Pitcha Liewchirakornab and
Kamonwad Ngamchuea*a
aSchool of Chemistry, Institute of Science, Suranaree University of Technology, 111 University Avenue, Suranaree, Muang, Nakhon Ratchasima 30000, Thailand. E-mail: kamonwad@g.sut.ac.th; Tel: +66 (0) 44 224 637
bInstitute of Research and Development, Suranaree University of Technology, 111 University Avenue, Suranaree, Muang, Nakhon Ratchasima, 30000, Thailand
First published on 13th October 2023
Herein, a low-cost electrolytic technology for starch modification has been developed using abundant chloride salt as a redox mediator. The effects of electrolysis conditions on the in situ starch modification are investigated in detail, including chloride concentrations, applied voltages, and electrolysis durations. The modification mechanisms are determined by the type of chlorine species (Cl2, HClO, ClO−, and HCl) generated during the process. Following electrolysis, carbonyl and carboxyl groups ranging from 0.056 to 1.3 g/100 g of starch and 0.006 to 0.5 g/100 g of starch, respectively, were observed. Starch granule median size can be reduced from 15.3 μm to 13.5 μm. In addition to the pronounced changes in granule size, shape, and functional groups, electrolysis leads to increased moisture resistance, higher crystallinity, and substantial alterations in the pasting properties.
However, cassava starch in its native form has limitations in physicochemical properties, and it is necessary to modify the chemical structures and functionalities of starch to have the desired properties and broaden its applications. These desired properties include, for example, reduced viscosity, shear stability, thermal stability, improved moisture resistance, and increasing chemical compatibility with other polymers.12–15 Industrial production of modified starch involves the utilization of hazardous chemicals, physical processes, enzymes, and the combination approaches.16,17 Additionally, there are alternative methods for starch modification, such as ozone treatment,18,19 corona electrical discharge,20 ultrasound treatment,21 microwave,22 pulsed electric fields23 and electrochemical techniques.24–26 Table 1 presents a comprehensive overview of the various techniques employed for the modification of starch.
Methods | Chemical reagents | Advantages | Disadvantages | Ref. |
---|---|---|---|---|
Chemical oxidation | e.g. H2O2, HClO, O2, O3, Br2, IO4−, MnO4−, TEMPO (2,2,6,6-tetramethylpiperidine-1-oxyl) | • Simple operation | • Generate waste | 17 |
• Capable of scaling up to industrial levels | • Slow reaction rate; typically require catalyst | |||
Corona electrical discharge | — | • Fast | • May cause crosslinking, increasing polymer weight | 20 |
• Wasteless | • May cause degradation | |||
Ultrasound | — | • Efficient | • Require coupling with other methods for oxidation purposes | 27 |
• Fast | ||||
• Low energy consumption | ||||
Microwave | — | • Efficient | • Uneven heating | 22 |
• Fast | • Require coupling with other methods for oxidation purposes | |||
• Low energy consumption | ||||
Pulsed electric fields | Can be performed with or without reagents e.g. IO4−, ClO−, etc. | • Efficient | • Equipment complexity | 23 |
• Fast | • Relatively high energy consumption | |||
Direct electrooxidation | — | • Mild reaction conditions | • Require high voltage | 24 |
• Generate less waste | • Electrode passivation | |||
Redox-mediated electrooxidation | TEMPO (2,2,6,6-tetramethylpiperidine-1-oxyl) | • Environmentally friendly | • Expensive reagent (TEMPO) | 25 |
Br− | • Low cost (Br− and Cl−) | • Scale-up challenges | ||
Cl− | • Use a small amount of reagent | • Scale-up challenges | 26 | |
• Reagent regenerated after starch modification | • Scale-up challenges | This work | ||
• Generate less waste |
However, chemical processes remain the most commonly employed method for starch modification due to their low investment costs, especially in Southeast Asia. Considering the critical aspects of waste management and environmental impact, the development of green and low-cost technologies becomes imperative for starch modification.
This work aims to address this need by developing a simple electrochemical method, using mild conditions, to modify the functional groups of cassava starch. However, direct electrooxidation of starch requires high overpotentials (high energy input), and its application in aqueous solutions would result in side-reactions of the hydrogen evolution reaction (HER) and oxygen evolution reaction (OER) at the cathode and anode, respectively. In this work, we utilize a chlorine-based system as redox mediators. The oxidizing chlorine species are generated in situ by applying potential or voltage between two conducting electrodes, as demonstrated in Scheme 1. The method relies on the use of readily available, cost-effective, and eco-friendly sodium chloride salt as the starting material, making the process not only highly efficient but also environmentally sustainable. The oxidation of chloride occurs at a much lower potential than the OER, which helps prevent the occurrence of side-reactions and improves the efficiency of starch modification.
Scheme 1 Schematic diagram presenting the typical structure of amylose/amylopectin in cassava starch granule after electrolysis mediated by the in situ generated oxidizing chlorine species (Cl2, HClO, and ClO−).30,31 (a) oxidation at C2 position, (b) oxidation at C2 and C3, and (c) oxidation at the α-1,4-glycosidic linkage.28,29,32 |
However, organic molecules like starches can undergo oxidation through a series of intricate processes that involve numerous radical intermediates and subsequent reactions when chlorine species are generated. Alkyl and carbon radicals are formed during these reactions by the abstraction of hydrogen. The hydroxyl groups at C2, C3, and C6 positions in starches are easily oxidized.28 In other degradation processes, the glycosidic bonds of the glucose units can be attacked by chlorine species, potentially hydrolyzing them into alcohol (OH) groups or converting the C–C bonds into carbonyl groups, including aldehydes, ketones, and carboxylates.29
The focus of our investigation revolves around unraveling the correlations between the applied potential and the extent of starch oxidation during electrolysis. By systematically exploring various electrolyte and oxidation conditions, including applied potential, current density, pH, time, and temperature, we aim to pinpoint the optimal parameters for starch modifications. In addition to examining the modifications of functional groups, we conduct rigorous investigations into the changes in physicochemical properties associated with starch oxidation, encompassing aspects such as starch granule size, viscosity, thermal stability, crystal structure, morphology, and pasting properties. By comprehensively exploring these aspects, this research aims to provide valuable insights into the effects of the proposed oxidation method on starch properties, thereby facilitating its effective and sustainable utilization in diverse applications.
The carbonyl content was expressed as a percent mass fraction of the carbonyl groups per starch, specifically as grams of carbonyl groups per 100 grams of oxidized starch:
(1) |
For carboxyl analysis, 2.00 g of starch was mixed with 25.00 mL of 0.10 N HCl, stirred for 30 minutes, and then washed with deionized water to ensure the absence of chloride residue (verified using silver nitrate solution). The resulting starch was split into two equal portions. The first portion was oven-dried at 40 °C for 12 hours to determine the net dry weight. The other portion was dispersed in 100.0 mL of deionized water, gelatinized in a boiling water bath for 10 minutes, and titrated to a pH of 8.3 with standardized 0.010 N NaOH.
The carboxyl content was expressed as a percent mass fraction of carboxyl groups per starch, specifically as grams of carboxyl groups per 100 grams of oxidized starch:
(2) |
The morphology of the starch granules was examined using a field emission scanning electron microscope (AURIGA FE-SEM/FIB/EDX, Zeiss, Germany). Starch samples were suspended in ethanol to obtain a 1% w/v suspension. The samples were then treated with ultrasound for 15 minutes to prevent aggregation, deposited onto carbon tape, dried at 40 °C for 12 hours, and finally coated with gold for SEM analysis.
The crystal structures of starch samples were analyzed using a powder X-ray diffractometer (D2 Phaser XRD, Bruker, Karlsruhe, Germany) under the following conditions: 30 kV and 10 mA with Cu tube radiation (0.154184 nm), and a scan speed of 2° min−1. Each scan covered a range from 5 to 50°. The relative crystallinity (RC%) of the starch granules was determined using the following equation:
(3) |
The functional groups in the starch samples were evaluated using an ATR-FTIR spectrometer (Tensor 27 FT-IR Spectrometer, Bruker, Germany). The starch powders were oven-dried at 60 °C for 15 hours prior to testing. FTIR spectra were recorded over a wavenumber range from 4000 to 400 cm−1. The resolution was set to 4 cm−1 and each scan was repeated 64 times.
Thermal stability testing of the starch samples was carried out under a nitrogen atmosphere with a heating rate of 10 °C min−1 using a thermal gravimetric analyzer (TGA/DSC 1, Mettler Toledo, Germany). The scanning temperature range extended from 35 to 600 °C.
The pasting properties of starches were assessed using a Rapid Visco Analyzer (MCR-52, Anton Paar, Graz-8054, Austria) following the testing conditions outlined by Chandak et al.35 A starch suspension (1.2 g of dry starch in 13.8 g of deionized water) was initially equilibrated at 50 °C for one minute, then heated from 50 °C to 95 °C at a rate of 6 °C per minute, and maintained at 95 °C for 2.7 minutes. Subsequently, the suspension was gradually cooled back to 50 °C at the same rate and held at that temperature for 2 minutes.
In this section, we assess the resulting carbonyl content in starch after electrolysis. Fig. 1 illustrates a clear time-dependent relationship between the carbonyl group content and electrolysis duration. In the investigations conducted under both 12 V and 24 V applied voltages, a noticeable and time-dependent increase in the concentration of carbonyl groups within starch samples was observed as the electrolysis duration was extended. Note that the selection of the two studied voltages, 12 V and 24 V, was based on their practical applicability in achieving the desired levels of starch oxidation while considering factors like chloride concentration and electrolysis duration. Voltages below 12 V can induce starch oxidation, but achieving a high degree of oxidation requires substantial chloride salt and prolonged electrolysis. Conversely, voltages higher than 24 V yield very low oxidized starch output, resulting in excessively small starch particles. Although using filtration paper with smaller pore size can improve this, the overly fine starch particles may not be suitable for many applications. It is worth noting that the choice of voltage depends on specific applications, as different applications may require starch with varying sizes and degrees of oxidation. However, for the purposes of this study, we focused on 12 V and 24 V to demonstrate the proof-of-concept regarding the effects of voltage on starch oxidation through chloride salt electrolysis.
Fig. 1 Effects of NaCl concentration (wt% based on starch) and electrolysis time on the carbonyl contents in oxidized starches at the applied voltage of (a) 12 V and (b) 24 V. |
At an applied voltage of 12 V (Fig. 1a), when considering starch samples with a lower NaCl concentration of 2.5 wt% (equivalent to 0.04 mol L−1), the carbonyl content showed an escalation from 0.06 g/100 g starch at 30 minutes to 0.17 g/100 g starch at 120 minutes. Similarly, with an elevated NaCl concentration of 5 wt% (0.09 mol L−1), the carbonyl content exhibited a rise from 0.17 g/100 g starch at 30 minutes to 0.48 g/100 g starch at 120 minutes. This trend persisted for higher NaCl concentrations: at 10 wt% NaCl (0.17 mol L−1), the carbonyl content increased from 0.53 g/100 g starch at 30 minutes to 1.0 g/100 g starch at 120 minutes, and for 15 wt% NaCl (0.26 mol L−1), the carbonyl content increased from 0.89 g/100 g starch at 30 minutes to 1.3 g/100 g starch at 120 minutes.
When the applied voltage was increased to 24 V (Fig. 1b), a similar pattern emerged: for starch samples with a low NaCl concentration of 2.5 wt% (0.04 mol L−1), the carbonyl content increased from 0.1 g/100 g starch at 30 minutes to 0.26 g/100 g starch at 120 minutes. With NaCl concentration at 5 wt% (0.09 mol L−1), the carbonyl content rose from 0.2 g/100 g starch at 30 minutes to 0.72 g/100 g starch at 120 minutes. At 10 wt% NaCl (0.17 mol L−1), the carbonyl content exhibited an increase from 0.81 g/100 g starch at 30 minutes to 1.22 g/100 g starch at 120 minutes. Similarly, for 15 wt% NaCl (0.26 mol L−1), the carbonyl content increased from 1.11 g/100 g starch at 30 minutes to 1.24 g/100 g starch at 120 minutes.
Fig. 2 Effects of NaCl concentration (wt% based on starch) and electrolysis time on the carboxyl contents in oxidized starches at the applied voltage of (a) 12 V and (b) 24 V. |
Under an applied voltage of 12 V (Fig. 2a), a low NaCl concentration of 2.5 wt% triggered carboxyl content growth from 0.01 g/100 g starch at 30 minutes to 0.03 g/100 g starch at 120 minutes. Similarly, higher NaCl concentrations (5 wt%, 10 wt%, and 15 wt%) led to increases from 0.04 g/100 g starch to 0.1 g/100 g starch, from 0.17 g/100 g starch to 0.32 g/100 g starch, and from 0.27 g/100 g starch to 0.49 g/100 g starch, respectively, over the same time span.
At the applied voltage of 24 V (Fig. 2b), the carboxyl group content rose from 0.02 g/100 g starch at 30 minutes to 0.07 g/100 g starch at 120 minutes for the 2.5 wt% NaCl concentration. Similarly, for higher NaCl concentrations (5 wt%, 10 wt%, and 15 wt%), the content increased from 0.06 g/100 g starch to 0.18 g/100 g starch, from 0.31 g/100 g starch to 0.38 g/100 g starch, and from 0.41 g/100 g starch to 0.5 g/100 g starch, respectively. Notably, the increase of carboxyl content is less pronounced at the highest NaCl concentration of 15 wt% (NaCl 0.26 mol L−1), suggesting a saturation point for carbonyl and carboxyl group increase under these conditions.
Sample | Electrolysis conditions | Current during electrolysis (A) | pH after electrolysis | DO (CO + COOH) (g/100 g starch) | Yield (%) | ||
---|---|---|---|---|---|---|---|
NaCl (wt%) | Time (min) | Applied voltage (V) | |||||
a Note: (i) pH of deionized water = 6.95 ± 0.1, (ii) pH of native starch (8 g) in deionized water (80 mL) = 5.7 ± 0.1, (iii) carbonyl content of native starch = 0.06 ± 0.000 g/100 g starch. | |||||||
1 | 2.5 | 30 | 12 | 0.14–0.16 | 7.34 ± 0.010 | 0.06 ± 0.000 | 98.8 ± 0.21 |
2 | 2.5 | 60 | 12 | 0.14–0.16 | 7.10 ± 0.010 | 0.09 ± 0.000 | 98.5 ± 0.33 |
3 | 2.5 | 120 | 12 | 0.14–0.16 | 3.83 ± 0.010 | 0.19 ± 0.000 | 97.9 ± 0.40 |
4 | 5 | 30 | 12 | 0.27–0.30 | 7.63 ± 0.010 | 0.20 ± 0.000 | 98.4 ± 0.96 |
5 | 5 | 60 | 12 | 0.27–0.30 | 3.88 ± 0.010 | 0.37 ± 0.000 | 94.1 ± 0.32 |
6 | 5 | 120 | 12 | 0.27–0.30 | 3.33 ± 0.010 | 0.57 ± 0.001 | 90.2 ± 0.39 |
7 | 10 | 30 | 12 | 0.54–0.60 | 7.63 ± 0.010 | 0.70 ± 0.001 | 92.6 ± 0.21 |
8 | 10 | 60 | 12 | 0.54–0.60 | 3.14 ± 0.010 | 1.16 ± 0.002 | 86.3 ± 0.22 |
9 | 10 | 120 | 12 | 0.54–0.60 | 3.31 ± 0.010 | 1.32 ± 0.002 | 83.1 ± 0.64 |
10 | 15 | 30 | 12 | 0.82–0.90 | 7.42 ± 0.006 | 1.17 ± 0.001 | 86.1 ± 0.60 |
11 | 15 | 60 | 12 | 0.82–0.90 | 3.14 ± 0.010 | 1.60 ± 0.002 | 85.8 ± 0.88 |
12 | 15 | 120 | 12 | 0.82–0.90 | 3.25 ± 0.006 | 1.79 ± 0.002 | 76 ± 0.39 |
13 | 2.5 | 30 | 24 | 0.35–0.38 | 7.30 ± 0.010 | 0.12 ± 0.000 | 98.4 ± 0.85 |
14 | 2.5 | 60 | 24 | 0.35–0.38 | 3.67 ± 0.010 | 0.26 ± 0.001 | 98.2 ± 0.16 |
15 | 2.5 | 120 | 24 | 0.35–0.38 | 3.34 ± 0.010 | 0.34 ± 0.002 | 97.3 ± 0.33 |
16 | 5 | 30 | 24 | 0.68–0.75 | 7.36 ± 0.010 | 0.25 ± 0.000 | 98.2 ± 0.99 |
17 | 5 | 60 | 24 | 0.68–0.75 | 3.20 ± 0.010 | 0.58 ± 0.001 | 93.8 ± 0.14 |
18 | 5 | 120 | 24 | 0.68–0.75 | 3.09 ± 0.010 | 0.91 ± 0.001 | 87.3 ± 0.61 |
19 | 10 | 30 | 24 | 1.28–1.50 | 7.05 ± 0.010 | 1.12 ± 0.001 | 91.0 ± 0.35 |
20 | 10 | 60 | 24 | 1.28–1.50 | 3.13 ± 0.010 | 1.36 ± 0.002 | 86.0 ± 0.71 |
21 | 10 | 120 | 24 | 1.28–1.50 | 2.97 ± 0.010 | 1.60 ± 0.004 | 82.6 ± 0.14 |
22 | 15 | 30 | 24 | 1.84–2.10 | 2.85 ± 0.010 | 1.52 ± 0.003 | 86.0 ± 0.72 |
23 | 15 | 60 | 24 | 1.84–2.10 | 3.05 ± 0.010 | 1.58 ± 0.004 | 78.3 ± 1.00 |
24 | 15 | 120 | 24 | 1.84–2.10 | 2.97 ± 0.010 | 1.74 ± 0.004 | 31.25 ± 1.09 |
The increase in carbonyl and carboxyl content depends on the concentration of NaCl, the duration of electrolysis, and the applied voltage. These variations are linked to the in situ formation of oxidizing chlorine species (HClO, ClO−, and Cl2), which can subsequently create acids, causing pH fluctuations and changes in the composition of oxidizing chlorine species within the solution. Higher NaCl concentrations result in a greater concentration of the generated oxidizing chlorine species. Moreover, the application of a higher voltage leads to increased carbonyl and carboxyl levels due to enhanced oxidation and reduction rates occurring at the anode and cathode.
However, at the highest NaCl concentration (15 wt%), an increase in voltage has a limited effect on carbonyl and carboxyl group increase, potentially due to structural degradation during electrolysis. The action of chlorine species can hydrolyze the amorphous regions (α-1,4-glycosidic linkage) before the α-1,6-glycosidic linkage of the granules, which in turn can enhance the crystallinity of the starch.36 This process reduces starch molecular weight and hot paste viscosity.37 Therefore, the amount of carbonyl and carboxyl groups on starch granules possibly increases, but some that deteriorated under severe electrolysis conditions could break off significantly, resulting in very small fragments smaller than 2 μm. These fragments could be lost during the filtration process using filter paper (2 μm), leading to a lower concentration of carbonyl and carboxyl groups than usual.
As the electrolysis was carried out at high voltages (up to 24 V) and high currents (up to 2.10 A), it was essential to investigate the potential effects of electrode poisoning. We examined both the surface and electroactivity of the electrodes before and after the electrolytic modifications using an optical microscope and cyclic voltammetry of the [Fe(CN)6]4−/3− standard redox probe, respectively. The results, as depicted in Fig. S2 and S3 (ESI),† revealed that there were no significant changes in the appearance of the electrodes. However, following electrolysis, a slight decrease in the electroactivity of both the anode and cathode was observed, possibly due to some degree of electrode passivation. Nevertheless, the electrode activities could be restored through a cleaning procedure involving immersion in a 0.10 M HCl solution for 2 minutes, followed by mechanical polishing using alumina slurry (1.0, 0.3, and 0.05 μm, Buehler, USA) on soft polishing microcloths (Buehler, USA), and subsequent sonication to remove any remaining alumina from the surface.
Sample | D50 (μm) |
---|---|
Native cassava starch | 15.3 ± 0.05 |
NaCl 5 wt% based on starch, 12 V, 30 min | 15.0 ± 0.08 |
NaCl 5 wt% based on starch, 12 V, 120 min | 14.6 ± 0.03 |
NaCl 10 wt% based on starch, 12 V, 30 min | 14.9 ± 0.08 |
NaCl 10 wt% based on starch, 12 V, 60 min | 14.8 ± 0.09 |
NaCl 10 wt% based on starch, 12 V, 120 min | 14.7 ± 0.21 |
NaCl 15 wt% based on starch, 12 V, 30 min | 14.8 ± 0.14 |
NaCl 15 wt% based on starch, 12 V, 60 min | 14.5 ± 0.23 |
NaCl 15 wt% based on starch, 12 V, 120 min | 14.0 ± 0.17 |
NaCl 5 wt% based on starch, 24 V, 30 min | 14.7 ± 0.02 |
NaCl 5 wt% based on starch, 24 V, 120 min | 14.5 ± 0.22 |
NaCl 10 wt% based on starch, 24 V, 30 min | 14.6 ± 0.15 |
NaCl 10 wt% based on starch, 24 V, 60 min | 14.4 ± 0.14 |
NaCl 10 wt% based on starch, 24 V, 120 min | 14.1 ± 0.08 |
NaCl 15 wt% based on starch, 24 V, 30 min | 14.4 ± 0.02 |
NaCl 15 wt% based on starch, 24 V, 60 min | 13.9 ± 0.01 |
NaCl 15 wt% based on starch, 24 V, 120 min | 13.5 ± 0.30 |
Fig. 3 The particle size of native starch compared with oxidized starch prepared using 15 wt% NaCl, the applied voltage of 24 V, and the electrolysis time of 30–120 minutes. |
In particular, the study focused on modified starches and their granule median size changes under different NaCl concentrations and applied voltages during electrolysis. The experimentation began at a NaCl concentration of 5 wt% due to minimal size change below this concentration. The granule median size decreased from 15.0 to 14.0 μm when the NaCl concentration was increased to 15 wt% with an electrolysis time of 120 minutes and an applied voltage of 12 V. This reduction was attributed to hydrochloric acid presence during electrolysis, which hydrolyzed starch granules. The oxidation and electrolysis reactions primarily affected amylose before amylopectin, leading to the separation of both components. This oxidation and electrolysis process, driven by chlorine species, caused the breaking of 1,4-glycosidic linkages and consequently reduced starch size.36
A higher applied voltage of 24 V resulted in a stronger electrolysis reaction compared to 12 V, leading to greater reduction in granule median size under the same conditions. Specifically, a NaCl concentration of 15 wt% combined with an applied voltage of 24 V significantly reduced starch median size from 14.4 to 13.5 μm over an electrolysis time ranging from 30 minutes to 120 minutes, due to enhanced chlorine generation and subsequent increase in solution acidity. The interplay of these factors, along with increased chlorine gas dissolution and subsequent hydrochloric and hypochlorous acid formation, contributed to the more substantial reduction in granule median size for this specific condition.
Fig. 5 XRD patterns of (a) native starch and oxidized starches modified using (b) 10 wt% NaCl, 12 V, 30 min, (c) 15 wt% NaCl, 24 V, 30 min, and (d) 15 wt% NaCl, 24 V, 60 min. |
The % relative crystallinity was further determined from the ratio of integrated crystalline area and total integrated area of the XRD patterns, according to the method previously described in the literature.39 The initial relative crystallinity of native starch stands at approximately 22.4%. Following electrolysis under NaCl 10 wt%, 12 V, 30 min conditions, the modified starch experiences an increase in relative crystallinity to 22.8%, while the NaCl 15 wt%, 24 V, 30 min condition elevates this value to 23.3%. The most pronounced increase is witnessed under the rigorous electrolysis conditions of NaCl 15 wt%, 24 V, 120 min, resulting in the highest relative crystallinity of 24.2%. This augmented crystallinity arises from the transformation of some amorphous or amylose portions into small fragments during electrolysis. The shorter amylose chains, due to their smaller size, can move and undergo rearrangement, leading to an increase in crystallinity.40,41 Besides, these fragments are small (<2 μm), enough to pass through filter paper during the filtration process.
Fig. 6 ATR-FTIR spectra of (a) native starch and oxidized starch prepared using (b) 10 wt% NaCl, 24 V, 30 min, (c) 15 wt% NaCl, 24 V, 30 min, (d) 15 wt% NaCl, 24 V, 120 min. |
The ATR-FTIR analysis demonstrated changes in starch's functional groups following oxidation and electrolysis, particularly notable in starch modified under severe electrolysis conditions (15 wt% NaCl, 24 V, 120 min). Modified starch displayed reduced water absorption compared to native starch. The decline in peak height at 1005 cm−1 confirmed the transformation of C–OH at C2, C3, and C6 into carbonyl and carboxyl groups. Furthermore, reduced peak heights at 1149 cm−1 and 924 cm−1 was associated with starch depolymerization at alpha glycosidic linkage due to oxidation and electrolysis reactions.
Fig. 7 Thermal gravimetric analysis of (a) native starch, and oxidized starches using (b) 10 wt% NaCl, 12 V, 30 min, (c) 15 wt% NaCl, 24 V, 30 min, and (d) 15 wt% NaCl, 24 V, 120 min. |
Upon considering the modification of starch under severe conditions (15 wt% NaCl, 24 V, 120 min), it becomes evident that the gelatinization and retrogradation properties are lost. This is manifested by the occurrence of consistent viscosity (91.0 cP) during testing. This outcome is attributed to significant alterations in the morphology of starch granules, as can be observed in Fig. 4i and j. The oxidized starch sample subjected to these conditions exhibits heightened hardness and is almost translucent, setting it apart from native starch.
The pasting temperature (PT) of native cassava starch is 68.3 °C. When cassava starch is oxidized under different conditions (varying concentrations of NaCl, applied voltage, and electrolysis time), the resulting starches exhibit higher pasting temperatures, ranging from 69.1 to 73.5 °C (Table S1, ESI).† These effects, including the lack of indications for swelling, gelatinization, and retrogradation behaviors during the pasting test, as well as the elevated pasting/gelatinizing temperature,45 result from a significant reduction in starch granule size, a notably low amylose content, and an increase in crystallinity.46
Next, the study compares native starch and oxidized starches in terms of viscosity properties. Native starch has the highest peak viscosity (PV) of 1996 cP, while oxidized starches show reduced PV values due to depolymerization reactions caused by acid-thinning and oxidation, which occur mainly in the amorphous area of the starch granules.47 Breakdown viscosity (BDV) measures starch's resistance to heat and shear.35 Native starch has the highest BDV of 1065 cP, while certain oxidized starches under specific electrolysis conditions may exhibit no BDV due to reduced resilience (the ability to absorb and store energy when it is deformed), refer to Table S1, ESI.†
The final viscosity (FV) of starch indicates how amylose molecules assemble and increase viscosity upon cooling. Among the tested starches, native starch has the highest FV at 1511 cP. The oxidized starches showed reduced FV values ranging from 869.4 cP to 73.0 cP (Table S1, ESI).† This reduction is primarily influenced by the remaining amount of amylose after electrolysis, which affects water retention. Starch granules with lower water absorption and smaller size demonstrate less development of final viscosity upon cooling.35
Setback viscosity (SBV) is a measure of how starch forms gels or retrogrades.48 Native starch has an SBV of 579.7 cP. In general, the oxidized starches had lower SBV values, while some oxidized starches had no SBV at all (Table S1, ESI†). Setback is the process in which tangled starch molecules reassociate to create a network that retains water. Native starches displayed higher setback than modified ones, suggesting they are more stable against retrogradation, or the process of forming such networks.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3ra06382h |
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