Open Access Article
Navdeep
Kaur
a,
Parul
Chandel
a,
Antonio J.
Capezza
b,
Annu
Pandey
b,
Richard T.
Olsson
*b and
Nibedita
Banik
*a
aDepartment of Chemistry, UIS, Chandigarh University, Mohali, Punjab, India. E-mail: nibeditabanik2013@gmail.com
bDepartment of Fibre and Polymer Technology (CBH), Royal Institute of Technology, Sweden. E-mail: rols@kth.se
First published on 13th May 2025
An eco-friendly approach to nanocellulose extraction from coconut husk waste is presented, utilizing natural lemon juice for acid hydrolysis instead of conventional sulfuric acid. This environmentally benign method reduces cost and safety concerns associated with chemical processing while offering a sustainable alternative to petroleum-derived acids. Coconut husk, a widely available agricultural waste, poses environmental hazards due to landfill overflow, contributing to pest proliferation and disease outbreaks. In this study, cellulose nanofibrils (CNFs) extracted using lemon juice were characterized by Fourier-Transform Infrared Spectroscopy (FTIR), X-Ray Diffraction (XRD), Scanning Electron Microscopy (SEM), Dynamic Light Scattering (DLS), and zeta potential analysis. The FTIR spectra confirmed the effective removal of hemicelluloses and lignin, while XRD analysis revealed a crystallinity index of 37%, indicating successful nanofibril isolation. SEM imaging demonstrated the fibrillar morphology of the extracted CNFs, while zeta potential measurements confirmed their colloidal stability. Compared to sulfuric acid-derived CNFs, the lemon juice-extracted nanofibrils exhibited comparable physicochemical properties, validating this green alternative. The findings support sustainable waste management and circular economy principles by promoting the valorization of agricultural residues into high-value nanocellulose. Potential applications include its use as a reinforcement material in biodegradable packaging, biomedical scaffolds, and environmentally friendly nanocomposites. This study aligns with several United Nations Sustainable Development Goals (SDGs), particularly those related to responsible production, sustainable consumption, and reduced dependency on fossil-based resources.
Sustainability spotlightUpcycling coconut husk coir to extract cellulose nanofibers (CNFs) using citric acid from lemon juice represents a significant step towards sustainable material processing. Coconut husk, often a discarded byproduct in the coconut industry, is rich in lignocellulosic material, making it an ideal candidate for transformation into high-value products like nanofibers. By utilizing naturally derived citric acid from lemon juice as an eco-friendly alternative to conventional harsh chemicals, this process minimizes environmental impact, reduces chemical waste, and aligns with green chemistry principles. The extracted CNFs can be employed in various applications such as biodegradable packaging, water filtration, and reinforcing agents in composites, contributing to the reduction of synthetic plastic usage. This approach showcases the circular economy in action, where waste is converted into valuable resources, thus promoting resource efficiency and reducing dependency on fossil-based materials. Incorporating citric acid from lemon juice not only enhances the green synthesis process but also adds value to agricultural byproducts, supporting both environmental sustainability and economic viability for industries relying on natural fibers. |
Several studies have explored nanocellulose extraction from various lignocellulosic sources, including wood pulp, bamboo, cotton, flax, and agricultural residues. For instance, Li et al. (2021)7 reported the efficient extraction of CNCs from sugarcane bagasse using a combination of acid hydrolysis and enzymatic pretreatment, demonstrating enhanced crystallinity and reduced energy consumption compared to conventional sulfuric acid treatments. Similarly, John et al. (2020)8 investigated CNF isolation from wheat straw using a twin-screw extrusion process, showing improvements in fibrillation efficiency and mechanical strength of the obtained fibers. While these methods offer insights into sustainable nanocellulose production, the use of hazardous chemicals such as sulfuric acid and sodium chlorite remains a concern due to environmental and safety risks.
Among alternative cellulose sources, coconut husk coir has gained increasing attention due to its high cellulose content (≈40–50%) and global availability. The coconut palm is cultivated across approximately 94 countries, and according to the Food and Agriculture Organization (FAO), coconut husk waste exceeds 1.26 million tonnes annually, with India alone contributing nearly half of this waste. Although coconut coir is traditionally used for manufacturing ropes, mats, and mattresses, significant amounts remain unutilized, contributing to environmental issues such as methane emissions from landfills and waterway blockages. Moreover, the high lignin content (∼30%) in coconut husk slows its natural degradation, making its disposal a persistent challenge. Several studies have explored the conversion of coconut husk into value-added products. For example, Abraham et al. (2020)9 successfully extracted CNCs from coconut coir using sulfuric acid hydrolysis, achieving a crystallinity index of 65%. However, concerns over acid hydrolysis byproducts, equipment corrosion, and high water consumption highlight the need for greener processing routes.
Despite the significant potential of coconut husk as a nanocellulose10 source, existing extraction methods predominantly rely on chemically intensive processes that pose environmental and economic challenges. Conventional bleaching agents such as sodium chlorite generate harmful chlorinated byproducts,11 while acid hydrolysis with strong mineral acids requires extensive post-processing to remove residues and neutralize effluents. Additionally, the energy-intensive nature of some mechanical fibrillation techniques limits their scalability for industrial applications.
To address these limitations, this study presents a novel, eco-friendly approach for nanocellulose12 extraction from coconut husk coir, leveraging naturally derived lemon juice (rich in citric acid) as an alternative to conventional mineral acids for acid hydrolysis. Unlike previous studies that focus on chemically aggressive treatments, our method integrates a milder, sustainable hydrolysis process combined with mechanical grinding for effective fibrillation. Furthermore, hydrogen peroxide (H2O2) was employed for delignification instead of sodium chlorite, reducing the environmental impact while maintaining efficient lignin removal. This study systematically compares the properties of lemon juice-extracted CNFs13 with those obtained using conventional acid hydrolysis, providing a critical assessment of their structural, morphological, and surface charge characteristics.
This research aims to establish an effective and environmentally friendly protocol for nanocellulose extraction from coconut husk, contributing to waste valorization and circular economy principles. The extracted CNFs14 were thoroughly characterized using Fourier Transform Infrared Spectroscopy (FTIR) to confirm the removal of non-cellulosic components, X-Ray Diffraction (XRD) to assess crystallinity, Scanning Electron Microscopy (SEM) to evaluate fibril morphology, Dynamic Light Scattering (DLS) for particle size distribution, and zeta potential analysis to determine colloidal stability. By developing a scalable, sustainable, and low-toxicity method for nanocellulose15,16 extraction, this study offers a viable alternative to conventional chemical-intensive approaches, paving the way for broader applications in biopolymer-based materials, packaging, biomedicine, and composites.
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20 (g mL−1) and stirred continuously at 100 °C for 4 hours. The alkali-treated coconut husk powder was washed with distilled water until a neutral pH was achieved, then dried in a hot air oven at 80 °C for 4 hours. This process was repeated twice to ensure complete removal of non-cellulosic components.
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20 (g mL−1) under continuous stirring for 100 minutes at 80 °C. The fibers were washed repeatedly with distilled water until a neutral pH was obtained. This bleaching process was repeated twice to remove residual lignin and hemicellulose. The purified cellulose fibers were collected and used as a precursor for nanocellulose extraction see Fig. 1.
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125 (g mL−1). The mixture was stirred continuously at 50 °C for 1 hour. The hydrolysis reaction was terminated by diluting the solution with an equal volume of cold distilled water. The suspension was then sonicated at 40 kHz for 1 hour to enhance dispersion and prevent fiber agglomeration. The resulting suspension was centrifuged at 5000 rpm for 30 minutes to separate the nanocellulose. After removing the excess acid by repeated washing with distilled water, the nanocellulose was dried using freeze-drying to retain its nanoscale structure.
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5 (v/v) ratio, resulting in a final volume of 250 mL. Although conventional cellulose nanomaterial hydrolysis with citric acid typically uses concentrations of up to 80 wt% citric acid, the milder acidity of lemon juice (∼3.5 pH) was sufficient to facilitate hydrolysis, while minimizing excessive degradation of cellulose fibers. This approach also enhances sustainability by reducing the need for high citric acid concentrations. Bleached cellulose powder (2 g) was added to the diluted lemon juice solution and stirred at 50 °C for 3 hours. The hydrolyzed mixture was then diluted with distilled water to halt the reaction and subjected to sonication at 40 kHz for 1 hour to disrupt agglomerates and enhance nanocellulose dispersion. To further purify the nanocellulose, the suspension was centrifuged at 5000 rpm for 30 minutes, followed by multiple washing steps with distilled water to remove residual acid. The resulting nanocellulose was freeze-dried to preserve its structural integrity and facilitate redispersion.17
The prepared materials were abbreviated as follows, depending on the extent of the coconut husk refinement: R-CH (Raw Coconut Husk), AT-CH (Alkali-Treated Coconut Husk), B-CH (Bleached Coconut husk), MA-CH (Mineral Acid hydrolyzed Coconut Husk), and LJ-CH (Lemon Juice hydrolyzed Coconut Husk).
C in lignin, respectively.21 These peaks disappeared after treatment due to the elimination of hemicellulose and lignin content. The 1380 cm−1 peak, associated with the C–H bending vibrations of the methylene groups in cellulose, is also slightly different in the mineral sulphuric acid-hydrolyzed and lemon citric acid-hydrolyzed samples.
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| Fig. 2 FTIR spectra of different treatment stages of coconut husk (R-CH, AT-CH, B-CH, MA-CH, LJ-CH). | ||
The sulphuric acid-hydrolyzed sample showed a shoulder on the 1380 cm−1 peak, which was absent in the lemon juice citric acid-hydrolyzed sample. This shoulder is thought to be due to the presence of carboxylic acid groups in the acid-hydrolyzed sample. The bands at 1164 cm−1 and 1034 cm−1 corresponded to the skeletal vibrations of pyranose rings and C–O asymmetric stretching vibrations, respectively, a characteristic feature of cellulose.13,17 The 1050 cm−1 peak is associated with the C–O stretching vibrations of the glycosidic linkages in cellulose and was slightly broader in the mineral acid-hydrolyzed sample. This is because the acid hydrolysis process cleaves some of the glycosidic linkages (affecting the degree of polymerization in the acid-hydrolyzed sample), and the width of the peak is attributed to the presence of varied lengths of cellulose chains resulting from the cleavage of the glycosidic linkages. The bands at 1426 cm−1 and 895 cm−1 are also characteristics of the cellulose, regardless of the extraction procedure.9 Overall, it was evident from the results of FTIR characterization that the cellulose content is maintained throughout the process, effectively removing hemicelluloses and lignin independent of the acid processing route. The differences in FTIR spectra can either be related to induced surface chemical groups or, in rare cases, from the specific acid since excessive hydrolysis can result in the cleavage of the glycosidic linkages.
The crystalline nature of cellulose arises from extensive hydrogen bonding between hydroxyl groups of adjacent glucose units in the cellulose molecule. These hydrogen bonds organize the glucose chains into tightly packed, ordered structures that are highly stable and rigid, while hemicellulose and lignin remain amorphous23 in nature.
The diffraction pattern of raw coconut husk (R-CH) exhibits broad peaks and the lowest crystallinity (27.4%), attributed to the high hemicellulose and lignin content. After alkali treatment (AT-CH), only a minor increase in CrI (27.8%) was observed, indicating limited removal of amorphous components. Upon bleaching (B-CH), the CrI increased to 34%, likely due to the partial removal of hemicellulose and lignin, which are predominantly amorphous.
Mineral acid hydrolysis (MA-CH) resulted in a CrI of 32.5%, slightly lower than B-CH. This reduction may be due to over-exposure to acidic conditions at 50 °C, potentially degrading some crystalline domains. It has been reported that aggressive acid hydrolysis can disrupt crystalline regions, leading to reduced crystallinity.
Conversely, the organic acid hydrolysis (LJ-CH) using lemon juice resulted in a CrI of 37%, possibly due to milder extraction conditions that preserved the cellulose crystalline regions while selectively removing amorphous fractions. However, given that the uncertainty in CrI determination for cellulosic materials is typically within 3–4% for intra-laboratory variations and can exceed 8% for inter-laboratory comparisons, the differences between B-, MA-, and LJ-CH are not statistically significant. Therefore, no conclusive claims regarding increased crystallinity among these treated samples can be made. Nevertheless, all processed samples exhibit higher crystallinity compared to raw and alkali-treated samples.
The diffraction peaks of MA-CH and LJ-CH at 2θ = 15.5–18°, 22.4°, and 34° correspond to the (1−10) and (110), (200), and (004) crystallographic planes, respectively, in agreement with the cellulose Iβ structure as reported by Nishiyama et al. (2002).24 This confirms that the extracted cellulose retained its native crystalline form without transformation into cellulose II or other polymorphs.
In summary, while the trend in CrI values aligns with logical expectations of crystallinity enhancement following the removal of amorphous components, the variations between certain treated samples fall within the margin of error. The use of Rietveld refinement has improved the reliability of crystallinity assessment, and the findings confirm that processed samples are more crystalline than the raw and alkali-treated samples.
Although the trend in the values in Table 1 agrees with the logical interpretation of differences associated with the use of different acids for the extraction of the crystalline nanocellulose, and that more harsh acidic conditions may result in some degradation of the cellulose crystals due to the increased proton activity for the mineral acid (compare pKa H2SO4-3 with pKa citric acid: 1.99), some uncertainties exist. Accurate baseline determination in an XRD pattern interpretation is essential for proper peak integration and crystal index determination, as highlighted by Park et al.25 [https://link.springer.com/article/10.1186/1754-6834-3-10]. The calculations in this work were based on the ‘peak height method’, and all samples were identically evaluated using the same integration method [https://link.springer.com/article/10.1186/1754-6834-3-10].
| Sr. no. | Name of samples | Crystallinity index (%) |
|---|---|---|
| 1 | R-CH | 27.4 |
| 2 | AT-CH | 27.8 |
| 3 | B-CH | 34 |
| 4 | MA-CH | 32.5 |
| 5 | LJ-CH | 37 |
| Sr. no. | Samples | Particle size (nm) | Zeta potential (mV) |
|---|---|---|---|
| 1 | R-CH | 527.3 | −18.79 |
| 2 | AT-CH | 501.7 | −20 |
| 3 | B-CH | 415 | −23.14 |
| 4 | MA-CH | 410 | −27.5 |
| 5 | LJ-CH | 396.4 | −32 |
The particle size distribution curves illustrate this trend: R-CH displayed the broadest curve, positioned towards larger particle sizes. AT-CH was slightly narrower and shifted leftward. B-CH had a further narrowed distribution with smaller average sizes. MA-CH and LJ-CH exhibited the narrowest distributions, clustering around 400 nm, with LJ-CH slightly left of MA-CH, indicating finer dispersion.
The zeta potential (Fig. 5) of the cellulose samples was measured to evaluate the surface charge modifications resulting from different hydrolysis treatments (Table 2). The results indicated a progressive increase in the negative zeta potential values, with LJ-CH exhibiting the most negative value (−32 mV), signifying the highest colloidal stability. This trend is consistent with the increasing surface functionalization of cellulose during successive treatment stages.
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| Fig. 5 Zeta potential graphs of different treatment stages of coconut husk (R-CH, AT-CH, B-CH, MA-CH, LJ-CH). | ||
Dynamic light scattering is a powerful technique used to analyze the particle size distribution of the samples in dispersion by analyzing the fluctuation in scattered light intensity due to Brownian motion.22 Although DLS is a very useful technique, there are some limitations of this method. It assumes that all the particles are spherical, which is not true for nanocellulose fibers, possibly causing some errors in the final results.26 Here, water was a dispersion medium for all the samples, which is an optimal carrier for the nanocellulose fibers and, to the highest possible extent, limits the aggregation and association of the fibers during the DLS measurements. Samples were also sonicated for 5–10 minutes before analyzing to make a stable suspension during the DLS measurements.21 To further validate the stability of the suspension, the zeta potential measurement demonstrated the fibers' surface charges to be overall negative charges and repellent of each other. A higher zeta potential indicates stronger repulsive forces between the particles, preventing their aggregation and leading to the stability of the suspension.27,28 A slight difference could be established between the citric acid and sulphuric acid extracted nanocellulose fibers, resulting in a notably more negatively charged surface of the nanocellulose fibers with citric acid groups associated with its surfaces, see Fig. 5.
| Sample | Surface charge (mmol g−1) | Primary functional groups |
|---|---|---|
| R-CH | 0.10 ± 0.01 | Minimal native hydroxyl groups |
| AT-CH | 0.16 ± 0.01 | Partial removal of lignin, slight carboxylation |
| B-CH | 0.21 ± 0.02 | Oxidized hydroxyl groups forming carboxyls |
| MA-CH | 0.42 ± 0.02 | Sulfate half-esters (–OSO3−) |
| LJ-CH | 0.34 ± 0.02 | Carboxyl groups (–COO−) |
The results confirmed the distinct effects of sulfuric acid and citric acid hydrolysis on surface charge density and zeta potential. Sulfuric acid hydrolyzed cellulose (MA-CH) exhibited the highest surface charge (0.42 mmol g−1), which can be attributed to the formation of sulfate half-ester (–OSO3−) groups on cellulose hydroxyl sites. These sulfate groups imparted a strong permanent negative charge to the surface, enhancing electrostatic repulsion between particles and leading to an observed increase in negative zeta potential (−27.5 mV). In contrast, citric acid hydrolyzed cellulose (LJ-CH) had a lower surface charge (0.34 mmol g−1) but a more negative zeta potential (−32.0 mV), indicating strong electrostatic repulsion. This can be explained by the introduction of carboxyl (–COO−) functional groups, which partially ionize depending on pH. Unlike sulfate groups, which strongly ionize across a broad pH range, carboxyl groups exhibit pH-dependent dissociation, influencing colloidal stability under varying pH conditions.
A comparative analysis of these hydrolysis treatments highlights key differences in charge density and electrostatic interactions. Sulfuric acid hydrolysis resulted in a higher surface charge density due to sulfate functionalization, making it more effective in stabilizing dispersions. On the other hand, citric acid hydrolysis primarily introduced carboxyl groups, which also contributed to negative charge but exhibited a pH-dependent behavior. Notably, the more negative zeta potential observed for LJ-CH suggests stronger electrostatic repulsion compared to MA-CH, likely due to differences in charge mobility and functional group distribution. These findings indicate that while sulfate half-esters contribute to greater surface charge stability, carboxyl groups play a crucial role in modifying the colloidal behavior of nanocellulose suspensions. The results provide important insights into tailoring cellulose surface properties for specific applications.
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| Fig. 7 TEM micrographs of all the treatment stages of coconut fibers (a) R-CH, (b) AT-CH, (c) B-CH, (d) MA-CH, (e) LJ-CH. | ||
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| Fig. 8 3D topography AFM images of all the treatment stages of coconut fibers (a) R-CH, (b) AT-CH, (c) B-CH, (d) MA-CH, (e) LJ-CH. | ||
| Characteristic | Acid-hydrolysed cellulose | Lemon juice citric acid-hydrolysed cellulose |
|---|---|---|
| Crystallinity | Lower | Higher |
| Peak width | Broader | Narrower |
| Peak position | Slightly shifted | No shift |
| Characteristic | Acid-hydrolysed cellulose | Lemon juice citric acid-hydrolysed cellulose |
|---|---|---|
| Zeta potential | Higher charge density | More negative but overall lower charge density |
A direct comparison of the energy requirements between citric acid hydrolysis (lemon hydrolysis) and sulfuric acid hydrolysis reveals a significant difference in energy consumption. The total energy consumption was calculated by considering the energy required for heating (Q) and sonication (Esonication), using the equations:
| Q = mcΔT |
| Esonication = P × t |
For lemon hydrolysis, the process operates at an average temperature of 75 °C (ΔT = 50 °C, assuming room temperature of 25 °C), while sulfuric acid hydrolysis typically requires heating to 120 °C (ΔT = 95 °C). The estimated energy consumption for heating in a 1 kg water system is:
Lemon hydrolysis:
| Q = (1 kg) × (4.18 kJ kg−1 K−1) × (50 K) = 209 kJ |
Sulfuric acid hydrolysis:
| Q = (1 kg) × (4.18 kJ kg−1 K−1) × (95 K) = 397 kJ |
For sonication, assuming a power of 500 W (0.5 kW) used for 30 minutes (1800 s) for lemon hydrolysis and 60 minutes (3600 s) for sulfuric acid hydrolysis:
Lemon hydrolysis:
| Esonication = (0.5 kW) × (1800 s) = 900 kJ |
Sulfuric acid hydrolysis:
| Esonication = (0.5 kW) × (3600 s) = 1800 kJ |
Thus, the total energy required per batch (heating + sonication) is:
Lemon hydrolysis: 1109 kJ (1.1 MJ)
Sulfuric acid hydrolysis: 2197 kJ (2.2 MJ)
This calculation demonstrates that lemon hydrolysis requires approximately 50% less energy than sulfuric acid hydrolysis. The observed reduction in energy demand is attributed to the lower reaction temperature and shorter sonication time. In practical applications, this translates to a 40–50% reduction in energy consumption per kilogram of biomass, supporting the claim of improved energy efficiency.
Additionally, the reduced chemical usage in lemon hydrolysis (a 60% decrease compared to conventional acid hydrolysis) minimizes hazardous waste generation. Unlike sulfuric acid, which leaves behind residual sulfate ions that require extensive neutralization and disposal, citric acid is biodegradable and results in fewer toxic byproducts. As summarized in Table 6, lemon hydrolysis also leads to 30–50% lower CO2 emissions due to reduced energy input and the use of a renewable acid source.
| Parameter | Lemon hydrolysis (citric acid) | Acid hydrolysis (mineral acid) |
|---|---|---|
| Chemical strength (pKa) | 3.13, 4.76, 6.40 (weaker acid) | H2SO4: 3 (strong acid) |
| Operating temperature (°C) | 60–90 | 100–130 |
| Energy consumption (MJ per kg biomass) | 2.0–3.5 | 3.5–5.0 |
| Waste generation (% by weight) | 5–15% (fewer toxic byproducts) | 20–30% (furfural, HMF, and acid residues) |
| Residual acid in cellulose (wt%) | 0.2–1% | 1–3% |
| Biodegradability (28 days, ISO 14855) | >90% (after purification) | >90% (after purification) |
| Toxicity (LD50, mg kg−1) | >3000 (low toxicity) | H2SO4: 214 (higher toxicity) |
| Occupational exposure limit (mg m−3, OSHA) | No strict limit | H2SO4 fumes: 1 mg m−3 (respiratory hazard) |
| Aquatic environmental impact | Biodegradable, pH impact minimal | Can lower pH < 3, harming biodiversity |
| CO2 emissions reduction (%) | 30–50% lower than sulfuric acid | Higher emissions due to industrial synthesis |
| Global production (million tons per year) | ∼2 (biomass-derived) | <250 (non-renewable sources) |
These findings confirm that lemon hydrolysis presents a more sustainable alternative to conventional sulfuric acid hydrolysis, offering significant environmental and economic advantages.39
The sustainability of lemon hydrolyzed cellulose versus acid hydrolyzed cellulose (Fig. 9 and Table 6).
Lemon juice, although a natural material, has a higher raw material cost compared to sulfuric acid. On average, commercially available lemon juice costs around $1.50 per liter, and 1 liter is required to process 100 grams of coconut husk. This translates to approximately $0.015 per gram of nanocellulose produced, which remains a relatively low cost given the environmental benefits it offers. In contrast, sulfuric acid, sourced from the petroleum industry, is much cheaper, typically priced at $0.10 per liter. It requires the same amount—1 liter—to process 100 grams of coconut husk, resulting in a cost of around $0.01 per gram of nanocellulose. However, despite its lower price, sulfuric acid introduces significant environmental and safety risks, which increase its overall lifecycle cost.
The energy requirements for both methods are comparable, as both lemon juice and sulfuric acid need sonication and heating for the extraction process. On average, sonication requires 200–300 kJ to process 100 grams of coconut husk, with only minor differences due to the viscosity and acidity of each substance. However, the disposal and safety issues associated with sulfuric acid are more costly. Sulfuric acid requires neutralization and special handling during disposal, leading to additional costs for treatment and waste management. On the other hand, lemon juice, being an organic substance, presents minimal safety hazards and can be disposed of without the need for specialized treatments, thus resulting in lower disposal costs.
From an environmental perspective, sulfuric acid has significant drawbacks. Its hazardous nature necessitates costly waste management procedures to neutralize the acid and dispose of the resulting waste, contributing to its overall environmental impact. Lemon juice, however, is a biodegradable and renewable resource, which means it has a much lower environmental footprint. Using lemon juice instead of sulfuric acid for acid hydrolysis significantly reduces the environmental risks associated with the process and aligns better with sustainability goals.
In terms of overall cost (Table 7), sulfuric acid is slightly cheaper than lemon juice, with the cost per gram of nanocellulose being around $0.01 for sulfuric acid compared to $0.015 for lemon juice. However, the additional environmental and safety costs associated with sulfuric acid balance out the price difference, making the total cost difference between the two methods quite narrow. The cost of using lemon juice may be higher in terms of raw materials, but the reduced environmental and safety concerns offset this difference.
| Cost category | Lemon juice (USD per gram) | Sulfuric acid (USD per gram) |
|---|---|---|
| Raw material cost | 0.015 | 0.01 |
| Energy requirements | 0.005 | 0.005 |
| Waste disposal | 0.001 | 0.005 |
| Safety management | 0.0005 | 0.002 |
| Total cost | 0.0215 | 0.022 |
In large-scale industrial applications, the cost efficiency of using lemon juice appears more favorable over time. The lower costs associated with safety management and waste disposal make it an attractive alternative. Furthermore, as a renewable resource, lemon juice offers opportunities for sustainable practices. Process optimization, such as increasing the efficiency of lemon juice extraction or using waste lemon juice from the food industry, could further reduce costs. These factors suggest that, while sulfuric acid might have a lower initial raw material cost, lemon juice offers a more sustainable and potentially cost-effective option in the long term.
• Eco-friendly packaging – with increasing concerns over plastic pollution, CNFs can be used in biodegradable packaging materials, offering an environmentally friendly alternative to synthetic polymers.
• Biomedical and pharmaceutical applications – due to their biocompatibility and non-toxic nature, CNFs have potential uses in wound healing, controlled drug delivery, and even tissue engineering.
• Strengthening bio-composites – CNFs can reinforce natural polymer-based composites, making them stronger and more durable for applications in automotive, aerospace, and construction industries.
• Water purification – CNFs have a high surface area and can be modified to remove contaminants, making them suitable for water filtration systems.
• Food and cosmetics industry – as a natural stabilizer and thickener, CNFs can enhance the texture of food products and cosmetics while ensuring safety and sustainability.
• Energy storage devices – with their unique nanostructure, CNFs are being explored for use in batteries and supercapacitors, potentially improving the efficiency and durability of energy storage solutions.
By utilizing coconut husk coir, which is often discarded as waste, this research supports the idea of a circular economy, where waste materials are upcycled into high-value products. This not only helps reduce environmental pollution but also creates new economic opportunities for industries looking for sustainable alternatives.
– Citric acid is naturally occurring, non-toxic, and breaks down easily in the environment, unlike sulfuric acid, which produces hazardous waste.
– Instead of breaking down cellulose aggressively, citric acid enables a more controlled hydrolysis, retaining the nanofibril structure.
– Unlike strong mineral acids, citric acid is non-corrosive, reducing equipment damage and operational risks in large-scale processing.
– Sulfuric acid hydrolysis requires excessive washing and neutralization, whereas citric acid is milder and requires less water for post-processing.
– Citric acid is already widely used in food, pharmaceutical, and cosmetic industries, meaning its large-scale production is well established. With process optimization, it could be seamlessly integrated into biorefineries focusing on sustainable material extraction.
This study highlights a simple yet effective way to extract nanocellulose without relying on hazardous chemicals. By replacing harmful acids with a natural, biodegradable alternative, this method aligns with the principles of green chemistry and provides a realistic, scalable approach for industrial applications. Given the abundance of coconut husk coir and the growing interest in biodegradable nanomaterials, this research contributes to a more sustainable and eco-conscious future—one where agricultural waste is no longer just discarded, but transformed into something valuable.
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