# Isolation of Prebiotics fromArtocarpus integer’s Seed

Authors: Joel-Ching-Jue Wong; Siew-Ling Hii; Chen-Chung Koh
Journal: International Journal of Food Science
 (2021)

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## Abstract

There has been a high amount of attention given to prebiotics due to their significant physiological function and health benefits. Prebiotics contain nondigestible compounds that allow specific changes, both in the growth and in the activity of bacteria in the host gastrointestinal tract, that provide benefits upon the host by promoting a healthy digestive system and preventing disease. This study aims at investigating the potential prebiotic activity of bioactive compounds extracted from the seeds of an underutilized indigenous plantArtocarpus integer (A. integer). The optimum microwave-assisted extraction conditions were a microwave power of 1500 W, extraction time of 180 s, and solvent-to-sample ratio of 1000 : 1. The maximum amount of the total carbohydrate content extracted from A. integer was 787 mg/L. The percentage hydrolysis levels of A. integer extract in gastric juice at pH 1, 2, 3, and 4 were 6.14%, 7.12%, 8.98%, and 10.23%, respectively. For enzymatic digestion, the percentage of hydrolysis was 0.16% at pH 7. A. integer extract was found to support the growth of probiotics such as L. acidophilus and L. casei. After 72 hours of incubation, L. acidophilus achieved 6.96 log10 CFU, whereas L. casei reached 8.33 log10 CFU. The study makes an important contribution to the development of the use of Sarawakian underutilized plants and to the identification of new sources of prebiotic materials to be used in food.


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## Body

## 1. Introduction

In this globalization era, human societies have become more urban and economic activity is mainly geared towards being manufacturing based rather than being agricultural based. Human lifestyle, diet, and physical activity are greatly affected by this phenomenon. Humans have more leisure time, most of them have the privilege to sample a wider variety of foods, and their lifestyle needs less physical activity. The biodiversity of the human gut microbiota is more likely to be affected by this modern lifestyle, which results in changes of its microbial composition that are associated with increased propensity to a wide range of chronic and noncommunicable diseases (NCD) such as high blood pressure, cardiovascular disease, and type 2 diabetes [1]. The introduction of prebiotics might be a possible way to solve this situation. Many studies on prebiotics have confirmed them to be clinically effective in increasing the number of human gut microbiota to improve human health conditions. According to the International Scientific Association for Probiotics and Prebiotics [2], prebiotics are “substrates that are selectively utilized by host microorganisms conferring health benefits.” The host microorganism is well-known as a probiotic, a selected and viable microorganism that, when introduced in sufficient amounts, beneficially affects the human organisms through their effects in the intestinal tract [3].The major prebiotics are identified as inulin and oligosaccharides. Prebiotics are often obtained through three different techniques: isolation from natural resources, microbiological synthesis, and enzymatic degradation of polysaccharides [4]. A food ingredient is classified as prebiotic if it fulfils three criteria. First, it must be a nondigestible food which is resistant to gastric acidity, mammalian enzymatic digestion, and intestinal absorption. Second, the food must be susceptible to fermentation by the intestinal microbiota. Third, it must selectively stimulate the growth and/or activity of beneficial microbiota that inhabit the intestine of mammals, including human [5].As the largest state in Malaysia, Sarawak carries abundant biodiversity and has endemic flora and fauna that are different from the other regions of the country. Plants such asterung asam, dabai, cempedak, and engkala have been exploited traditionally by various ethnic and indigenous people living in Sarawak. The crops are highly consumed by Sarawakians and can be considered as a culinary specialty [6]. Nowadays, these plants or crops remain largely underutilized as sustenance for the general population. Underutilized plant species only receive little investment through formal research and development, although they can make a stronger contribution to nutrition, health, income, and sustainability of the environment [7]. However, most of the underutilized plant species are reported as natural sources of bioactive ingredients that possess the potential to be further developed into functional foods. This study aims at investigating the potential of developing underutilized botanical sources into food that helps to maintain the general well-being and prevent diseases. The seed of chempedak (Artocarpus integer) was selected as an agricultural material for further study.A. integer is the scientific name for the tropical fruit chempedak. It is a large and unique composite tropical fruit that belongs to the Moraceae family. A. integer originates in the forests of equatorial countries in the Indian subcontinent and Southeast Asia countries such as Malaysia, Thailand, Indonesia, Myanmar, and Vietnam, where it grows extensively in the wild [8]. It is locally called chempedak and cultivated as a commercial commodity in Malaysia. It offers benefits as a profitable multipurpose crop for producing timber and fruits. In Malaysia, A. integer is mainly used for medicinal and culinary purposes. In terms of medicinal use, A. integer has been used as a traditional folk medicine in Malaysia for curing diseases such as inflammation, malarial fever and ulcers, abscess, and diarrhoea [9]. In terms of culinary use, A. integer is used in its immature and ripe form. Immature fruit is used for making pickles in curry preparation while ripe fruit with golden yellow colour bulbs can be consumed straight. Ripe fruit pulp is eaten fresh or made into different local delicacies, including chutney, jam, jelly, and paste, or preserved as sweets by drying or mixing with sugar, honey, or syrup [10].The significance of extracting biologically active ingredients of interest from raw materials is generally acknowledged. Extraction represents the primary procedure in the analysis of plants because it is a prerequisite to extract the desired bioactive compounds from the plants. The extracted compounds must undergo further isolation and identification or characterization of its components. The extraction method involved in this study was microwave-assisted extraction (MAE). MAE is one of the innovative techniques of extraction, which has been extensively applied for the isolation, analysis, and quantification of bioactive ingredients. In MAE, microwave energy is used to heat solvents in contact with solid samples or liquid samples (or heat samples, e.g., fresh tissues), promoting the partition of sample-related compounds into the solvent.


## 2. Materials and Methods

### 2.1. Materials

Mature fruits ofA. integer were obtained from the Central Market, Sibu, Sarawak, Malaysia, and were transported immediately to the laboratory and stored at 4°C until further use. Human salivary α-amylase was purchased from Sigma-Aldrich. All chemicals used in this study were of analytical grade unless specified otherwise. Lactobacillus acidophilus DSM 20079, Lactobacillus casei DSM 20011, and Escherichia coli DSM 1103 were purchased from Leibniz-Institut DSMZ GmbH (Braunschweig, Germany). All stock cultures were maintained in sterile glycerol (30% v/v) at −20°C.


### 2.2. Preparation ofA. integer’s Fibrous Powder (AIFP)

A. integer’s fibrous powder (AIFP) was prepared following Larrauri [11] recommendations for obtaining fibrous powder from the seeds. The fruit was cleaned under running tap water to remove visible dirt. Then, the seeds were obtained by peeling the fruit and removing the pulp. The mass of seeds was determined. The seeds were subjected to a wet-milling process with the ratio of 1 g of seed to 1 mL of water. The juice and pomace from the seeds were separated by a cotton cloth filter. The weight of pomace was recorded. After that, the pomace was cleaned with water for 5 min. The ratio of pomace from seed to water is 1 : 2 (w/v). After washing, the pomace was filtered by a cotton cloth filter and dried at 50°C for 18 hours. After the drying process, the pomace was ground by blender again to make it into powder form for sieving purpose. The powder was sieved to pass through 250 μm sieve to obtain A. integer’s fibrous powder (AIFP). The powder was stored in a polypropylene container at −20°C until further analysis.


### 2.3. Microwave-Assisted Extraction

#### 2.3.1. Experimental Design

In the present study, microwave-assisted extraction method was applied to extract oligosaccharides fromA. integer’s fibrous powder (AIFP). The two-level full factorial design (FFD) was the first experimental design applied. Three process parameters, i.e., microwave power (A, Watt), extraction time (B, seconds), and solvent-sample ratio (C), were investigated for their effects towards the amount of total carbohydrate (Y, mg/L) produced.Each independent variable was assigned with two levels such as high (+1) and low (−1) levels corresponding to the minimum and maximum values of the factors under evaluation (Table1).Table 1
Independent variables and their levels used in two-level FFD.
Independent variableNotationUnitLow (−1)High (+1)Microwave powerAWatt1501500Extraction timeBSeconds30180Solvent-sample ratioC—1001000Table2 shows a total of twenty-eight (28) experimental runs with eight (8) different combinations of experiments in duplicate and twelve (12) centre points, together with the results of the response of the study. The experimental design was generated and analysed, and the predicted data were calculated using the Design-Expert® Software (version 10, Stat-Ease Inc., Minneapolis, MN, USA).Table 2
Design matrix of two-level FFD with total carbohydrate (Y) as response.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY1−1 (150)−1 (30)−1(100)222−1 (80)+1 (180)−1 (100)373−1 (150)−1 (30)+1 (1000)1774−1 (150)+1 (180)+1 (1000)1675−1 (150)+1 (180)+1 (1000)22760 (825)0 (105)0 (550)41570 (825)0 (105)0 (550)44780 (825)0 (105)0 (550)3649+1 (1500)+1 (180)+1 (1000)90510+1 (1500)+1 (180)+1 (1000)87211+1 (1500)−1 (30)−1 (100)3412−1 (150)−1 (30)+1 (1000)219130 (825)0 (105)0 (550)33914+1 (1500)+1 (180)−1 (100)9415+1 (1500)−1 (30)−1 (100)2816−1 (150)−1 (30)−1 (100)3617+1 (1500)+1 (180)−1 (100)8018+1 (1500)−1 (30)+1 (1000)19419−1 (150)+1 (180)−1 (100)9720+1 (1500)−1 (30)+1 (1000)170210 (825)0 (105)0 (550)345220 (825)0 (105)0 (550)393aFactors: A: microwave power (watts); B: extraction time (seconds); C: ratio of solvent to sample. Uncoded values are presented in brackets. bExperimental results of the response under investigation.Following the two-level FFD experimental work, additional experimental runs were performed for the FFD model with significant curvature. This process is known as the augmented central composite design (CCD), which is one of the many designs of the response surface methodology (RSM) technique. The augmented CCD is shown in Table3. It is a continuation of the two-level FFD by saving time for the experimenter to build another RSM model from scratch.Table 3
Design matrix of augmented CCD.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY23−1 (150)0 (105)0 (550)64240 (825)0 (105)−1 (100)41250 (825)−1 (30)0 (550)6726+1 (1500)0 (105)0 (550)230270 (825)+1 (180)0 (550)199280 (825)0 (105)+1 (1000)299aFactors: A: microwave power (watts); B: extraction time (seconds); C: solvent-sample ratio. Uncoded units are presented in brackets. bExperimental results of the response under investigation.


#### 2.3.2. Extraction and Purification Procedures

Microwave-assisted extraction was performed using a microwave oven with a frequency of 2450 MHz, 34 L capacity, and 1500 W input power. In each of the series of experiments, theA. integer’s fibrous powder (AIFP) was mixed with deionised water according to the specified solvent-sample ratio. The extraction was then performed at the respective settings of power and duration (Tables 2 and 3). Following this, the mixture was centrifuged at 4000 rpm, 4°C for 5 min, and the supernatant was mixed with 1 mL of trichloroacetic acid (50% w/v) to deproteinise the supernatant. After removal of the precipitate, the supernatant was dialysed against deionised water overnight (molecular weight cutoff (MWCO), 500 Da) to remove unwanted low-molecular weight compounds. Nondialysed liquid (extracted sample) was collected and stored at 4°C until further analysis.


### 2.4.In Vitro Digestion Studies

#### 2.4.1. Digestion by Gastric Juice

Simulated human gastric juice was prepared by suspending the following chemicals in 1 L of deionised water: 8 g sodium chloride (NaCl), 0.2 g potassium chloride (KCl), 8.25 g disodium phosphate dihydrate (Na2HPO4.2H2O), 14.35 g sodium hydrogen phosphate (NaHPO4), 0.1 g calcium chloride dihydrate (CaCl2.2H2O), and 0.18 g magnesium chloride hexahydrate (MgCl2.6H2O). The acidity levels of the gastric juice were adjusted to pH 1, 2, 3, and 4 by using 5 M hydrochloric acid (HCl).One mL of the extracted sample was mixed with 1 mL of simulated human gastric juices of various pH and incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for final reducing sugar content (Section 2.6.2). The 1% w/v of inulin solution was used as a positive control. The contents of total carbohydrate (Section 2.6.1) and reducing sugar of the extracted sample before the digestion process were also determined.The percentage of hydrolysis of the extracted sample was calculated by using equation (1) as follows:
(1)%hydrolysis=finalreducingsugarcontent−initialreducingsugarcontenttotalcarbohydratecontent−initialreducingsugarcontent×100%


#### 2.4.2. Enzymatic Digestion

In vitro enzymatic digestions of extracted samples and inulin (positive control) by using human salivary α-amylase were conducted [12]. The enzyme with an activity of 5.2 μmol/mL/min was prepared in 20 mM sodium phosphate buffer (pH 7) to give a final concentration of 0.45 mg/mL.One mL of enzyme solution was mixed with 1 mL extracted sample. The mixtures were incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for the final reducing sugar content. The 1% w/v of inulin solution was used as a positive control. The total carbohydrate content and total reducing sugar content of the extracted sample before digestion were also determined. The percentage of hydrolysis of the extracted sample was calculated by using equation (1).


### 2.5.In Vitro Fermentation of Extracted Sample

Lactobacillus acidophilus DSM 20079, Lactobacillus casei DSM 20011, and Escherichia coli DSM 1103 were selected to investigate their abilities to ferment the extracted plant materials. The fermentation process was conducted with DeMan, Rogosa, and Sharpe (MRS) broth for the Lactobacillus species while tryptic soy (TS) broth was for E. coli. Fermentation was carried out in the respective culture broth in which the glucose was replaced by the extracted sample.After inoculation with the respective bacterial cultures, the media were incubated for up to 72 hours. All incubation, fermentation, and enumeration ofLactobacillus species were performed in an anaerobic system.The viable count of the bacterial cultures was determined by total plate count using MRS agar for theLactobacillus and TS agar for E. coli. The result was expressed as log10 CFU.


### 2.6. Analytical Procedures

#### 2.6.1. Determination of the Total Carbohydrate Content

The total carbohydrate content was determined by the phenol-sulphuric acid method [13]. One mL of the extracted sample was mixed with 1 mL of 5% phenol solution, and 5 mL concentrated sulphuric acid was added subsequently to the mixture. The mixture was vortexed and incubated in a water bath at 30°C for 30 min before the measurement of absorbance at 490 nm. The amount of total carbohydrate in each sample was obtained using the D-glucose standard curve.


#### 2.6.2. Determination of Reducing Sugar Content

The reducing sugar content was determined by dinitrosalicylic acid (DNSA) assay [14]. One mL of the extracted sample was mixed with 1 mL DNSA reagent. The mixture was heated in a boiling water bath for 15 min. Following this, 0.2 mL of 40% (w/v) potassium sodium tartrate solution was added to the mixture and 0.8 mL deionised water was added to cool down the mixture. Then, the mixture was vortexed and its absorbance was measured at 575 nm. The D-glucose was used as the standard for determination of the reducing sugar content in the extracted sample.


### 2.7. Statistical Analysis ofIn Vitro Studies

Every experiment was conducted in triplicate. All results were expressed asmean±standard deviation. Statistical analysis was performed using IBM SPSS version 23 (SPSS Inc., Chicago, IL, USA). Experimental results were subjected to one-way analysis of variance (ANOVA) and the significant difference among the means at 95% confidence limits (p<0.05) was determined by the Tukey test.


## 2.1. Materials

Mature fruits ofA. integer were obtained from the Central Market, Sibu, Sarawak, Malaysia, and were transported immediately to the laboratory and stored at 4°C until further use. Human salivary α-amylase was purchased from Sigma-Aldrich. All chemicals used in this study were of analytical grade unless specified otherwise. Lactobacillus acidophilus DSM 20079, Lactobacillus casei DSM 20011, and Escherichia coli DSM 1103 were purchased from Leibniz-Institut DSMZ GmbH (Braunschweig, Germany). All stock cultures were maintained in sterile glycerol (30% v/v) at −20°C.


## 2.2. Preparation ofA. integer’s Fibrous Powder (AIFP)

A. integer’s fibrous powder (AIFP) was prepared following Larrauri [11] recommendations for obtaining fibrous powder from the seeds. The fruit was cleaned under running tap water to remove visible dirt. Then, the seeds were obtained by peeling the fruit and removing the pulp. The mass of seeds was determined. The seeds were subjected to a wet-milling process with the ratio of 1 g of seed to 1 mL of water. The juice and pomace from the seeds were separated by a cotton cloth filter. The weight of pomace was recorded. After that, the pomace was cleaned with water for 5 min. The ratio of pomace from seed to water is 1 : 2 (w/v). After washing, the pomace was filtered by a cotton cloth filter and dried at 50°C for 18 hours. After the drying process, the pomace was ground by blender again to make it into powder form for sieving purpose. The powder was sieved to pass through 250 μm sieve to obtain A. integer’s fibrous powder (AIFP). The powder was stored in a polypropylene container at −20°C until further analysis.


## 2.3. Microwave-Assisted Extraction

### 2.3.1. Experimental Design

In the present study, microwave-assisted extraction method was applied to extract oligosaccharides fromA. integer’s fibrous powder (AIFP). The two-level full factorial design (FFD) was the first experimental design applied. Three process parameters, i.e., microwave power (A, Watt), extraction time (B, seconds), and solvent-sample ratio (C), were investigated for their effects towards the amount of total carbohydrate (Y, mg/L) produced.Each independent variable was assigned with two levels such as high (+1) and low (−1) levels corresponding to the minimum and maximum values of the factors under evaluation (Table1).Table 1
Independent variables and their levels used in two-level FFD.
Independent variableNotationUnitLow (−1)High (+1)Microwave powerAWatt1501500Extraction timeBSeconds30180Solvent-sample ratioC—1001000Table2 shows a total of twenty-eight (28) experimental runs with eight (8) different combinations of experiments in duplicate and twelve (12) centre points, together with the results of the response of the study. The experimental design was generated and analysed, and the predicted data were calculated using the Design-Expert® Software (version 10, Stat-Ease Inc., Minneapolis, MN, USA).Table 2
Design matrix of two-level FFD with total carbohydrate (Y) as response.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY1−1 (150)−1 (30)−1(100)222−1 (80)+1 (180)−1 (100)373−1 (150)−1 (30)+1 (1000)1774−1 (150)+1 (180)+1 (1000)1675−1 (150)+1 (180)+1 (1000)22760 (825)0 (105)0 (550)41570 (825)0 (105)0 (550)44780 (825)0 (105)0 (550)3649+1 (1500)+1 (180)+1 (1000)90510+1 (1500)+1 (180)+1 (1000)87211+1 (1500)−1 (30)−1 (100)3412−1 (150)−1 (30)+1 (1000)219130 (825)0 (105)0 (550)33914+1 (1500)+1 (180)−1 (100)9415+1 (1500)−1 (30)−1 (100)2816−1 (150)−1 (30)−1 (100)3617+1 (1500)+1 (180)−1 (100)8018+1 (1500)−1 (30)+1 (1000)19419−1 (150)+1 (180)−1 (100)9720+1 (1500)−1 (30)+1 (1000)170210 (825)0 (105)0 (550)345220 (825)0 (105)0 (550)393aFactors: A: microwave power (watts); B: extraction time (seconds); C: ratio of solvent to sample. Uncoded values are presented in brackets. bExperimental results of the response under investigation.Following the two-level FFD experimental work, additional experimental runs were performed for the FFD model with significant curvature. This process is known as the augmented central composite design (CCD), which is one of the many designs of the response surface methodology (RSM) technique. The augmented CCD is shown in Table3. It is a continuation of the two-level FFD by saving time for the experimenter to build another RSM model from scratch.Table 3
Design matrix of augmented CCD.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY23−1 (150)0 (105)0 (550)64240 (825)0 (105)−1 (100)41250 (825)−1 (30)0 (550)6726+1 (1500)0 (105)0 (550)230270 (825)+1 (180)0 (550)199280 (825)0 (105)+1 (1000)299aFactors: A: microwave power (watts); B: extraction time (seconds); C: solvent-sample ratio. Uncoded units are presented in brackets. bExperimental results of the response under investigation.


### 2.3.2. Extraction and Purification Procedures

Microwave-assisted extraction was performed using a microwave oven with a frequency of 2450 MHz, 34 L capacity, and 1500 W input power. In each of the series of experiments, theA. integer’s fibrous powder (AIFP) was mixed with deionised water according to the specified solvent-sample ratio. The extraction was then performed at the respective settings of power and duration (Tables 2 and 3). Following this, the mixture was centrifuged at 4000 rpm, 4°C for 5 min, and the supernatant was mixed with 1 mL of trichloroacetic acid (50% w/v) to deproteinise the supernatant. After removal of the precipitate, the supernatant was dialysed against deionised water overnight (molecular weight cutoff (MWCO), 500 Da) to remove unwanted low-molecular weight compounds. Nondialysed liquid (extracted sample) was collected and stored at 4°C until further analysis.


## 2.3.1. Experimental Design

In the present study, microwave-assisted extraction method was applied to extract oligosaccharides fromA. integer’s fibrous powder (AIFP). The two-level full factorial design (FFD) was the first experimental design applied. Three process parameters, i.e., microwave power (A, Watt), extraction time (B, seconds), and solvent-sample ratio (C), were investigated for their effects towards the amount of total carbohydrate (Y, mg/L) produced.Each independent variable was assigned with two levels such as high (+1) and low (−1) levels corresponding to the minimum and maximum values of the factors under evaluation (Table1).Table 1
Independent variables and their levels used in two-level FFD.
Independent variableNotationUnitLow (−1)High (+1)Microwave powerAWatt1501500Extraction timeBSeconds30180Solvent-sample ratioC—1001000Table2 shows a total of twenty-eight (28) experimental runs with eight (8) different combinations of experiments in duplicate and twelve (12) centre points, together with the results of the response of the study. The experimental design was generated and analysed, and the predicted data were calculated using the Design-Expert® Software (version 10, Stat-Ease Inc., Minneapolis, MN, USA).Table 2
Design matrix of two-level FFD with total carbohydrate (Y) as response.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY1−1 (150)−1 (30)−1(100)222−1 (80)+1 (180)−1 (100)373−1 (150)−1 (30)+1 (1000)1774−1 (150)+1 (180)+1 (1000)1675−1 (150)+1 (180)+1 (1000)22760 (825)0 (105)0 (550)41570 (825)0 (105)0 (550)44780 (825)0 (105)0 (550)3649+1 (1500)+1 (180)+1 (1000)90510+1 (1500)+1 (180)+1 (1000)87211+1 (1500)−1 (30)−1 (100)3412−1 (150)−1 (30)+1 (1000)219130 (825)0 (105)0 (550)33914+1 (1500)+1 (180)−1 (100)9415+1 (1500)−1 (30)−1 (100)2816−1 (150)−1 (30)−1 (100)3617+1 (1500)+1 (180)−1 (100)8018+1 (1500)−1 (30)+1 (1000)19419−1 (150)+1 (180)−1 (100)9720+1 (1500)−1 (30)+1 (1000)170210 (825)0 (105)0 (550)345220 (825)0 (105)0 (550)393aFactors: A: microwave power (watts); B: extraction time (seconds); C: ratio of solvent to sample. Uncoded values are presented in brackets. bExperimental results of the response under investigation.Following the two-level FFD experimental work, additional experimental runs were performed for the FFD model with significant curvature. This process is known as the augmented central composite design (CCD), which is one of the many designs of the response surface methodology (RSM) technique. The augmented CCD is shown in Table3. It is a continuation of the two-level FFD by saving time for the experimenter to build another RSM model from scratch.Table 3
Design matrix of augmented CCD.
RunsExperimental factorsaTotal carbohydrate (mg/L)bABCY23−1 (150)0 (105)0 (550)64240 (825)0 (105)−1 (100)41250 (825)−1 (30)0 (550)6726+1 (1500)0 (105)0 (550)230270 (825)+1 (180)0 (550)199280 (825)0 (105)+1 (1000)299aFactors: A: microwave power (watts); B: extraction time (seconds); C: solvent-sample ratio. Uncoded units are presented in brackets. bExperimental results of the response under investigation.


## 2.3.2. Extraction and Purification Procedures

Microwave-assisted extraction was performed using a microwave oven with a frequency of 2450 MHz, 34 L capacity, and 1500 W input power. In each of the series of experiments, theA. integer’s fibrous powder (AIFP) was mixed with deionised water according to the specified solvent-sample ratio. The extraction was then performed at the respective settings of power and duration (Tables 2 and 3). Following this, the mixture was centrifuged at 4000 rpm, 4°C for 5 min, and the supernatant was mixed with 1 mL of trichloroacetic acid (50% w/v) to deproteinise the supernatant. After removal of the precipitate, the supernatant was dialysed against deionised water overnight (molecular weight cutoff (MWCO), 500 Da) to remove unwanted low-molecular weight compounds. Nondialysed liquid (extracted sample) was collected and stored at 4°C until further analysis.


## 2.4.In Vitro Digestion Studies

### 2.4.1. Digestion by Gastric Juice

Simulated human gastric juice was prepared by suspending the following chemicals in 1 L of deionised water: 8 g sodium chloride (NaCl), 0.2 g potassium chloride (KCl), 8.25 g disodium phosphate dihydrate (Na2HPO4.2H2O), 14.35 g sodium hydrogen phosphate (NaHPO4), 0.1 g calcium chloride dihydrate (CaCl2.2H2O), and 0.18 g magnesium chloride hexahydrate (MgCl2.6H2O). The acidity levels of the gastric juice were adjusted to pH 1, 2, 3, and 4 by using 5 M hydrochloric acid (HCl).One mL of the extracted sample was mixed with 1 mL of simulated human gastric juices of various pH and incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for final reducing sugar content (Section 2.6.2). The 1% w/v of inulin solution was used as a positive control. The contents of total carbohydrate (Section 2.6.1) and reducing sugar of the extracted sample before the digestion process were also determined.The percentage of hydrolysis of the extracted sample was calculated by using equation (1) as follows:
(1)%hydrolysis=finalreducingsugarcontent−initialreducingsugarcontenttotalcarbohydratecontent−initialreducingsugarcontent×100%


### 2.4.2. Enzymatic Digestion

In vitro enzymatic digestions of extracted samples and inulin (positive control) by using human salivary α-amylase were conducted [12]. The enzyme with an activity of 5.2 μmol/mL/min was prepared in 20 mM sodium phosphate buffer (pH 7) to give a final concentration of 0.45 mg/mL.One mL of enzyme solution was mixed with 1 mL extracted sample. The mixtures were incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for the final reducing sugar content. The 1% w/v of inulin solution was used as a positive control. The total carbohydrate content and total reducing sugar content of the extracted sample before digestion were also determined. The percentage of hydrolysis of the extracted sample was calculated by using equation (1).


## 2.4.1. Digestion by Gastric Juice

Simulated human gastric juice was prepared by suspending the following chemicals in 1 L of deionised water: 8 g sodium chloride (NaCl), 0.2 g potassium chloride (KCl), 8.25 g disodium phosphate dihydrate (Na2HPO4.2H2O), 14.35 g sodium hydrogen phosphate (NaHPO4), 0.1 g calcium chloride dihydrate (CaCl2.2H2O), and 0.18 g magnesium chloride hexahydrate (MgCl2.6H2O). The acidity levels of the gastric juice were adjusted to pH 1, 2, 3, and 4 by using 5 M hydrochloric acid (HCl).One mL of the extracted sample was mixed with 1 mL of simulated human gastric juices of various pH and incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for final reducing sugar content (Section 2.6.2). The 1% w/v of inulin solution was used as a positive control. The contents of total carbohydrate (Section 2.6.1) and reducing sugar of the extracted sample before the digestion process were also determined.The percentage of hydrolysis of the extracted sample was calculated by using equation (1) as follows:
(1)%hydrolysis=finalreducingsugarcontent−initialreducingsugarcontenttotalcarbohydratecontent−initialreducingsugarcontent×100%


## 2.4.2. Enzymatic Digestion

In vitro enzymatic digestions of extracted samples and inulin (positive control) by using human salivary α-amylase were conducted [12]. The enzyme with an activity of 5.2 μmol/mL/min was prepared in 20 mM sodium phosphate buffer (pH 7) to give a final concentration of 0.45 mg/mL.One mL of enzyme solution was mixed with 1 mL extracted sample. The mixtures were incubated in a water bath at37±1°C for 5 hours. After incubation, one mL of the mixture was withdrawn and tested for the final reducing sugar content. The 1% w/v of inulin solution was used as a positive control. The total carbohydrate content and total reducing sugar content of the extracted sample before digestion were also determined. The percentage of hydrolysis of the extracted sample was calculated by using equation (1).


## 2.5.In Vitro Fermentation of Extracted Sample

Lactobacillus acidophilus DSM 20079, Lactobacillus casei DSM 20011, and Escherichia coli DSM 1103 were selected to investigate their abilities to ferment the extracted plant materials. The fermentation process was conducted with DeMan, Rogosa, and Sharpe (MRS) broth for the Lactobacillus species while tryptic soy (TS) broth was for E. coli. Fermentation was carried out in the respective culture broth in which the glucose was replaced by the extracted sample.After inoculation with the respective bacterial cultures, the media were incubated for up to 72 hours. All incubation, fermentation, and enumeration ofLactobacillus species were performed in an anaerobic system.The viable count of the bacterial cultures was determined by total plate count using MRS agar for theLactobacillus and TS agar for E. coli. The result was expressed as log10 CFU.


## 2.6. Analytical Procedures

### 2.6.1. Determination of the Total Carbohydrate Content

The total carbohydrate content was determined by the phenol-sulphuric acid method [13]. One mL of the extracted sample was mixed with 1 mL of 5% phenol solution, and 5 mL concentrated sulphuric acid was added subsequently to the mixture. The mixture was vortexed and incubated in a water bath at 30°C for 30 min before the measurement of absorbance at 490 nm. The amount of total carbohydrate in each sample was obtained using the D-glucose standard curve.


### 2.6.2. Determination of Reducing Sugar Content

The reducing sugar content was determined by dinitrosalicylic acid (DNSA) assay [14]. One mL of the extracted sample was mixed with 1 mL DNSA reagent. The mixture was heated in a boiling water bath for 15 min. Following this, 0.2 mL of 40% (w/v) potassium sodium tartrate solution was added to the mixture and 0.8 mL deionised water was added to cool down the mixture. Then, the mixture was vortexed and its absorbance was measured at 575 nm. The D-glucose was used as the standard for determination of the reducing sugar content in the extracted sample.


## 2.6.1. Determination of the Total Carbohydrate Content

The total carbohydrate content was determined by the phenol-sulphuric acid method [13]. One mL of the extracted sample was mixed with 1 mL of 5% phenol solution, and 5 mL concentrated sulphuric acid was added subsequently to the mixture. The mixture was vortexed and incubated in a water bath at 30°C for 30 min before the measurement of absorbance at 490 nm. The amount of total carbohydrate in each sample was obtained using the D-glucose standard curve.


## 2.6.2. Determination of Reducing Sugar Content

The reducing sugar content was determined by dinitrosalicylic acid (DNSA) assay [14]. One mL of the extracted sample was mixed with 1 mL DNSA reagent. The mixture was heated in a boiling water bath for 15 min. Following this, 0.2 mL of 40% (w/v) potassium sodium tartrate solution was added to the mixture and 0.8 mL deionised water was added to cool down the mixture. Then, the mixture was vortexed and its absorbance was measured at 575 nm. The D-glucose was used as the standard for determination of the reducing sugar content in the extracted sample.


## 2.7. Statistical Analysis ofIn Vitro Studies

Every experiment was conducted in triplicate. All results were expressed asmean±standard deviation. Statistical analysis was performed using IBM SPSS version 23 (SPSS Inc., Chicago, IL, USA). Experimental results were subjected to one-way analysis of variance (ANOVA) and the significant difference among the means at 95% confidence limits (p<0.05) was determined by the Tukey test.


## 3. Results and Discussion

### 3.1. Two-Level Full Factorial Design

In the present study, two-level FFD was first employed in the development of three response models, i.e.,A: microwave power, B: extraction time, and C: solvent-sample ratio, on the effect of total carbohydrate extracted (Y).In the Design-Expert® Software, the curvature test is placed in front of the ANOVA when centre points are included in the experimental design. The curvature test involves the randomisation of multiple centre points (replicates) throughout the other experimental conditions to get an adequate assessment of whether the actual values measured at this point match what is predicted by the linear model. If the curvature test is significant, a quadratic or higher-order model is needed to model the relationship between the factors and the response.As shown in Table4, the curvature test of FFD is significant with a p value less than 0.05. Therefore, a response surface model was used as augmentation. A face-centred central composite design (CCD) was chosen as the response surface model, which is comprised of different combinations of six axial points, as shown in Table 3.Table 4
ANOVA of two-level FFD.
SourceSum of squaresa (×105)dfbMean squarec (×105)F valuedp value, Prob>FeRemarkModel11.2471.605177.71<0.0001SignificantA: microwave power1.21611.216134.64<0.0001B: extraction time1.59811.598176.90<0.0001C: solvent-sample ratio3.91613.916433.47<0.0001AB1.31611.316145.67<0.0001AC1.06811.068118.19<0.0001BC0.93510.935103.49<0.0001ABC1.18911.189131.57<0.0001Curvature0.99810.998110.45<0.0001SignificantPure error0.090130.090Cor total12.32021aSum of the differences between the squared value of the average value and the overall mean. bDegree of freedom. cSum of squares divided by df. dRatio of the mean regression sum of squares divided by the mean error sum of squares. eProbability of seeing the observed F value if the null hypothesis is true.


### 3.2. Fitting the Central-Composite Design (CCD) Model

Table5 shows the results of ANOVA for the response surface reduced cubic model conducted at 95% confidence level (p=0.05). The significance of each coefficient of the model was determined using the F test and p value. The larger the F value and the smaller the p value, the more significant was the corresponding model term. The F value of 112.49 and p value that is less than 0.0001 implied the model was very significant. Besides, since the p value of “lack of fit” was 0.2170 (p>0.05), “lack of fit” was not significant. A not-significant “lack of fit” indicated that the model fits the actual experimental response data. The ANOVA results confirmed that the model was precise.Table 5
Response surface reduced cubic model for the total carbohydrate content.
SourceSum of squares (×105)dfMean square (×105)F valuep value, Prob>FRemarkBlock0.54310.543Model13.0591.450112.49<0.0001SignificantA: microwave power1.35411.354104.99<0.0001B: extraction time1.66511.665129.10<0.0001C: solvent-sample ratio4.23514.235328.46<0.0001AB1.31611.316102.05<0.0001AC1.06811.06882.80<0.0001BC0.93510.93572.50<0.0001A20.19010.19014.740.0013B20.26710.26720.670.0003ABC1.18911.18992.18<0.0001Residual0.219170.013Lack of fit0.07440.0191.670.2170Not significantPure error0.149130.011Cor total13.8227The results of regression ANOVA show that the overall mean and standard deviation developed in this model was234.36±35.91mg/L (Table 6). The percentage of coefficient of variation (CV %) was 15.32% which represents a minimum variation of data of the model. The coefficient of determination R2 of 0.9835 indicated an adequately high degree of correlation between experimental and predicted values of the total carbohydrate content. The 98.35% of variation that was observed in the response (total carbohydrate content) can be explained by the model. The difference between adjusted R2 (0.9603) and predicted R2 (0.9747) was less than 0.2, which indicated that the adjusted R2 was in reasonable agreement with the predicted R2. Based on the results, the model was suggested to be a good simulation of the extraction experiment.Table 6
Regression analysis of variance for total carbohydrate content.
SourceValueSDa35.91Mean234.39CV %b15.32PRESSc52712.06R20.9835AdjustedR20.9747PredictedR20.9603Adequate precision38.399aStandard deviation. bPercentage of coefficient of variation. cPredicted residual sum of squares.The equation in terms of coded factors (equation (2)) can be used to make predictions about the total carbohydrate content for given levels of each factor. The coded equation is useful for identifying the relative impact of the factors by comparing the factor coefficients. The relative impact of the factors can be observed through the factor coefficients by referring to the coded equation. The factor coefficient of C (153.39) is the highest among the three factors. Therefore, factor C had the highest impact on the total carbohydrate content. The positive factor coefficient refers to a positive effect and vice versa.The final equation in terms of coded factors generated by the software was expressed as follows:(2)Y=291.61+86.72A+96.17B+153.39C+90.69AB+81.69AC+76.44BC−75.91A2−89.91B2+86.19ABC.The equation in terms of actual factors (equation (3)) can be used to make predictions about the total carbohydrate content for the given levels of each factor. This equation should not be used to determine the relative impact of each factor because the coefficients are scaled to accommodate the units of each factor and the intercept is not the centre of the design space.The final equation in terms of actual factors generated by the software was expressed as follows:(3)Y=−198.35+0.29A+3.63B+0.21C−2.89x10−4AB−1.28x10−4AC−8.56x10−4BC−1.67x10−4A2−0.016B2+3.78ABC.


### 3.3. Analysis of Response Surface Plots

As shown in Figure1, the amount of total carbohydrate extracted from A. integer increased when the microwave power was increased from 150 W to 1230 W, indicating that higher microwave power led to higher extraction of carbohydrate.Figure 1
Response surface plot showing the effect of microwave power and extraction time on the total carbohydrate content.Microwave energy acts as a radiation that enhances the lysis of the cell wall. Electromagnetic energy is quickly transferred to the biomolecules, resulting in more power being dissipated inside the solvent, helping to generate molecular movement in the plant materials, and improving the extraction efficiency of polysaccharides at the same time [15]. However, the amount of total carbohydrate extracted from A. integer decreased slightly with the further increase in microwave power (above 1230 W). Higher microwave power provides unnecessary energy to the solvent and matrix and drastically disturbs molecular interactions. This disorderly molecular interaction structure as well as higher microwave power may lead to thermal degradation of the polysaccharides, hence the decrease in the amount of total carbohydrate extracted from A. integer [16]. Thus, the microwave power should not be too high or else it would be a waste of energy during extraction.The amount of total carbohydrate extracted fromA. integer increased when the extraction time was increased from 30 s to 150 s, indicating that longer extraction time led to a higher extraction rate of carbohydrate (Figure 2). However, further increase in extraction time decreased the extraction rate. The excessive time exposure in the microwave field may cause polysaccharide degradation [16]. Similar results were observed in the extraction of triterpenoid saponins from Ganoderma atrum [17] and extraction of polysaccharides from pumpkin [18].Figure 2
Response surface plot showing the effect of extraction time and solvent-sample ratio on the total carbohydrate content.In Figure3, the solvent to sample ratio affects significantly on the amount of total carbohydrate content extracted from A. integer. The extraction rate of carbohydrate increased rapidly when the solvent-to-sample ratio was increased. In this study, the volume of the solvent (deionised water) was fixed at 100 mL; thus, the increase in the solvent-sample ratio was also known as the increase in the amount of A. integer fibrous powder. Solvent (deionised water) can efficiently absorb microwave energy and enhance the swelling of bioactive compounds, which is favourable to increase the contact surface area between bioactive compounds and the solvent. Thus, the cell walls were ruptured, which resulted in easy release of carbohydrate into the surrounding medium [19].Figure 3
Response surface plot showing the effect of microwave power and solvent-sample ratio on the total carbohydrate content.


### 3.4. Verification of the Response Surface Model

To validate the reliability of the response surface model, a verification process was performed based on the desirability value generated by the software. Experiment of verification was conducted using the optimised parameters as follows: 1500 W microwave power, 180 s extraction time, and 1000 : 1 solvent-sample ratio (Table7). The experiment was conducted in triplicate.Table 7
Verification of model.
ItemValueA: microwave power1500 WB: extraction time180 sC: solvent-sample ratio1000 : 1Predicted carbohydrate concentration797.08 mg/LActual carbohydrate concentration787.49 mg/L% difference1.2%The extracted carbohydrate under predicted optimal conditions is 787.49 mg/L (Table7) with only 1.2% difference in comparison with the predicted value (797.08 mg/L). The result of the verification test agreed well with the predicted values.


#### 3.4.1. Determination of Degree of Polymerisation

The degree of polymerisation is the number of monosaccharide units in a polysaccharide. The degree of polymerisation was calculated using equation (4).
(4)Degreeofpolymerisation=totalcarbohydratecontentreducingsugarcontent.In the present study, the oligosaccharides extracted fromA. integer were having a DP of 16.1. The result indicated that A. integer extract has the potential to be considered as a candidate prebiotic since the DP value of the reported prebiotic was within the range of 10 to 200 [20]. Commercial prebiotics such as inulin have a unique range of degrees of polymerisation varying from 2 to 100. The length, composition, and polydispersity of prebiotics depend on the plant species, harvesting time, and extraction and postextraction processes [21].


### 3.5.In Vitro Digestion Studies

#### 3.5.1. Digestion by Gastric Juice

Table8 shows the percentage of hydrolysis of A. integer extract and inulin after gastric juice digestion at pH 1 to 4. The percentage levels of hydrolysis of A. integer extract after gastric juice digestion at pH 1, 2, 3, and 4 were 6.14%, 7.12%, 8.98%, and 10.23%, respectively, indicating the increase of the reducing sugar content at higher pH conditions. Inulin was used as a positive control in this study, and it was found to have lower gastric juice digestibility.Table 8
Percentage hydrolysis byA. integer and inulin after gastric juice digestion in various pH.
pH% hydrolysisA. integer extractInulin16.14±0.71a0.00±0.00a27.12±0.36ab0.72±0.01b38.98±0.71bc0.90±0.06c410.23±0.36c1.16±0.02dAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (Tukey test, p<0.05).Food was usually retained in the human stomach where gastric juice (pH 2 to 4) was released within 2 hours. Thus, whenA. integer extract was consumed, 90% of them were estimated to reach the intestine. Similar results were observed in gastric juice digestion of oligosaccharides from pitaya (dragon fruit) flesh, where 96% of pitaya oligosaccharides were expected to reach the intestine after human consumption [22]. The results of the present study indicated that A. integer has the potential to be used as prebiotics due to its ability to resist gastric juice digestion.


#### 3.5.2. Enzymatic Digestion

The enzyme used in the present study was human salivaryα-amylase. Human salivary α-amylase is an enzyme that catalyses the hydrolysis of α-glycosidic bonds of polysaccharide starch. When human salivary α-amylase reacts with starch, it cuts off the disaccharide maltose. As the reaction progresses, the amount of starch decreases while the amount of maltose increases [23]. The ability of A. integer extract and inulin to resist enzymatic digestion was determined based on the percentage of hydrolysis (Table 9). Percentage hydrolysis was calculated using equation (1).Table 9
Percentage hydrolysis ofA. integer and inulin after enzymatic digestion and absorption at pH 7.
% hydrolysisA. integer extract0.16±0.12aInulin0.09±0.04aAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (p<0.05).The percentage levels of hydrolysis ofA. integer extract and inulin after enzymatic digestion were 0.16% and 0.09%, respectively. Both A. integer and inulin showed a very low percentage of hydrolysis after enzymatic digestion, which indicated that they were resistant to enzymatic digestion and could reach the small intestine with less content loss.According to Johnson and Schmit [24], 30% of the carbohydrates consumed were digested by brush-border enzymes in the small intestine such as isomaltase, glucoamylase, maltase, sucrase, and lactase that hydrolyse α-1, 4- and α-1, 6-linked glucosaccharides. Therefore, it was estimated that at least 60% of A. integer extract consumed would reach the colon since some of them were hydrolysed by gastric juice (10%), by α-amylase (0.16%), and by brush-border enzymes in the small intestine (30%). The analysis showed that A. integer has the potential to be used as prebiotics due to its ability to resist enzymatic digestion.In the present study, inulin was found to have similar percentage of hydrolysis withA. integer extract. Based on the results, it was estimated at least 69% of inulin would reach the colon after hydrolysis by gastric juice (1.16%), by α-amylase (0.09%), and by brush-border enzymes in the small intestine (30%). Similar results were observed by the study conducted by Al-Sheraji, et al. [25], which reported maximum hydrolysis of inulin were 8.02% at pH 7, indicated that more than 60% of inulin reach the colon. According to the ileostomy patient model and intubation model performed by Cummings and Marfarlance [26], 88% of inulin and oligofructose would reach the colon after enzymatic digestion.


### 3.6. Fermentation ofA. integer Extract by Selected Bacterial Strains

Table10 shows the growth of L. acidophilus, L. casei, and E. coli in media containing A. integer extract and inulin (as positive control). L. acidophilus and L. casei are well recognised as probiotics that require the carbon source to grow actively. E. coli was selected in this study because it is one of the human gut pathogens.Table 10
Growth ofL. acidophilus, L. casei, and E. coli in media containing A. integer extract and inulin as the sole carbon source.
Time (hours)log10 CFU/mLL. acidophilusL. caseiE. coliExtractInulinExtractInulinExtractInulin02.46±0.20a2.31±0.25a2.94±0.08a2.98±0.08a2.79±0.02a2.45±0.17a246.49±0.25b6.02±0.07b5.36±0.06b5.48±0.20b9.09±0.02b9.11±0.12bc486.66±0.07b5.99±0.55b7.45±0.22c7.69±0.17c9.11±0.12b9.28±0.15b726.96±0.34b7.05±0.06c8.33±0.17d8.53±0.17d8.90±0.07c8.84±0.22cAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (Tukey test, p<0.05).Kolida and Gibson [20] indicated that increments of 0.5 to 1.0 log10 in bacterial colonies could be considered as a major shift in the gut microbiota towards a potentially healthier composition of the intestinal microbiota. The presence of the significant growth of L. acidophilus and L. casei in media containing A. integer extract indicated that both Lactobacillus strains were able to utilise them as carbon sources and thus conferred potential prebiotic characteristics on them. In addition, the A. integer extract had a similar effect to inulin on stimulating the growth of L. acidophilus and L. casei.BothA. integer extract and inulin were found to support the growth of E. coli at the earlier stage of the fermentation process. However, the growth of E. coli declined after 48 hours of fermentation, while both L. acidophilus and L. casei continuously grew up to 72 hours.Other reported studies have also demonstrated the utilisation of prebiotics by pathogenic bacteria, including the growth ofClostridia and Enterobacteria in arabinoxylan-substituted media [27], the growth of Clostridia in oligosaccharide-substituted media [28], and the growth of Salmonella in media containing Gigantochloa levis extract [29]. The possibility of these prebiotics utilised by pathogenic bacteria in vivo was highly probable based on in vitro studies. Furthermore, Shoaf et al. [30] stated that inulin inhibited the adherence of E. coli to the epithelial cell surface of tissue culture cells by 30 to 40%, which indicated that inulin does not always inhibit the growth of pathogenic bacteria.


## 3.1. Two-Level Full Factorial Design

In the present study, two-level FFD was first employed in the development of three response models, i.e.,A: microwave power, B: extraction time, and C: solvent-sample ratio, on the effect of total carbohydrate extracted (Y).In the Design-Expert® Software, the curvature test is placed in front of the ANOVA when centre points are included in the experimental design. The curvature test involves the randomisation of multiple centre points (replicates) throughout the other experimental conditions to get an adequate assessment of whether the actual values measured at this point match what is predicted by the linear model. If the curvature test is significant, a quadratic or higher-order model is needed to model the relationship between the factors and the response.As shown in Table4, the curvature test of FFD is significant with a p value less than 0.05. Therefore, a response surface model was used as augmentation. A face-centred central composite design (CCD) was chosen as the response surface model, which is comprised of different combinations of six axial points, as shown in Table 3.Table 4
ANOVA of two-level FFD.
SourceSum of squaresa (×105)dfbMean squarec (×105)F valuedp value, Prob>FeRemarkModel11.2471.605177.71<0.0001SignificantA: microwave power1.21611.216134.64<0.0001B: extraction time1.59811.598176.90<0.0001C: solvent-sample ratio3.91613.916433.47<0.0001AB1.31611.316145.67<0.0001AC1.06811.068118.19<0.0001BC0.93510.935103.49<0.0001ABC1.18911.189131.57<0.0001Curvature0.99810.998110.45<0.0001SignificantPure error0.090130.090Cor total12.32021aSum of the differences between the squared value of the average value and the overall mean. bDegree of freedom. cSum of squares divided by df. dRatio of the mean regression sum of squares divided by the mean error sum of squares. eProbability of seeing the observed F value if the null hypothesis is true.


## 3.2. Fitting the Central-Composite Design (CCD) Model

Table5 shows the results of ANOVA for the response surface reduced cubic model conducted at 95% confidence level (p=0.05). The significance of each coefficient of the model was determined using the F test and p value. The larger the F value and the smaller the p value, the more significant was the corresponding model term. The F value of 112.49 and p value that is less than 0.0001 implied the model was very significant. Besides, since the p value of “lack of fit” was 0.2170 (p>0.05), “lack of fit” was not significant. A not-significant “lack of fit” indicated that the model fits the actual experimental response data. The ANOVA results confirmed that the model was precise.Table 5
Response surface reduced cubic model for the total carbohydrate content.
SourceSum of squares (×105)dfMean square (×105)F valuep value, Prob>FRemarkBlock0.54310.543Model13.0591.450112.49<0.0001SignificantA: microwave power1.35411.354104.99<0.0001B: extraction time1.66511.665129.10<0.0001C: solvent-sample ratio4.23514.235328.46<0.0001AB1.31611.316102.05<0.0001AC1.06811.06882.80<0.0001BC0.93510.93572.50<0.0001A20.19010.19014.740.0013B20.26710.26720.670.0003ABC1.18911.18992.18<0.0001Residual0.219170.013Lack of fit0.07440.0191.670.2170Not significantPure error0.149130.011Cor total13.8227The results of regression ANOVA show that the overall mean and standard deviation developed in this model was234.36±35.91mg/L (Table 6). The percentage of coefficient of variation (CV %) was 15.32% which represents a minimum variation of data of the model. The coefficient of determination R2 of 0.9835 indicated an adequately high degree of correlation between experimental and predicted values of the total carbohydrate content. The 98.35% of variation that was observed in the response (total carbohydrate content) can be explained by the model. The difference between adjusted R2 (0.9603) and predicted R2 (0.9747) was less than 0.2, which indicated that the adjusted R2 was in reasonable agreement with the predicted R2. Based on the results, the model was suggested to be a good simulation of the extraction experiment.Table 6
Regression analysis of variance for total carbohydrate content.
SourceValueSDa35.91Mean234.39CV %b15.32PRESSc52712.06R20.9835AdjustedR20.9747PredictedR20.9603Adequate precision38.399aStandard deviation. bPercentage of coefficient of variation. cPredicted residual sum of squares.The equation in terms of coded factors (equation (2)) can be used to make predictions about the total carbohydrate content for given levels of each factor. The coded equation is useful for identifying the relative impact of the factors by comparing the factor coefficients. The relative impact of the factors can be observed through the factor coefficients by referring to the coded equation. The factor coefficient of C (153.39) is the highest among the three factors. Therefore, factor C had the highest impact on the total carbohydrate content. The positive factor coefficient refers to a positive effect and vice versa.The final equation in terms of coded factors generated by the software was expressed as follows:(2)Y=291.61+86.72A+96.17B+153.39C+90.69AB+81.69AC+76.44BC−75.91A2−89.91B2+86.19ABC.The equation in terms of actual factors (equation (3)) can be used to make predictions about the total carbohydrate content for the given levels of each factor. This equation should not be used to determine the relative impact of each factor because the coefficients are scaled to accommodate the units of each factor and the intercept is not the centre of the design space.The final equation in terms of actual factors generated by the software was expressed as follows:(3)Y=−198.35+0.29A+3.63B+0.21C−2.89x10−4AB−1.28x10−4AC−8.56x10−4BC−1.67x10−4A2−0.016B2+3.78ABC.


## 3.3. Analysis of Response Surface Plots

As shown in Figure1, the amount of total carbohydrate extracted from A. integer increased when the microwave power was increased from 150 W to 1230 W, indicating that higher microwave power led to higher extraction of carbohydrate.Figure 1
Response surface plot showing the effect of microwave power and extraction time on the total carbohydrate content.Microwave energy acts as a radiation that enhances the lysis of the cell wall. Electromagnetic energy is quickly transferred to the biomolecules, resulting in more power being dissipated inside the solvent, helping to generate molecular movement in the plant materials, and improving the extraction efficiency of polysaccharides at the same time [15]. However, the amount of total carbohydrate extracted from A. integer decreased slightly with the further increase in microwave power (above 1230 W). Higher microwave power provides unnecessary energy to the solvent and matrix and drastically disturbs molecular interactions. This disorderly molecular interaction structure as well as higher microwave power may lead to thermal degradation of the polysaccharides, hence the decrease in the amount of total carbohydrate extracted from A. integer [16]. Thus, the microwave power should not be too high or else it would be a waste of energy during extraction.The amount of total carbohydrate extracted fromA. integer increased when the extraction time was increased from 30 s to 150 s, indicating that longer extraction time led to a higher extraction rate of carbohydrate (Figure 2). However, further increase in extraction time decreased the extraction rate. The excessive time exposure in the microwave field may cause polysaccharide degradation [16]. Similar results were observed in the extraction of triterpenoid saponins from Ganoderma atrum [17] and extraction of polysaccharides from pumpkin [18].Figure 2
Response surface plot showing the effect of extraction time and solvent-sample ratio on the total carbohydrate content.In Figure3, the solvent to sample ratio affects significantly on the amount of total carbohydrate content extracted from A. integer. The extraction rate of carbohydrate increased rapidly when the solvent-to-sample ratio was increased. In this study, the volume of the solvent (deionised water) was fixed at 100 mL; thus, the increase in the solvent-sample ratio was also known as the increase in the amount of A. integer fibrous powder. Solvent (deionised water) can efficiently absorb microwave energy and enhance the swelling of bioactive compounds, which is favourable to increase the contact surface area between bioactive compounds and the solvent. Thus, the cell walls were ruptured, which resulted in easy release of carbohydrate into the surrounding medium [19].Figure 3
Response surface plot showing the effect of microwave power and solvent-sample ratio on the total carbohydrate content.


## 3.4. Verification of the Response Surface Model

To validate the reliability of the response surface model, a verification process was performed based on the desirability value generated by the software. Experiment of verification was conducted using the optimised parameters as follows: 1500 W microwave power, 180 s extraction time, and 1000 : 1 solvent-sample ratio (Table7). The experiment was conducted in triplicate.Table 7
Verification of model.
ItemValueA: microwave power1500 WB: extraction time180 sC: solvent-sample ratio1000 : 1Predicted carbohydrate concentration797.08 mg/LActual carbohydrate concentration787.49 mg/L% difference1.2%The extracted carbohydrate under predicted optimal conditions is 787.49 mg/L (Table7) with only 1.2% difference in comparison with the predicted value (797.08 mg/L). The result of the verification test agreed well with the predicted values.


### 3.4.1. Determination of Degree of Polymerisation

The degree of polymerisation is the number of monosaccharide units in a polysaccharide. The degree of polymerisation was calculated using equation (4).
(4)Degreeofpolymerisation=totalcarbohydratecontentreducingsugarcontent.In the present study, the oligosaccharides extracted fromA. integer were having a DP of 16.1. The result indicated that A. integer extract has the potential to be considered as a candidate prebiotic since the DP value of the reported prebiotic was within the range of 10 to 200 [20]. Commercial prebiotics such as inulin have a unique range of degrees of polymerisation varying from 2 to 100. The length, composition, and polydispersity of prebiotics depend on the plant species, harvesting time, and extraction and postextraction processes [21].


## 3.4.1. Determination of Degree of Polymerisation

The degree of polymerisation is the number of monosaccharide units in a polysaccharide. The degree of polymerisation was calculated using equation (4).
(4)Degreeofpolymerisation=totalcarbohydratecontentreducingsugarcontent.In the present study, the oligosaccharides extracted fromA. integer were having a DP of 16.1. The result indicated that A. integer extract has the potential to be considered as a candidate prebiotic since the DP value of the reported prebiotic was within the range of 10 to 200 [20]. Commercial prebiotics such as inulin have a unique range of degrees of polymerisation varying from 2 to 100. The length, composition, and polydispersity of prebiotics depend on the plant species, harvesting time, and extraction and postextraction processes [21].


## 3.5.In Vitro Digestion Studies

### 3.5.1. Digestion by Gastric Juice

Table8 shows the percentage of hydrolysis of A. integer extract and inulin after gastric juice digestion at pH 1 to 4. The percentage levels of hydrolysis of A. integer extract after gastric juice digestion at pH 1, 2, 3, and 4 were 6.14%, 7.12%, 8.98%, and 10.23%, respectively, indicating the increase of the reducing sugar content at higher pH conditions. Inulin was used as a positive control in this study, and it was found to have lower gastric juice digestibility.Table 8
Percentage hydrolysis byA. integer and inulin after gastric juice digestion in various pH.
pH% hydrolysisA. integer extractInulin16.14±0.71a0.00±0.00a27.12±0.36ab0.72±0.01b38.98±0.71bc0.90±0.06c410.23±0.36c1.16±0.02dAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (Tukey test, p<0.05).Food was usually retained in the human stomach where gastric juice (pH 2 to 4) was released within 2 hours. Thus, whenA. integer extract was consumed, 90% of them were estimated to reach the intestine. Similar results were observed in gastric juice digestion of oligosaccharides from pitaya (dragon fruit) flesh, where 96% of pitaya oligosaccharides were expected to reach the intestine after human consumption [22]. The results of the present study indicated that A. integer has the potential to be used as prebiotics due to its ability to resist gastric juice digestion.


### 3.5.2. Enzymatic Digestion

The enzyme used in the present study was human salivaryα-amylase. Human salivary α-amylase is an enzyme that catalyses the hydrolysis of α-glycosidic bonds of polysaccharide starch. When human salivary α-amylase reacts with starch, it cuts off the disaccharide maltose. As the reaction progresses, the amount of starch decreases while the amount of maltose increases [23]. The ability of A. integer extract and inulin to resist enzymatic digestion was determined based on the percentage of hydrolysis (Table 9). Percentage hydrolysis was calculated using equation (1).Table 9
Percentage hydrolysis ofA. integer and inulin after enzymatic digestion and absorption at pH 7.
% hydrolysisA. integer extract0.16±0.12aInulin0.09±0.04aAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (p<0.05).The percentage levels of hydrolysis ofA. integer extract and inulin after enzymatic digestion were 0.16% and 0.09%, respectively. Both A. integer and inulin showed a very low percentage of hydrolysis after enzymatic digestion, which indicated that they were resistant to enzymatic digestion and could reach the small intestine with less content loss.According to Johnson and Schmit [24], 30% of the carbohydrates consumed were digested by brush-border enzymes in the small intestine such as isomaltase, glucoamylase, maltase, sucrase, and lactase that hydrolyse α-1, 4- and α-1, 6-linked glucosaccharides. Therefore, it was estimated that at least 60% of A. integer extract consumed would reach the colon since some of them were hydrolysed by gastric juice (10%), by α-amylase (0.16%), and by brush-border enzymes in the small intestine (30%). The analysis showed that A. integer has the potential to be used as prebiotics due to its ability to resist enzymatic digestion.In the present study, inulin was found to have similar percentage of hydrolysis withA. integer extract. Based on the results, it was estimated at least 69% of inulin would reach the colon after hydrolysis by gastric juice (1.16%), by α-amylase (0.09%), and by brush-border enzymes in the small intestine (30%). Similar results were observed by the study conducted by Al-Sheraji, et al. [25], which reported maximum hydrolysis of inulin were 8.02% at pH 7, indicated that more than 60% of inulin reach the colon. According to the ileostomy patient model and intubation model performed by Cummings and Marfarlance [26], 88% of inulin and oligofructose would reach the colon after enzymatic digestion.


## 3.5.1. Digestion by Gastric Juice

Table8 shows the percentage of hydrolysis of A. integer extract and inulin after gastric juice digestion at pH 1 to 4. The percentage levels of hydrolysis of A. integer extract after gastric juice digestion at pH 1, 2, 3, and 4 were 6.14%, 7.12%, 8.98%, and 10.23%, respectively, indicating the increase of the reducing sugar content at higher pH conditions. Inulin was used as a positive control in this study, and it was found to have lower gastric juice digestibility.Table 8
Percentage hydrolysis byA. integer and inulin after gastric juice digestion in various pH.
pH% hydrolysisA. integer extractInulin16.14±0.71a0.00±0.00a27.12±0.36ab0.72±0.01b38.98±0.71bc0.90±0.06c410.23±0.36c1.16±0.02dAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (Tukey test, p<0.05).Food was usually retained in the human stomach where gastric juice (pH 2 to 4) was released within 2 hours. Thus, whenA. integer extract was consumed, 90% of them were estimated to reach the intestine. Similar results were observed in gastric juice digestion of oligosaccharides from pitaya (dragon fruit) flesh, where 96% of pitaya oligosaccharides were expected to reach the intestine after human consumption [22]. The results of the present study indicated that A. integer has the potential to be used as prebiotics due to its ability to resist gastric juice digestion.


## 3.5.2. Enzymatic Digestion

The enzyme used in the present study was human salivaryα-amylase. Human salivary α-amylase is an enzyme that catalyses the hydrolysis of α-glycosidic bonds of polysaccharide starch. When human salivary α-amylase reacts with starch, it cuts off the disaccharide maltose. As the reaction progresses, the amount of starch decreases while the amount of maltose increases [23]. The ability of A. integer extract and inulin to resist enzymatic digestion was determined based on the percentage of hydrolysis (Table 9). Percentage hydrolysis was calculated using equation (1).Table 9
Percentage hydrolysis ofA. integer and inulin after enzymatic digestion and absorption at pH 7.
% hydrolysisA. integer extract0.16±0.12aInulin0.09±0.04aAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (p<0.05).The percentage levels of hydrolysis ofA. integer extract and inulin after enzymatic digestion were 0.16% and 0.09%, respectively. Both A. integer and inulin showed a very low percentage of hydrolysis after enzymatic digestion, which indicated that they were resistant to enzymatic digestion and could reach the small intestine with less content loss.According to Johnson and Schmit [24], 30% of the carbohydrates consumed were digested by brush-border enzymes in the small intestine such as isomaltase, glucoamylase, maltase, sucrase, and lactase that hydrolyse α-1, 4- and α-1, 6-linked glucosaccharides. Therefore, it was estimated that at least 60% of A. integer extract consumed would reach the colon since some of them were hydrolysed by gastric juice (10%), by α-amylase (0.16%), and by brush-border enzymes in the small intestine (30%). The analysis showed that A. integer has the potential to be used as prebiotics due to its ability to resist enzymatic digestion.In the present study, inulin was found to have similar percentage of hydrolysis withA. integer extract. Based on the results, it was estimated at least 69% of inulin would reach the colon after hydrolysis by gastric juice (1.16%), by α-amylase (0.09%), and by brush-border enzymes in the small intestine (30%). Similar results were observed by the study conducted by Al-Sheraji, et al. [25], which reported maximum hydrolysis of inulin were 8.02% at pH 7, indicated that more than 60% of inulin reach the colon. According to the ileostomy patient model and intubation model performed by Cummings and Marfarlance [26], 88% of inulin and oligofructose would reach the colon after enzymatic digestion.


## 3.6. Fermentation ofA. integer Extract by Selected Bacterial Strains

Table10 shows the growth of L. acidophilus, L. casei, and E. coli in media containing A. integer extract and inulin (as positive control). L. acidophilus and L. casei are well recognised as probiotics that require the carbon source to grow actively. E. coli was selected in this study because it is one of the human gut pathogens.Table 10
Growth ofL. acidophilus, L. casei, and E. coli in media containing A. integer extract and inulin as the sole carbon source.
Time (hours)log10 CFU/mLL. acidophilusL. caseiE. coliExtractInulinExtractInulinExtractInulin02.46±0.20a2.31±0.25a2.94±0.08a2.98±0.08a2.79±0.02a2.45±0.17a246.49±0.25b6.02±0.07b5.36±0.06b5.48±0.20b9.09±0.02b9.11±0.12bc486.66±0.07b5.99±0.55b7.45±0.22c7.69±0.17c9.11±0.12b9.28±0.15b726.96±0.34b7.05±0.06c8.33±0.17d8.53±0.17d8.90±0.07c8.84±0.22cAll results are expressed asmean±standard deviation of three replicates. Results in the same column followed by different superscripts are significantly different (Tukey test, p<0.05).Kolida and Gibson [20] indicated that increments of 0.5 to 1.0 log10 in bacterial colonies could be considered as a major shift in the gut microbiota towards a potentially healthier composition of the intestinal microbiota. The presence of the significant growth of L. acidophilus and L. casei in media containing A. integer extract indicated that both Lactobacillus strains were able to utilise them as carbon sources and thus conferred potential prebiotic characteristics on them. In addition, the A. integer extract had a similar effect to inulin on stimulating the growth of L. acidophilus and L. casei.BothA. integer extract and inulin were found to support the growth of E. coli at the earlier stage of the fermentation process. However, the growth of E. coli declined after 48 hours of fermentation, while both L. acidophilus and L. casei continuously grew up to 72 hours.Other reported studies have also demonstrated the utilisation of prebiotics by pathogenic bacteria, including the growth ofClostridia and Enterobacteria in arabinoxylan-substituted media [27], the growth of Clostridia in oligosaccharide-substituted media [28], and the growth of Salmonella in media containing Gigantochloa levis extract [29]. The possibility of these prebiotics utilised by pathogenic bacteria in vivo was highly probable based on in vitro studies. Furthermore, Shoaf et al. [30] stated that inulin inhibited the adherence of E. coli to the epithelial cell surface of tissue culture cells by 30 to 40%, which indicated that inulin does not always inhibit the growth of pathogenic bacteria.


## 4. Conclusion

In summation,A. integer is one of the underutilised plant species providing promising potential which is not being capitalised upon. This study served as a starting point for A. integer to explore its great potential as a natural resource of prebiotics. A. integer extract showed prebiotic properties such as resistant to gastric juice and enzymatic digestion. Approximately 90% of the extract was estimated to reach the intestine after 4 hours of consumption based on the in vitro gastric juice digestion study. In addition, the A. integer extract was found to be resistant to enzymatic digestion with only 0.16% hydrolysis recorded at pH 7 through the in vitro digestion study. The A. integer extract was found to support the growth of probiotics such as L. acidophilus and L. casei. The results of the present study indicated that A. integer extract was comparable to the commercial prebiotics inulin. Therefore, A. integer extract has the potential to be considered as prebiotic materials and can be used as an ingredient to develop functional foods.



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*Source: 9940078-2021-07-21.xml*