was observed upon variation in the PEI Mw. In contrast, the films prepared using a low lignin content (10–33%) exhibited diminished UV shielding performances. In particular, the UVA transmittance reached 57% for a lignin/PEI ratio of 10
:
90, indicating a significant reduction in its protection properties due to the reduced lignin content. With regard to the LS-PEI films, Fig. 3b shows that these films exhibit a slightly yellowish appearance compared with the SESC-PEI films, although no significant differences were observed in their Tt and haze values. In the case of the LS-PEI films, the UVA transmittance was higher than those exhibited by the SESC-PEI films, and a high haze value of 6.1% was observed for a lignin/PEI ratio of 50
:
50 and a PEI Mw of 10
000. Moreover, the LS-PEI films exhibited higher UV transmittance characteristics compared with the corresponding SESC-PEI films. This can be attributed to the strong interactions between PEI and the highly polar sulfonic acid groups of LS, which promote lignin aggregation and generate a heterogeneous microstructure. This can be clearly observed in Fig. 2b2, where significantly larger particles and aggregates are present. These observations clearly contrast with the SESC-PEI films shown in Fig. 2b1. Moreover, the absorbance of SESC lignin alone was higher than that of LS lignin alone (Fig. S3), which likely contributed to the reduced UV protection properties observed for the LS-PEI films. Notably, the soda-PEI films demonstrated the lowest UV transmittance values, which seemingly indicates a superior performance. However, since soda is essentially dark in color (Fig. 3c) and possesses a low dispersibility, the soda-PEI films exhibit a dark brown color with a poor transparency. Consequently, they absorb a broad range of light (Fig. S4), not only in the UV region, but also in the visible range, ultimately leading to a decrease in the Tt. Furthermore, the durability of the lignin-PEI films was evaluated using accelerated weathering tests (Table S2). A comparison of color differences before and after the weathering test showed that the b* value increased for all samples, confirming yellowing of the films. As a result, a decrease in UVA transmittance was observed, particularly for the SESC and LS, leading to enhanced UVA shielding performance. The minimum bending radius determined by the mandrel test was less than 1 mm for SESC and soda, and 2 mm for LS, and these values remained unchanged before and after the light-resistance test.
| Lignin | PEI Mw | Lignin/PEI ratio | Film thickness (µm) | UVA transmittance (%) | UVB transmittance (%) | Tt (%) | Haze value (%) |
|---|---|---|---|---|---|---|---|
| SESC | 600 | 50/50 | 13 | 9.0 | 0.10 | 81 | 31 |
| 1800 | 50/50 | 10 | 9.0 | 0.10 | 80 | 25 | |
10 000 |
10/90 | 11 | 57 | 1.0 | 89 | 1.8 | |
| 17/83 | 6 | 49 | 0.60 | 89 | 4.0 | ||
| 25/75 | 18 | 23 | 0.13 | 87 | 3.6 | ||
| 33/67 | 9 | 31 | 0.23 | 79 | 3.3 | ||
| 50/50 | 12 | 15 | 0.10 | 83 | 1.5 | ||
| 67/33 | 8 | 10 | 0.10 | 80 | 7.7 | ||
70 000 |
17/83 | 8 | 8.0 | 0.32 | 85 | 2.0 | |
| 50/50 | 15 | 11 | 0.10 | 83 | 2.8 | ||
| LS | 600 | 50/50 | 6 | 20 | 0.18 | 85 | 9.8 |
| 1800 | 50/50 | 7 | 21 | 0.22 | 85 | 11 | |
10 000 |
50/50 | 9 | 29 | 0.03 | 82 | 6.1 | |
70 000 |
50/50 | 8 | 33 | 0.38 | 82 | 4.9 | |
| Soda | 600 | 50/50 | 10 | 0.2 | 0.17 | 51 | 5.6 |
| 1800 | 50/50 | 13 | 9.0 | 0.18 | 49 | 30 | |
10 000 |
50/50 | 10 | 0.10 | 0.17 | 31 | 1.5 | |
70 000 |
50/50 | 11 | 0.10 | 0 | 28 | 1.2 |
![]() | ||
Fig. 3 Representative photographic images of the lignin-PEI films prepared from (a) SESC, (b) LS, and (c) soda. A lignin/PEI ratio of 50 : 50 was used in each case. | ||
| This journal is © The Royal Society of Chemistry 2026 |