Abstract
The effects of acidified chlorite (NaClO2) and totally chlorine free (TCF) bleaching were evaluated relative to the properties of microcrystalline cellulose (MCC) fabricated from oil palm empty fruit bunch fibres (OPEFB). The MCC properties were analyzed using X-ray diffraction (XRD), scanning electron microscopy (SEM), and thermogravimetric analysis (TGA) methods, and they were compared with commercial MCC. The results revealed that all MCC belongs to cellulose type 1 and OPEFB-NaClO2-MCC showed a higher crystallinity index than OPEFB-TCF-MCC. The TGA indicated that all MCC samples showed a higher decomposition temperature compared to pure cellulose. However, OPEFB-NaClO2-MCC showed better thermal stability than OPEFB-TCF-MCC. It was clear from SEM images that the different MCC particles had rough surfaces and micro-sized particles. Overall, results confirmed that the obtained MCC samples displayed comparable properties with those of commercial MCC. The MCC produced from OPEFB using NaClO2 is a promising material to prepare high value-added products compared to MCC produced using TCF delignification treatment.
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Delignification’s Effect on Microcrystalline Cellulose Obtained from Oil Palm Empty Fruit Bunch Fibres
Najieha Norazli,a Nurul Fazita Mohammad Rawi,a,b,* Owolabi Folahan Abdulwahab Taiwo,c Mohamad Haafiz Mohamad Kassim,a,b,* and Mohammad Jawaid d
The effects of acidified chlorite (NaClO2) and totally chlorine free (TCF) bleaching were evaluated relative to the properties of microcrystalline cellulose (MCC) fabricated from oil palm empty fruit bunch fibres (OPEFB). The MCC properties were analyzed using X-ray diffraction (XRD), scanning electron microscopy (SEM), and thermogravimetric analysis (TGA) methods, and they were compared with commercial MCC. The results revealed that all MCC belongs to cellulose type 1 and OPEFB-NaClO2-MCC showed a higher crystallinity index than OPEFB-TCF-MCC. The TGA indicated that all MCC samples showed a higher decomposition temperature compared to pure cellulose. However, OPEFB-NaClO2-MCC showed better thermal stability than OPEFB-TCF-MCC. It was clear from SEM images that the different MCC particles had rough surfaces and micro-sized particles. Overall, results confirmed that the obtained MCC samples displayed comparable properties with those of commercial MCC. The MCC produced from OPEFB using NaClO2 is a promising material to prepare high value-added products compared to MCC produced using TCF delignification treatment.
DOI: 10.15376/biores.18.1.1901-1915
Keywords: Oil palm empty fruit bunch; Microcrystalline cellulose; Acidified chlorite; Totally chlorine free; Structural properties; Thermal properties; Morphological properties
Contact information: a: Bioresource Technology Division, School of Industrial Technology, Universiti Sains Malaysia, Penang, Malaysia; b: Green Biopolymer, Coatings and Packaging Cluster, School of Industrial Technology, 11800 Minden Universiti Sains Malaysia; c: Pulp and Paper Division, Federal Institute of Industrial Research Oshodi, Lagos, Nigeria; d: Laboratory of Biocomposite Technology, INTROP, University Putra Malaysia, 43400 Serdang, Selangor, Malaysia;
* Corresponding authors: fazita@usm.my; mhaafiz@usm.my
GRAPHICAL ABSTRACT
INTRODUCTION
The demand for sustainable and renewable materials has increased intensely in the last few decades and is the topic for the “2030 Agenda for Sustainable Development” organized by the United Nations General Assembly (2015). In line with the United Nations mantra “Transforming our world”, the focus is to protect the planet from exploitation of its natural resources (Haldar and Purkait 2020). As awareness of the impact of climate change grows, researchers have reported that one of the most abundant and sustainable biopolymers on earth is cellulose. This versatile and renewable material can be obtained from various sources such as agricultural waste or biomass (Galiwango et al. 2019; Li et al. 2019; Mishra et al. 2019).
Natural cellulosic fibers derived from lignocellulosic biomass have several advantages, including their abundance, renewable nature, low cost, high specific strength, and reactive surfaces, coupled with their biocompatibility and biodegradability, which has been a great asset in applying micro and nano-sized particles from cellulose fibre for enhancement of strength properties in composites. When compared to synthetic fibre composites, natural fibre composites use less energy to manufacture. Globally accessible natural fibres have been employed and studied as reinforcement in polymer composites such as bagasse (Alizadeh Asl et al. 2017; Abd El-Baky et al. 2019; Suresh et al. 2020), hemp (Dayo et al. 2017), and date palm (Awad et al. 2020; Alhijazi et al. 2020). These fibres offer similar qualities and can be used to replace synthetic fibre composites (Kannan and Thangaraju 2021). Since the production and report of microcrystalline cellulose (MCC) by Smith and Battista (1955), it has since been widely used in various industries because of its numerous advantages (Taiwo et al. 2016; Tarchoun et al. 2019). Any material that contains a high concentration of cellulose can be used to make MCC. Various lignocellulosic biomass sources for MCC are reported in the literature such as forest residue (rose stem and date seeds), agricultural residue (tea wastes), and aquatic residue (brown algae) (Haldar and Purkait 2020).
Malaysia’s and the world’s palm oil industries have continued to expand to sustainably meet the growing global demand for oils and fats as stated by the Malaysia palm oil council (2019). With a palm tree yielding only 10% oil, this growth results in a variety of wastes from oil palm products because of its vast planting lands and large number of oil palm mills (Shamsuddin et al. 2021). Oil palm activities generate a variety of wastes, including oil palm empty fruit bunches (OPEFB), oil palm fronds (OPF), and oil palm trunks (OPT) (Ramlee et al. 2021). This results in roughly 90% of enormous amounts of waste biomass from oil palm activities, while about 10% of oil extraction comes from two primary sources: plantations and mills. While oil palm plantations generate a large amount of oil palm trunks and fronds, other biomasses, such as mesocarp fibre, kernel shell, and empty fruit bunches are generated during the milling of fresh fruit bunches (Anuar et al. 2019). Oil palm empty fruit bunch generates up to 22 to 23 million tons of residue yearly in Malaysia and is the cheapest natural fibre with as good characteristics as a non-wood fibre. It has a lot of promising characteristics as a major raw material to replace woody plants, which are expensive in many sectors (Padzil et al. 2020). These organic and natural by-products have the potential to be employed as a value-added product in the industrial sector.
As with other plant species, cellulose, hemicellulose, and lignin are the major constituents of biomass’ natural fibres, which also contain trace amounts of proteins and extractives. Cellulose is well-embedded in the intricate network of hemicellulose and lignin in each of the fibre materials. Apart from the treatment process chosen, the quality and quantity of cellulose used in the process dictate the formation of derivatives. Thus, it is critical to emphasize the structure and composition of cellulose within the lignocellulosic biomass fibres.
The properties of the modified cellulose properties are not only dependent on the type of lignocellulosic source but also on the pretreatments used to extract its native cellulose. These pretreatments are performed to separate pure and crystalline cellulose. They are also used to reduce the degree of polymerization and increase the reactivity of cellulose (Kargarzadeh et al. 2017). Due to the various factors that can affect the success of the pretreatment, it is important that the techniques are optimized to avoid generating toxic, hazardous wastes as well as high overall process costs (Phanthong et al. 2018). The delignification process is widely used to remove hemicellulose and lignin from raw biomass (Jiang and Hsieh 2015; Ilyas et al. 2018; Liao et al. 2020); however, various other methods have been used as well to remove hemicellulose and lignin. Asl, Mousavi, and Labbafi (2017) extracted alpha cellulose using a digester at 370 °C, then bleached the fibres with chlorine gas and sodium hypochlorite. Asif et al. (2022) in other hands, delignified pedicles fiber with 5% wt NaOH solution and bleached the resulting fibres with sodium chlorite solution to obtain cellulose. Shi and Liu (2021) extracted cellulose using totally chlorine free bleaching method. The conventional method involves the use of chlorine-based protocol, but recent approaches are by green delignification with totally chlorine free methods (Cheng et al. 2018; Robles et al. 2018). To reduce the production of chlorinated organic compounds during pulp manufacturing, totally chlorine-free (TCF) bleaching is being used more frequently as a result of global trends and environmental pressures for cleaner bleaching processes (Li et al. 2017).
The dependence of the isolated pure cellulose and MCC from OPEFB on the raw material, the process, and also the pretreatments has been widely reported. Various previous studies have been conducted to generate MCC from OPEFB. Despite this, there have been no controlled studies comparing differences in the effects of pretreatment on the final characteristics of the derived MCC from OPEFB. This paper aims to improve the efficiency of the process by developing effective methods for the isolation and production of pure MCC from OPEFB and to compare two different pretreatment processes before MCC isolation. To achieve this, two delignification processes were employed in this study, the acidified chlorite (NaClO2) method and the totally chlorine free (TCF) delignification method. The prepared MCC samples were characterized with analytical techniques of Fourier transform infrared (FT-IR), X-ray diffraction (XRD), scanning electron microscopy (SEM), and thermogravimetric analysis (TGA) to investigate the impact of the different delignification process used on the physiochemical and thermal properties of isolated MCC. The commercial MCC was used as reference to compare the properties of extracted MCC.
EXPERIMENTAL
Materials
The OPEFB strands were procured from United Oil Palm Sdn Bhd, Nibong Tebal, Penang, Malaysia. Commercial microcrystalline cellulose (Sigma-Aldrich (31069-7)) used as a control. Other materials used include distilled water, sodium hydroxide (NaOH), sodium chlorite (NaClO2), acetic acid 98%, hydrochloric acid (HCl) 37%, magnesium sulphate heptahydrate (MgSO4.H2O), hydrogen peroxide (H2O2), sulphuric acid (H₂SO₄), ammonia hydroxide (NH₄OH), and silicon oil; all chemicals used were purchased from Sigma Aldrich, Merck (United States).
Preparation of OPEFB pulp with soda pulping
The OPEFB strands were pre-hydrolyzed via immersion in water for 1 h at 170 ℃ in a digester. The preparation of OPEFB pulp was completed by the pulping milieu as reported by Leh et al. (2008). After that, OPEFB was washed to eliminate all contaminations. A total of 300 g oven-dried (OD) OPEFB was pulped with 26% NaOH solution at a solid-to-liquid ratio of 1:7 and heated to 170 ℃ for 100 min. The obtained OPEFB pulp was then washed with water through a hydro pulper and then screened using pulp screening equipment with diameter of 15 mm. The fine OPEFB pulp was labeled as dissolving pulp and kept in the refrigerator for further study.
Preparation of totally chlorine-free cellulose
Three sequences that were used to produce totally chlorine-free (TCF) pulp include oxygen, ozone, and peroxide bleaching according to the procedure reported by Leh et al. (2008). Oxygen bleaching was completed using an autoclave equipped with a gas inlet, stirrer, and computer-controlled thermocouple manufactured by Parr Instrument Company, Moline, IL, USA. A total of 100 g OD of dissolved pulp was mixed with 1.0% magnesium sulfate (MgSO4.7H2O) solution, 2.0% sodium hydroxide (NaOH) solution, and an appropriate amount of water to achieve 10% concentration. The reaction temperature and oxygen pressure were maintained at 95 ℃ and 80 psi, respectively. The autoclave was maintained for 30 min with occasional stirring.
A modified revolving vessel designed for evaporation attached to an ozone generator and oxygen cylinder was used for ozone bleaching. The pulp was treated with acidic water at a pH of 1.5 (adjusted by addition of H2SO4) for 2 h. Then, the pulp was squeezed to a consistency of 27% and placed in a round bottom flask reaction vessel. The regenerated ozone gas was passed through the vessel and the vessel was rotated to make sure homogeneous mixing between pulp and ozone gas for 2.5 min. The reaction was continued for another 20 min. Then the obtained pulp was washed with distilled water.
The next stage was hydrogen peroxide bleaching, for which 3.0% hydrogen peroxide solution, 2.0% NaOH solution, and 0.5% MgSO4·7H2O solution based on pulp weight were mixed with an appropriate amount of water to achieve 15% concentration. The pulp slurry was transferred to a plastic bag and the reaction was completed at 65 ℃ for 1 h in a water bath and squeezed every 10 min to get proper extraction. The pulp was then treated with purified water. To obtain pure cellulose from delignified pulp, the pulp was then treated with 17.5% NaOH at 80 ℃ for 1 h following the Pachuau et al. (2014) method. The sample was filtered, repeatedly washed with distilled water to neutralize it, and oven-dried overnight at 40 ℃ and labeled as OPEFB-TCF-C.
Preparation of acidified sodium chlorite cellulose pulp
The dissolving pulp was added with acidified sodium chlorite according to the report by Foo et al. (2020). Then, 20 g of dissolving pulp was added with NaClO2 and 10% of acetic acid until the pH reached 4. The dissolving pulp was boiled in sodium chlorite solution for 2 h at 80 ℃. The resultant delignified dissolving pulp was subsequently washed with distilled water. To obtain pure cellulose from delignified pulp, the pulp was treated with 17.5% NaOH at 80 ℃ for 1 h following Pachuau et al.’s (2014) method. The sample was filtered, repeatedly washed with distilled water to neutralize it and oven-dried overnight at 40 ℃ and denoted as OPEFB-NaClO2-C.
Production of OPEFB MCC
The acid hydrolysis treatment was conducted to obtain MCC according to the optimized method describe by Hassan et al. (2019). 10 g oven dried weight of OPEFB cellulose sample was added with 2.5 N hydrochloric acid with the ratio of 1:20 (OPEFB cellulose to dilute acid) and heated using silicon oil at temperature 106 °C for 20 min. After being hydrolyzed, the sample was then washed with distilled water and 5% NH₄OH solution to achieve a neutral pH of 7. The sample was then dried at 40 ℃ overnight until consistent weight and subsequently ground into fine powder.
Methods
Fourier transform infrared spectroscopy
Fourier transform infrared spectroscopy was performed on an infrared spectrometer (Perkin-Elmer; PC1600, USA) using the potassium bromide (KBr) method. The oven-dried powder of each sample was mixed with KBr with a ratio of 1:100 and then pressed to form a pellet. The pellet was scanned within the range of 500 to 4000 cm-1 at a resolution of 4 cm-1.
Thermogravimetric analysis
A thermogravimetric analyzer (TGA/DSC 1; Mettler-Toledo, Switzerland) was used to determine the thermal stability of the samples. The samples were scanned from 30 ℃ to 800 ℃ at a rate of 10 ℃/min-1 under a nitrogen gas atmosphere. The thermograms showed the plot of weight loss percentage against the temperature.
Differential scanning calorimetry
To determine the melting temperature for all samples, a modified Perkin Elmer Pyris 7 thermal analyzer was used under nitrogen purge at a heating rate of 10 ℃/min from room temperature to 400 ℃.
Morphological analysis
The morphological characteristics of the samples were observed using SEM analysis (Leo Supra 50 VP Field Emission; Carl- ZEISS SMT, Oberkochen, Germany). The entire sample was dried overnight in an oven at 40 ℃ to remove moisture. Then, the sample was coated with platinum before imaging to avoid charging.
X-ray diffraction analysis
The crystallinity of all samples was determined using XRD (D8 Advance; Bruker, Germany), and diffractograms of all samples were collected. The sample data crystallinity was obtained at 2θ between 5° and 45°. The approach of Segal et al. (1959) was used to measure the degree of crystallinity index using Equation 1 as follows,
CrI (%) = (I200 – Iam) / I200 x 100 (1)
where I200 is the peak intensity of the crystalline fraction and Iam is the peak intensity of the amorphous fraction.
RESULTS AND DISCUSSION
FT-IR Analysis
The FT-IR spectra of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC obtained are presented in Fig. 1. The peak assignments are summarized in Table 1. Based on Fig. 1, all samples showed three main absorbance regions, which are single bond region (2500 to 4000 cm-1), double bond region (1500 to 2000 cm-1), and fingerprint region (600 to 1500 cm-1) (Nandiyanto et al. 2019). There are more than five absorbance bands, indicating that the sample is a complex molecule.
Fig. 1. FT-IR spectra of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
There was a broad peak in the range 3200 to 3600 cm-1, indicating a hydrogen bond. This band confirms the presence of hydrate (H2O) and hydroxyl (OH) groups. The broad peak located from 3200 to 3600 cm-1 was assigned to the stretching vibration of -OH groups while the peak at 2900 cm1 represented the stretching vibration of C-H in -CH2 groups of primary alcohol (Fathy et al. 2016). In the double bond region (1500 to 2000 cm-1), peaks at 1641 cm-1 were detected. The absorbance band at 1641 cm-1 was due to the O-H bending of water molecules, and this showed the absorbance of water molecules by the samples due to the strong interaction between water molecules and cellulose (Haafiz et al. 2013; Trache et al. 2016). In the fingerprint region (600 to 1500 cm-1), several peaks were detected and indicated an aromatic ring. The absorbance band at 1425 cm-1 was assigned to the bending vibration of -CH2 group (Haafiz et al. 2013). The absorbance band at 1168 cm-1 was due to the stretching vibration of a glycosidic bond (C-O-C), while the absorbance band at 896 cm-1 attributed to the rock vibration of C-H in cellulose (Fahma et al. 2010; Haafiz et al. 2013). From Fig. 1, the absorbance band at 1518 cm-1 can be seen clearly in the EFB spectrum and was due to the skeletal vibration of aromatic C=C. However, the absorbance band was absent in the spectra of bleached pulp (NaClO2-Pulp and TCF-Pulp) and MCC from both OPEFB-NaClO2-MCC and OPEFB-TCF-MCC, indicating that the lignin component in the EFB sample was completely removed after bleaching (Fahma et al. 2010; Haafiz et al. 2013). Moreover, the intensity of the peak at 1433 cm-1 for OPEFB-TCF-MCC increased, which suggested a higher degree of crystallinity of OPEFB-TCF-MCC (Hussin et al. 2016).
Table 1. FT-IR Spectral Peak Assignments for OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
Through comparing the FT-IR spectra obtained, the spectra did not show particular changes based on the peak frequency, which suggested that the acid hydrolysis used to produce the MCC from bleached pulp will not affect the chemical structure of cellulosic components in MCC (Haafiz et al. 2013, 2014)
Thermal Properties
The results of the thermogravimetric analysis TGA (Fig. 2a) and differential thermogravimetric analysis DTG (Fig. b) curves were used to characterize the chemical phase to ascertain the thermal stability of cellulose and MCCs samples (OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, OPEFB-TCF-MCC). Table 2 shows the summary of the result of the changes in the thermal properties of the prepared samples which is important for the development of high temperature biocomposite materials.
Table 2. Thermal Properties of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
The TGA graph illustrated the sample’s weight loss over time while it was heated at a constant ramp rate. In the range of 50 to 400 °C, the thermogram curve revealed two weight loss expressions. Based on Fig. 2, the initial weight loss in the range of 50 to 150 °C was due to the evaporation of water from the surface of the samples. The sample’s intermolecular hydrogen bound water was evaporated at a temperature of around 150 °C. The second set of decreased in the curves in the range of 250 to 400 °C was due to the degradation of cellulose via disintegration of glycosyl units followed by transformation to char that occurred at maximum temperature of 250 °C to 400 °C, accounting for around 80% of the overall degradation. This was followed by the char formation (Haafiz et al. 2013, 2019).
a)
b)
Fig. 2. a) TGA and b) DTG curves of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
Thermal degradation was seen at a lower temperature than the cellulose sample throughout a wider temperature range, indicating a reduced thermal stability because of a higher number of free ends in the chain, a reduction in molecular weight, and breakdown of cellulose’s amorphous domains (Mandal and Chakrabarty 2011). This result was similar with previous studies (Haafiz et al. 2013; Hassan et al. 2019).
Based on Table 2, the degradation and DTG peak temperature of MCC were lower than OPEFB cellulose pulp, which may be due to the drastic decrease in the molecular weight of the latter caused by the acid hydrolysis that makes it more vulnerable to degrade when temperature increases (Haafiz et al. 2013; Dungani et al. 2017). It was observed that sample that was prepared using NaClO2 treatment displayed higher thermal stability compared to those obtained by the TCF treatment.
However, the residual weight of MCC at 400 °C was higher than that of cellulose pulp due to the high crystallinity of MCC that makes it more flame resistant (Mandal and Chakrabarty 2011; Haafiz et al. 2013). Furthermore, it is worth mentioning that the sample prepared using NaClO2 delignification showed higher residual weight at 400 °C compared to those obtained by TCF treatment. The highest residual weight of EFB at 400 °C suggested that it contains inorganic material, such as ash, that cannot be degraded during the analysis (Taiwo et al. 2017).
Morphology Analysis
The surface morphology of all the OPEFB cellulose and MCC samples was also studied by SEM analysis, as shown in Fig. 3 (a to f). It was discovered that the morphology of MCC changed after treatment. The SEM images showed changes of morphology dimensions in terms of size and shapes of OPEFB pulp and OPEFB MCC.
Fig. 3. SEM images of all cellulose: a) OPEFB-Raw, b) OPEFB-Unbleached Pulp, c) OPEFB-NaClO2-C, d) OPEFB-TCF-C, e) OPEFB-NaClO2-MCC, and f) OPEFB-TCF-MCC
The OPEFB-Raw as Fig. 3a shows a slightly rough surface area with irregular flake-like structure, which possibly can be attributed to the presence of substances like wax, lignin, and hemicelluloses (Taiwo et al. 2017). After alkaline treatment without delignification process, there was no noticeable different between OPEFB- Raw and OPEFB-Unbleached Pulp. Bleaching treatment clearly changed the morphology of the OPEFB as shown in Figs. 3c and 3d. Both NaClO2 and TCF bleached samples showed a clean and smoother surface and showed a long and uniform fibre. This result indicated that lignin and hemicelluloses were removed.
The MCC obtained after acid hydrolysis of the all the cellulose exhibited irregular shape, small-sized fibrils with diameters ranging from 10 to 19 μm, and the MCC also agglomerated with each other. Each bleaching treatment shows a slightly rough surface. Because of depolymerisation of cellulose polymers to a shorter chained MCC, the structure of MCC differed from that of cellulose (Mat Soom et.al. 2009).This was probably caused by removal of hemicellulose, silica, and lignin.
XRD Analysis
X-Ray diffraction analysis was used to study the crystallographic structure of prepared sample materials. The XRD pattern of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC are presented in Fig. 4. The patterns of XRD of various fibres are shown in Fig. 4. The peaks of these fibres were associated with cellulose type I structure.
Fig. 4. XRD pattern of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
The percentage of crystallinity index, CI (%), of all samples was calculated and displayed in Table 3. Studies show that cellulose consists of both crystalline and amorphous regions. Based on literature studies, the structure of the samples showed four characteristic peaks, with amplitudes ranging from 14 to 34.4. It is clear that cellulose I does not have doublets and that the absence of cellulose II is observable. Analysis showed that the crystallinity index of the MCC sample was higher than the starting cellulose sample. This indicates the removal of amorphous regions throughout the process. In this study, the crystallinity index of MCC from NaClO2 delignification method compared to MCC from TCF delignification was 64.5% and 61.5%, respectively. The MCC with NaClO2 delignification method showed the peaks as sharper and more intense as compared to the TCF delignification method. This might be due to the presence of some hemicelluloses that are not completely removed in TCF delignification, which leads to selective solubilization of the amorphous and hemicelluloses rather than the amorphous part of cellulose (Kishani et al. 2018).
Table 3. CI of OPEFB-Raw, OPEFB-Unbleached Pulp, OPEFB-NaClO2-C, OPEFB-TCF-C, OPEFB-NaClO2-MCC, and OPEFB-TCF-MCC
This result further shows that the acid hydrolysis process is not only utilized to hydrolyze the amorphous portions of cellulose molecules, but it also removes the remaining amorphous hemicelluloses.
CONCLUSIONS
- Microcrystalline cellulose (MCC) was successfully isolated from oil palm empty fruit bunch (OPEFB) using different delignification processes after the acid hydrolysis process. The study showed a notable effect of the diversified delignification protocols on the MCC samples based on the characterization, studies of both MCC produced were comparable to commercial MCC-CMCC.
- The scanning electron microscopy (SEM) analysis illustrated that NaClO2 – MCC exhibited a rough and compact structure, similar to TCF-MCC, although it exhibited smaller size of MCC. The Fourier transform infrared (FTIR) analysis revealed that both acidified chlorite and totally chlorine free (TCF) delignification influenced the purity of cellulose without any impact on cellulose chemical structure. The X-ray diffraction (XRD) analysis showed that the different delignification methods used did not alter the crystal structure from the cellulose 1 allomorph of OPEFB, and the crystallinity index ranged from 61% to 69%. From the studies, acidified chlorite delignification produced a higher crystallinity index of MCC than the MCC produced from TCF delignification. Thermal analysis indicated that MCC produced through acidified chlorite delignification cellulose had good thermal stability compared to TCF delignification.
- The finding of this study suggests that OPEFB MCC prepared with acidified chlorite delignification presented higher crystallinity index and higher thermal stability compared to TCF delignification process. However, the scope of these studies does not cover environmental considerations; it is only limited to diverse preparation milieu.
- The study concludes that MCC samples produced from OPEFB using NaClO2 is capable of giving high-value composite products compared to the MCC produced using TCF delignification treatment.
ACKNOWLEDGMENTS
The authors acknowledge Fundamental Research Grant Scheme (Grant number: FRGS/1/2022/STG05/USM/02/10), for providing financial support for this research.
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Article submitted: June 1, 2022; Peer review completed: August 28, 2022; Revised version received: October 21, 2022; Accepted: December 19, 2022; Published: January 20, 2023.
DOI: 10.15376/biores.18.1.1901-1915