• Tidak ada hasil yang ditemukan

A Thesis Submitted for the Award of the Degree of

N/A
N/A
Protected

Academic year: 2023

Membagikan "A Thesis Submitted for the Award of the Degree of "

Copied!
221
0
0

Teks penuh

Department of Chemical Technology Department of Chemical Technology Indian Institute of Technology Guwahati Indian Institute of Technology Guwahati. Furthermore, I would like to thank all other faculty and staff members of the Department of Chemical Engineering for their invaluable support during my research.

TO DEVELOP FUNCTIONAL FOOD AND PAPER BASED INDICATOR FROM ANTHOCYANIN

APPENDIX I-X

81 Table 3.6 Optimal conditions in the UAE for black and purple rice bran 88 Table 3.7 Compounds identified in the UAE extract of purple rice bran by. Table 4.1 Pseudo-first- and pseudo-second-order kinetics model parameters 106 Table 4.2 Adsorption isotherm model constants for anthocyanin at various.

Fig. 5.8.  Release profile of anthocyanin from microcapsule  144  Fig. 5.9.  Effect of microencapsulated powder on a) storage modulus b) loss modulus
Fig. 5.8. Release profile of anthocyanin from microcapsule 144 Fig. 5.9. Effect of microencapsulated powder on a) storage modulus b) loss modulus

INTRODUCTION

Rice bran

The bioactive compounds in rice bran have purported health benefits as well as antioxidant activity. Rice bran is therefore considered a potential source of several high-value bioactive compounds for use as additives in food, pharmaceuticals and cosmetics (Lloyd et al., 2000).

Pigmented rice bran

Bioactive compounds 1. Phenolic compounds

  • Anthocyanin

Because the anthocyanins have enormous industrial and commercial values, few researchers used engineered microorganisms to develop anthocyanin in the laboratory (Lim et al., 2015). Regardless of the sources, however, the color of anthocyanin is highly dependent on the pH of the environment. water phase (Ekici et al., 2014).

Fig. 1.1: The basic chemical structure of anthocyanin
Fig. 1.1: The basic chemical structure of anthocyanin

Extraction of bioactive compounds

  • Conventional extraction
    • Soxhlet extraction
    • Maceration
    • Hydrodistillation
  • Non-conventional extraction techniques
    • Enzyme-assisted extraction
    • Microwave-assisted extraction
    • Supercritical fluid extraction
    • Ultrasound-assisted extraction

Furthermore, the solvents commonly used for extraction are recognized as safe (da Silva et al., 2016). Assisted extraction has been shown to be an economically viable technique for the extraction of heat-sensitive bioactive compounds (Chemat et al., 2017).

Adsorption of bioactive compounds

Additionally, ultrasound-assisted extraction is used as a continuous process in the extraction industry (Pan et al., 2011). Adsorption of bioactive compounds from plant sources is considered as a physisorption process (Puri et al., 2012).

Microencapsulation of bioactive compound through spray drying

Microencapsulation is an effective way to improve the products' bioavailability and stability, as well as to manage the release of the active agent (Mahdavi et al., 2016). Spray drying involves making a homogeneous mixture of the core material and wall material, which is then atomized inside a spray dryer (Nedovic et al., 2011).

Table 1.3: Microencapsulation processes for anthocyanins  Process   Wall Material   Anthocyanin
Table 1.3: Microencapsulation processes for anthocyanins Process Wall Material Anthocyanin

Ready to cook food product

Commonly used wall materials for anthocyanin encapsulations are maltodextrin, gum arabic (Brouillard and Delaporte, 1977), skimmed milk powder (Hossain et al., 2009) and starches (Tonon et al., 2010). Researchers have used modified starch as a wall material to encapsulate various bioactive compounds (Hoyos-Leyva et al., 2018; Lacerda et al., 2016; Tonon et al., 2010).

Functional ready to cook extrudate food

However, due to high temperature and shear, the bioactive compounds are generally degraded during extrusion preparation. Therefore, the development of extrudate foods enriched with bioactive compounds is a challenge for the food technologist.

Smart packaging application Shukla et al. 2016) Agar/potato starch Smart packaging application Choi et al. In the paper sensor, different types of paper were used as substrate such as hydrophilic filter paper (Cai et al., 2014) Whatman no.

Fig. 1.2: Changes of anthocyanin structure in various pH   1.10. Anthocyanin based pH sensitive paper indicator
Fig. 1.2: Changes of anthocyanin structure in various pH 1.10. Anthocyanin based pH sensitive paper indicator

Knowledge gap and objectives of the thesis

Modeling and optimization of supercritical fluid extraction of anthocyanins and phenolic compounds from Syzygium cumini fruit pulp. Optimization of microwave-assisted extraction of anthocyanins from purple corn cob (Zea mays L.) and identification by HPLC–.

MATERIALS AND METHODS

  • Chemicals
  • Phytochemical profiling
    • Total phenolic contents
    • Monomeric anthocyanin content
    • Flavonoid content
    • Antioxidant properties
    • GC-MS analysis of extract
    • β-Carotene, tocopherol, and tocotrienol
    • Cyanidin-3-glucoside and peonidin-3-glucoside
    • Phenolic acid
  • Physicochemical properties 1. Water activity
    • Bulk density
    • True density
    • Water solubility index (WSI)
    • Porosity
    • Hausner ratio
    • Specific mechanical energy
    • Color
    • Cooking yield, cooking loss, and optimal cooking time
    • X-Ray diffraction
    • FT-IR analysis
    • Morphological properties
    • Steady-shear rheology
    • Oscillatory rheological properties
  • Storage study
  • Extraction
    • Conventional extraction
    • Ultrasound-assisted extraction
  • Adsorption and desorption 1. Pretreatment of adsorbent
    • Adsorption and desorption tests
    • Adsorption kinetics
    • Adsorption isotherm
    • Thermodynamic parameters of adsorption
  • Degradation experiment
    • Preparation of samples with hydrocolloids
    • Degradation studies
    • Degradation kinetics of anthocyanin
  • Encapsulation
    • Preparation of feed sample
    • Encapsulation
  • Extrusion

The color of the sample changed from yellowish to bluish depending on the concentration of phenolic compounds. The DPPH scavenging activity of the extract was measured as described by Wojdyło et al. The actual density of the extrudate was measured using a gas pycnometer (model: PYC-100A, Porous Materials Inc, brand: Ithaca, New York, USA) .

The encapsulation efficiency of the sample was measured using the method described by Mahdavi et al. Hunter Colorimeter (Make: HunterLab, Reston, Virginia, Model: ColorLab Ultrascan Vis) was used to measure the color of the sample.

Fig. 2.2: Calibration curve for the determination of total phenolic content
Fig. 2.2: Calibration curve for the determination of total phenolic content
  • Determination of sorption isotherms
  • Mathematical modelling of sorption isotherm
  • Paper indicator
    • Fabrication of pH sensitive paper indicator
    • Evaluation of indicator in simulated condition
    • Evaluation of indicator in food system
    • Color stability of indicator
    • Degradation kinetics of color
  • Design of experiment
    • Response surface methodology for microencapsulation process
    • Response surface methodology for extrusion cooking
  • Artificial Neural Networks (ANN)
    • Prediction of TPC for conventional extraction process
    • Prediction of TPC and anthocyanin for ultrasound assisted extraction process Four independent variables, i.e., temperature, pH, solvent (ethanol) concentration and
  • Statistical analysis

The indicator was applied to various food systems with a wide pH range to evaluate the performance of the indicator. The RCCD data were used to train (70%), test (15%) and validate (15%) the ANN model to effectively predict the experimental result. The best neural network training performance was determined based on the highest regression coefficient (R2).

Design Expert 7.0.0 software (Stat-Ease, Minneapolis, USA) was used to design the experiment. Effects of specific mechanical energy on the physicochemical properties of texturized soy protein during high-moisture extrusion cooking.

Fig. 2.4: Schematic diagram of extruder
Fig. 2.4: Schematic diagram of extruder

TO EVALUATE THE EXTRACTION PROCESSES USING SOLVENT

ANTHOCYANIN) FROM PURPLE AND BLACK RICE BRAN

TO EVALUATE THE EXTRACTION PROCESSES USING SOLVENT EXTRACTION TECHNIQUE FOR BIOACTIVE

  • Model and response surface analysis
    • Model fitting
    • Analysis of response surfaces
    • Optimization and prediction of parameters
    • Validation of optimal condition
    • Comparison of ANN and RSM models
  • Phytochemical properties
    • Total phenolic, anthocyanin, and flavonoid content
    • Phenolic acid
    • Antioxidant properties 1. DPPH scavenging activity
  • Modelling of UAE extraction process
  • Response surface analysis
    • Response surface analysis of total phenolic content
    • Response surface analysis of anthocyanin content
  • Optimization and validation of extraction conditions
  • Comparison with conventional extraction process
  • Comparison between ANN and RSM models
  • Analysis
    • GC-MS analysis of extract
    • β-Carotene, tocopherol, and tocotrienol
    • Cyanidin-3-glucoside and peonidin-3-glucoside
    • Phenolic acids

3.7 (a, b, c and d) shows the effect of pH, time (min), solvent concentration (%) and temperature (°C) on the content of monomeric anthocyanin in black and purple rice bran extract. Furthermore, an increase in pH above 2.5 drastically reduced the monomeric anthocyanin content of the rice bran extract. The change in solvent concentrations strongly influenced the content of monomeric anthocyanins in black and purple rice bran extract.

TPC and monomeric anthocyanin in black and purple rice bran extract compared with conventional extraction procedure. GC-MS analysis of black and purple rice bran extract is shown in Table 3.7.

Fig. 3.2: Influence of ethanol concentration a 1 ) acetone concentration a 2 ), temperature  b) extraction time c) solvent to solid ratio  d) on the extraction yield of TPC for purple  rice bran (    ) and black rice bran (   )
Fig. 3.2: Influence of ethanol concentration a 1 ) acetone concentration a 2 ), temperature b) extraction time c) solvent to solid ratio d) on the extraction yield of TPC for purple rice bran ( ) and black rice bran ( )

Summary

Optimization of ultrasound-assisted extraction of anthocyanins from haskap berries (Lonicera caerulea L.) using Response Surface Methodology. Optimization of ultrasound-assisted extraction of phenolic compounds, antioxidants and anthocyanins from sugar beet molasses. Optimization of ultrasonic extraction of phenolic compounds, antioxidants and anthocyanins from grape (Vitis vinifera) seeds.

Optimization of ultrasonic extraction of phenolic compounds from Euryale ferox seed pods using response surface methodology. Optimization of ultrasound assisted extraction of phenolic compounds from Sparganii rhizome with response surface methodology.

TO STUDY THE ADSORPTION AND DESORPTION CHARACTERISTICS

OF ANTHOCYANIN EXTRACTED FROM PURPLE RICE BRAN AND ITS

DEGRADATION KINETICS

TO STUDY THE ADSORPTION AND DESORPTION CHARACTERISTICS OF ANTHOCYANIN EXTRACTED FROM

Results and discussion

  • Adsorption and desorption of anthocyanin
  • Adsorption kinetics
  • Adsorption isotherms
    • Two parameter isotherms Langmuir isotherm model
    • Three parameter isotherms Redlich–Peterson isotherm model
  • Diffusion model
  • Thermodynamics parameters of adsorption
  • Anthocyanin and phenolic acid analysis

The adsorption kinetics of anthocyanin on XAD2, XAD4, XAD7 and bentonite are shown in Table 4.1. It was revealed from Table 4.1 that the pseudo-first order model agreed well with the adsorption data and gave higher coefficients of determination (R2). It was inferred from the result that the adsorption of anthocyanin on adsorbents was diffusion controlled (Yuh-Shan, 2004).

The adsorption mechanism of anthocyanin from purple rice bran extract on adsorbents was investigated using the Weber and Morris intra-particle diffusion model. It can therefore be concluded that the adsorption process of anthocyanin on XAD7 can be carried out at 28 °C.

Fig.  4.3:  Modelling  of  the  kinetics  data  using  a)  pseudo-first-order  kinetics,  and  b)  pseudo-second-order kinetics model
Fig. 4.3: Modelling of the kinetics data using a) pseudo-first-order kinetics, and b) pseudo-second-order kinetics model

Degradation of anthocyanins

  • Effect of pH
  • Effect of different temperature
  • Effect of degradation on color change
  • Effect of hydrocolloids on anthocyanins and antioxidant activity during pH based degradation
  • Effect of hydrocolloids on anthocyanins and antioxidant activity during thermal degradation
  • Effect of modified starch on degradation kinetics of anthocyanin

For increasing temperature, the rate of degradation increased due to the change and deterioration of the chemical structure of C3G and P3G. The effect of hydrocolloids on the stability of monomeric anthocyanin, C3G and P3G in pH 6 at ambient conditions (28 ± 2 oC) was investigated and shown in Table 4.8. Guan and Zhong (2015) suggested that during thermal treatment for the formation of complexes with gum arabic, the degradation of anthocyanin was inhibited.

The modified starch showed higher anthocyanin retention and antioxidant activity in pH and thermal degradation. The higher stability of anthocyanin in modified starch medium may be due to complex formation with highly branched amylopectin in starch (Lewis et al., 1995) and reduced water activity of the medium.

Table 4.6: Degradation kinetics parameters for anthocyanin, C3G, and P3G
Table 4.6: Degradation kinetics parameters for anthocyanin, C3G, and P3G

Summary

Modified rice starch showed a promising effect on anthocyanin stability and antioxidant activity than the other hydrocolloids. Adsorption/desorption characteristics and separation of anthocyanins and polyphenols from blueberries using macroporous adsorbent resins. Effects of temperature, time and pH on the stability of anthocyanin extracts: prediction of total anthocyanin content using nonlinear models.

Pananglapped iti thermal degradation ti anthocyanins iti tubbog ti blackberry babaen ti pannakainayon ti nadumaduma nga asukar Pananglapped iti thermal degradation ti anthocyanins iti tubbog ti blackberry babaen ti pannakainayon ti nadumaduma nga asukar. Nagtipon nga epekto ti pH ken nangato a temperatura iti kinatalged ken antioxidant capacity ti dua nga anthocyanins iti aqueous solution.

TO EVALUATE THE

MICROENCAPSULATION PROCESS OF ANTHOCYANIN AND ITS EFFECT

ON RICE DOUGH RHEOLOGY

TO EVALUATE THE MICROENCAPSULATION PROCESS OF ANTHOCYANIN AND ITS EFFECT ON RICE DOUGH RHEOLOGY

Results and discussion 1. Analysis of variance

  • Response surface analysis
  • Optimization and validation
  • Physicochemical properties of powder
  • Gelatinization properties
  • X-ray diffraction patterns
  • Surface morphology
  • Storage study
  • Dynamic oscillatory rheology

5.2 (c and e) it is shown that to increase the inlet air temperature; the anthocyanin content and DPPH scavenging activity of the microencapsulated powder decrease due to the heat sensitivity of anthocyanin. For increasing starch concentration up to 7% (w/v), anthocyanin content and DPPH scavenging activity of the powder increased, and then both decreased. An increase in starch concentration increases the viscosity of the emulsion, which inhibits internal circulation and increases the activity of the microcapsule in scavenging anthocyanin and DPPH (Bhandari et al., 1992).

There were noticeable differences in the peak melting temperatures of native, modified starch and encapsulated powder. In addition, the effect of the spray drying process may also be responsible for the distinct peak of the microencapsulated anthocyanin powder.

Table 5.1: Analysis of variance for the fitted quadratic polynomial model  Terms  Encapsulation
Table 5.1: Analysis of variance for the fitted quadratic polynomial model Terms Encapsulation

Summary

Moreover, for the increase of microencapsulated powder concentration from 5 to 20% (w/w), there was a sharp increase in moduli value, as shown in Figure. This increase in moduli suggested that internal structure rearrangement occurred during the oscillatory test. and this made the dough stiffer. Active chitosan/PVA films with anthocyanins from Brassica oleraceae (red cabbage) as time-temperature indicators for application in intelligent food packaging.

Effects of spray drying conditions on the physicochemical and antioxidant properties of the Gac (Momordica cochinchinensis) fruit seed powder. Digestibility and physicochemical properties of rice flour (Oryza sativa L.) and starch with different amylose content.

TO DEVELOP FUNCTIONAL FOOD AND PAPER BASED INDICATOR

FROM ANTHOCYANIN

TO DEVELOP FUNCTIONAL FOOD AND PAPER BASED INDICATOR FROM ANTHOCYANIN

Results and disscussion

  • Prelimeniery study for extrusion cooking
  • Regression analysis
  • Response surface analysis
    • Effect of process variable on anthocyanin content
    • Effect of process parameter on true density
    • Effect of process parameter on water activity
    • Effect of process parameter on water solubility index
    • Effect of process parameter on specific mechanical energy
  • Optimization and validation
  • Comparison of physico-chemical properties
  • Storage study
  • Paper indicator
    • Sensitivity of color value
    • Color sensitivity in simulated condition
    • Color stability
    • Comparison of sensitivity with literature

However, for increasing the extrusion temperature, the cooking loss of the extrudate decreases (Fig. 6.2b), due to proper gelatinization and the formation of a strong starch network. For the increase in moisture content in the food material, an increase in the water activity of the extrudate is observed (Fig. 6.3f). However, beyond the specified screw speed, the WSI of the finished product decreases may be due to less.

Thus, after a certain concentration of anthocyanin, there was no further increase in the brightness of the indicator. This is due to the deprotonation of the quinonoid base structure of anthocyanin and formed a colorless carbinol pseudo base structure on the indicator.

Fig. 6.2: Effect of a) screw speed, b) temperature, and c) moisture content on WSI (   )  and cooking loss (   )
Fig. 6.2: Effect of a) screw speed, b) temperature, and c) moisture content on WSI ( ) and cooking loss ( )

Summary

The purple potato and grape were used as sources of anthocyanin to make the above pH indicators. In the present study, purple rice waste bran was used for the extraction of anthocyanin for depositing the filter paper from the indicator. The average b sensitivity of this work is 9.3 times more than that of pH indicator films composed of agar/potato starch and 2.5 times more than chitosan-based pH indicator films, whereas the average a sensitivity is almost close to Choi et eel. 2017) and are slightly more than Yoshida et al.

The higher sensitivity of this assay was achieved due to the use of slightly opaque white filter paper, whereas the starch and chitosan used in Choi et al. 2014) are almost transparent white in color, which ensures a lower sensitivity. In addition, the time required for colorimetric measurements (20 s) using our filter paper pH indicator was lower than previous works (Choi et al., 2017; Yoshida et al., 2014).

Gambar

Fig. 5.8.  Release profile of anthocyanin from microcapsule  144  Fig. 5.9.  Effect of microencapsulated powder on a) storage modulus b) loss modulus
Fig. 1.2: Changes of anthocyanin structure in various pH   1.10. Anthocyanin based pH sensitive paper indicator
Fig. 3.2: Influence of ethanol concentration a 1 ) acetone concentration a 2 ), temperature  b) extraction time c) solvent to solid ratio  d) on the extraction yield of TPC for purple  rice bran (    ) and black rice bran (   )
Table 3.1: Analysis of variance of the regression parameters   Response  Sources  Sum of
+7

Referensi

Dokumen terkait

ii TABLE OF FIGURES Table 1: Latent heat of fusion by different manufacturer 9 Table 2: Mesh independent test 12 Table 3: Gantt chart 15 Table 4: Model dimension 17 Table 5: