Accepted Manuscript Changes in lycopene content and quality of tomato juice during thermal processing by a nanofluid heating medium
Seyyed Sajjad Jabari, Seid Mahdi Jafari, Danial Dehnad, Seyyed Ahmad Shahidi PII:
S0260-8774(18)30075-X
DOI:
10.1016/j.jfoodeng.2018.02.020
Reference:
JFOE 9175
To appear in:
Journal of Food Engineering
Received Date:
11 October 2017
Revised Date:
19 February 2018
Accepted Date:
21 February 2018
Please cite this article as: Seyyed Sajjad Jabari, Seid Mahdi Jafari, Danial Dehnad, Seyyed Ahmad Shahidi, Changes in lycopene content and quality of tomato juice during thermal processing by a nanofluid heating medium, Journal of Food Engineering (2018), doi: 10.1016/j.jfoodeng. 2018.02.020
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ACCEPTED MANUSCRIPT Changes in lycopene content and quality of tomato juice during thermal processing by a nanofluid heating medium
Running title: Nano-fluid thermal processing of tomato juice Seyyed Sajjad Jabari, Seid Mahdi Jafari, Danial Dehnad, Seyyed Ahmad Shahidi
Graphical Abstract:
Intelligent thermal/heating system for nanofluids (1) Insulated stainless steel shell and tube heat exchanger, (2) PT100 Sensors, (3) Nanofluid reservoir, (4) Food liquid reservoir, (5) Stainless steel centrifugal pump, (6) N700E vector inverter, (7) Digital contour, (8) PLC section
ACCEPTED MANUSCRIPT
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Changes in lycopene content and quality of tomato juice during thermal processing by a
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nanofluid heating medium
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Running title: Nano-fluid thermal processing of tomato juice Seyyed Sajjad Jabaria, Seid Mahdi Jafari*b, Danial Dehnadb, Seyyed Ahmad Shahidic
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a Young
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bDepartment
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Sciences and Natural Resources, Gorgan, Iran; Tel./fax: +98 17 324 26 432.
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cDepartment
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Researchers and Elite Club, Ayatollah Amoli Branch, Islamic Azad University, Amol, Iran of Food Materials and Process Design Engineering, Gorgan University of Agricultural of Food Science and Technology, Ayatollah Amoli Branch, Islamic Azad University,
Amol, Iran *Corresponding author:
[email protected]
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Abstract
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The main aim of this study was to evaluate the effects of shortening common thermal processing
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through nanofluids on quality of tomato juice for the first time. For this purpose, three different
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temperatures (between 70 and 90°C), nanoparticle concentrations (between 0 and 4%) and time
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(between 30 and 90 s) were selected for thermal processing of tomato juice in a shell and tube heat
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exchanger through central composite design. The findings indicated that while 4% nanoflluid at 30 °C
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for 30 s led to the best lycopene retention (96%) of tomato juice, hot water treatment (0% nanoparticle
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concentration) at 90 °C for 90 s resulted in the lowest lycopene retention (67%). The durations required
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for product to reach a certain temperature were dwindled and treated samples experienced lower color
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drops when higher nanoparticle concentrations were applied; a*/b* indices at 80°C were 1.7, 1.8 and
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1.9 for 0, 2 and 4% nanoparticles, respectively; indeed, higher nanoparticle concentration, and lower
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temperature and time led to higher lycopene retention and, as a consequence, higher a*/b* values. The
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effect of time on pH and acidity indices was not significant while temperature influenced those
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parameters significantly. Based on the indices considered, if temperature, concentration and time are
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set at 70°C, 4% and 30 s, the best responses will be obtained.
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Keywords: Nanofluids; Tomato juice; Heat exchanger; Nutritional properties. 1
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1. Introduction
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Tomato is the second most important produce around the world economically and planted in nearly all
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countries. Lycopene has the greatest contribution (around 83%) to the total pigments present in the
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tomatoes and is regarded as the most abundant carotenoid in this fruit (Shi et al., 1999). Besides, this
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pigment is the most important chemical compound in tomatoes, capable of neutralizing free radicals in
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human body with its antioxidant characteristics and preventing human being to be affected by cancer,
34
accelerated aging, cardiovascular diseases, osteoporosis, diabetes, and lots of other diseases (Basiri,
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2008). Considering above-mentioned points and high nutritional value of tomato, developing a
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technology capable of producing high quality product and accessible throughout the year in every
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condition is really beneficial (Jafari et al., 2017a). One of these suggested methods is thermal
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pasteurization used for long-term storage of fruit juices, especially tomato juice.
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Thermal processing of food products, in particular pasteurization of milk products, fruit juices,
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concentrates, and formulations, is one of operational units in the food industry, applied for
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improvement of their qualitative properties and extending their storage time. This process may be
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deployed for rapid heating of food products to at least 78°C. Although this processing is effective in
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inactivation of microorganisms and enzymes, it could be detrimental to the quality of fruit juices.
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During thermal processing, structural, and, in consequence, physical, chemical and biochemical
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changes in matrices of food products occur. If thermal processing is not applied rapidly or at
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reasonably minimal temperatures, fruit juices start to scatter in two phases due to pectin destruction
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(Goodman et al., 2002). So, today, one of the issues discussed in heat processing is the necessity of
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considerable increase in heat flux while minimizing heat transfer equipment required in the food
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industry.
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Because of issues above-mentioned, diverse methods have been applied for escalating heat transfer
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efficiency; however, all these methods were restricted on account of weak characteristics of
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conventional heat transfer fluids, e.g. water. In comparison with other fluids at larger dimensions than
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nano-scale, in particular micro scale, a remarkable raise in thermal conductivity is the most important
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effect observed for nano-scale fluids so that even at low concentrations of nanoparticles (1-5%v/v),
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thermal conductivity could be increased by more than 20% (Xuan and Li, 2003). Besides, nanofluids
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show high stability. Accordingly, nanofluids have attracted high attentions recently and a lot of
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researches have been carried out on this subject by now. Wen and Ding (2004) investigated the
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convective heat transfer of nanofluids (Al2O3 nanoparticles and de-ionized water) in the laminar flow
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regime. Their results showed a significant raise in convective heat transfer using the nanofluids, due to
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more thermal conduction, nanoparticles migration, and the consequent disturbance of the boundary
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layer. Nasiri et al. (2011) investigated heat transfer capacity of Al2O3/H2O and TiO2/H2O nanofluids
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through a circular channel for a turbulent flow mode. Based on their results, for any specific Peclet
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number, Nusselt number of nanofluids was higher than that of the base fluid and there was a direct
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relationship between the nanoparticle concentration and performance improvement for both nanofluids.
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However, heat transfer improvements for those nanofluids were similar. Our previous works on
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nanofluids thermal processing of fruit juices had been implemented for the first time in food products
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and it was shown that alumina could be a very good nanoparticle to be deployed for heat transfer
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purposes in other industries than common ones, including the food industry (Jafari et al., 2017b-e).
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In conclusion, the aim of this research was to intensify heat transfer efficiency in shell and tube heat
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exchangers, thereby retaining quality and nutritional properties, particularly lycopene content, of
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tomato juices during thermal processing more efficiently.
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2. Materials and methods
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2.1. Preparing the product
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Fresh tomatoes were purchased from a local fruit market (Gorgan, Iran) and stored at 3±1°C. At the
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appropriate time, they were crushed using a domestic juice extractor (MJ-W176P, Panasonic, Japan).
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The juice was filtered on a sterile double layer cheese cloth to remove seeds from the juice, and
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processed subsequently (Adekunte et al., 2010).
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2.2. Nano-fluid preparation
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Alumina nano-particles with 99% purity (US research nano-materials, Inc.) were purchased and
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dispersed with different volume concentrations of 0, 2 and 4% w/v in deionized distilled water. Then, it
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was stirred completely for an hour with a heater-stirrer at 1500 rpm in order to ensure nano-fluid
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stability (Jafari, et al., 2017b). No sedimentation was observed in the prepared nanofluid after 24 h. The
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details of nanoparticle properties are represented in Table 1. These alumina nano-particles were used in
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the heat exchanger as a part of the heating medium, but there was no direct contact between nanofluids
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and the product.
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Table 1
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2.3. Intelligent thermal processing system
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This system contains a shell and tube heat exchanger, two separate reservoirs, one for liquid food, and
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the other one equipped with a 1kw heater for heating the fluid (water or nano-fluid) and flow loop tubes
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for transferring the fluids from the reservoir to the heat exchanger, which means there is no contact
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between food and fluid throughout the system. Different parts of the intelligent thermal systems were
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shown in Fig. 1; complete descriptions of the equipment were represented by Jafari et al. (2017c) and
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Jafari et al. (2018a).
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Fig. 1. 4
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2.4. Lycopene determination
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5 mL of 95% ethanol, 5 mL 0.05% (w/v) of butylated hydroxytoluene in acetone, 10 mL of hexane and
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approximately 0.6 g of tomato juice were added to dark bottles. After 15 min stirring of the content
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with a magnetic stirrer (60F, FALC, Italy), 3 mL of deionized water was added to each bottle, and the
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bottles were shaken again for 5 min. A spectrophotometer (UV/VIS80, PG, UK) was used to analyze the
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upper hexane layer of each sample at 503 nm wavelength. Hexane was our blank sample. Finally,
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following equation was used to calculate lycopene content (Fish et al., 2002):
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Lycopene (mg/kg juice) =
A503 × 31.2
(1)
g juice
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Where 31.2 refers to the molar extinction coefficient, lycopene retention was calculated using equation
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(2):
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Retention (%) = mg lycopene/kg juice before treatment × 100
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2.5. Color analysis
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The samples were analyzed for a*/b* (red–green/ yellow–blue) color parameter using a chromameter
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(loviband CAM-System 500, Switzerland). This color index has been used in expressing color changes
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in commercial tomato products. The samples were placed on transparent plates and a few points were
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selected at random; the means were reported (Ganje et al., 2016).
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2.6. pH
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pH measurements were carried out using a digital pH meter (W3B, BEL, Italy) at room temperature.
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pH meter was calibrated using pH=7 and pH=4 buffers in advance. Three different points of each
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sample were selected and the mean values were reported (Jafari et al., 2018b).
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2.7. Acidity
mg lycopene/kg juice after treatment
5
(2)
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Acidity rate of tomato juices was measured by the potentiometric method (ISIRI, 2012). First, pH
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meter was calibrated with pH=7 and pH=4 buffers. Then, 50 mL of distilled water was boiled, cooled
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and displaced to a beaker. After that, 20 g of tomato juice was added and it was located on a heater
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stirrer. The probe of pH-meter was placed into the beaker. Both heater stirrer and pH meter were turned
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on. 0.1 N NaoH was added until pH of the tomato juice reached 8.1. Then, the volume of NaOH
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consumed was read and acidity was calculated by the following equation:
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𝐀=
123
where, V, M and A are volume of consumed 0.1 N NaOH (mL), weight of the sample (g), and total
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acidity in terms of citric acid (g/100g), respectively. 1 mL of 0.1 M NaOH is equivalent to 0.0064 g of
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citric acid.
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2.8. Statistical analysis
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Three different temperatures, nanoparticle concentrations and durations were selected to treat tomato
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juices (Table 2). To opt the best fitting models and for regression analysis, Design-Expert® 6.0.2
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software was applied. Selected methodology and design were Response Surface and Central
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Composite, respectively, which were used to survey the effects of variables on responses (p<0.05).
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Table 2
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3. Results and discussion
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3.1. Influence of nanofluids thermal processing on the lycopene content
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According to Table 3, all three factors had significant effects on lycopene content of tomato juices (p
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< 0.05). Untreated tomato juice had 46.7 mg/kg lycopene content; so, treatments No. 4 and 5, having
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the highest (45.0 mg/kg) and lowest (31.2 mg/kg) lycopene contents among all treated samples, led to
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lycopene retention percentages of 96.2 and 66.8%, respectively. Considering F values, temperature had
𝐕 × .𝟎𝟎𝟔𝟒 × 𝟏𝟎𝟎 𝐦
(3)
6
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the highest effect on this parameter (258.2); similarly, concentration had more considerable influence
139
on lycopene content than time, and higher lycopene content was maintained at higher nanoparticle
140
concentrations, due to more rapid heat transfer and lower processing time at this state. As a rule, higher
141
lycopene contents were caused by higher nanoparticle concentrations and lower temperature or time. In
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Fig. 2a, steeper slope of the graph on temperature side compared with time side hints deeper effect of
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temperature than time on this index, confirming the results of F value; lycopene content descended
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when temperature and time declined. As the Fig. 2a depicts, the highest lycopene content (42 mg/kg)
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was obtained at the lowest temperature and time; in contrast, the highest temperature and time led to
146
the lowest lycopene content (32 mg/kg).
147
Table 3
148
Fig. 2
149
The main reasons of lycopene destruction at higher temperatures are isomerization and oxidation
150
(Giovanelli and Paradiso, 2002). Besides, environmental factors including air, light and temperature
151
might change the influencing rates of these two processes on lycopene content of tomato products
152
(Anguelova and Warthesen, 2000). Goula and Adamopoulos (2006) reported that destruction of
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lycopene during thermal treatment of tomato products is affected by oxygen, light, humidity and
154
temperature; all of which are dependent on the temperature of the product.
155
However, light thermal treatment can retain lycopene content and improve its bioavailability due to
156
the release of chemical substances of plants from their matrices, facilitating lycopene extraction
157
(Gartner et al., 1997). Cis-isomers of lycopene intensify by increasing thermal time, the antioxidant
158
activity potentials of which are nearly twice those of β-carotene trans-isomers (Bohm et al., 2002).
159
D’Evoli et al. (2013) suggested that thermal processing and homogenization damage cellular
160
membrane and protein-carotenoid complexes, and make these carotenoids more available. 7
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3.2. Influence of nanofluids thermal processing on the color changes
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According to the Table 3, all the factors had significant effects on this response. As far as the F value is
163
concerned, temperature had the most considerable influence, with nanoparticle concentration and time
164
coming next, respectively. The a*/b* index for unprocessed tomato juices was 2.2; the highest and
165
lowest rates of this index were 2.2 and 1.5 for treatment numbers 4 and 5, respectively. Table 4
166
represents coefficients of the final model and different variables for that model; linear model was the
167
most appropriate factor for this index. Generally, lower temperatures and time, and higher nanoparticle
168
concentrations could improve a*/b* index. Figure 2b shows simultaneous effect of temperature and
169
concentration on the color. The highest color retention was relevant to the treatments with the highest
170
nanoparticle concentrations and lowest temperatures. In fact, higher concentrations caused the duration
171
needed to reach a given temperature to dwindle and those samples experienced lower color drops. For
172
example, a*/b* indices at 80°C were 1.7, 1.8 and 1.9 for 0, 2 and 4% nanoparticles, respectively;
173
indeed, the effect of concentration was really minimal in comparison with temperature. Color changes
174
in the graph during the temperature increase and color stability despite the concentration increase
175
illustrate their affecting types.
176
Table 4
177
The effect of each treatment on color changes could be attributed to its impact on lycopene content.
178
Indeed, those treatments which resulted in higher lycopene content, discussed in the previous section,
179
led to higher a*/b* values.
180
Our results suggested that higher temperatures decreased L* and a* values while increasing b*
181
value. Cortes et al. (2008) reported that thermal treatment at 90°C for 20 s intensified b* values of
182
processed orange juices, compared with raw orange juices, considerably. According to Lee and Coates
183
(2003), thermal treatment (90°C for 30 s) increased and decreased a* and b* values, respectively. 8
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Generally, color changes in food products during thermal processing are due to internal reactions
185
such as colorants destruction (especially carotenoids and chlorophylls), browning reactions, e.g.
186
Millard reactions with hexoses and amino acids, and ascorbic acid oxidation (Barreiro et al., 2000; Lee
187
and Coates, 1999; Lozano and Ibarz, 1997). So, final color parameters of the products could be used as
188
an index to evaluate quality loss due to thermal processing (Shin and Bhownik, 1995).
189
De Souza et al. (1999) reported L* and a* values are linked to lycopene content whereas b* values
190
have slight correlations with this index. Klim and Nagy (1988) reported that the reason of a decrease in
191
L* value during thermal treatment is formation of dark compounds by non-enzymatic browning,
192
resulting in a drop in desirability of fruit juices. In thermo-processed tomato juices, the probability of
193
enzymatic browning by enzyme activity of polyphenolase in oxygen presence is negligible in viewing
194
of application of heating throughout processing, inactivity of polyphenol oxidase enzyme and
195
deaeration, and ascorbic acid destruction most leads to the production of brown pigments through
196
anaerobic pathways (Porretta, 1991). Krebbers et al. (2003) and Shi and Le Maguer (2000) expressed
197
that low ratio of a*/b* represents orange to brown colors, the reasons of which are lycopene destruction
198
and Millard reaction through intense thermal operations. In fact, lycopene destruction is associated with
199
a decrease in L* and a* values of tomato juices.
200
3.3. Influence of nanofluids thermal processing on the acidity changes
201
As shown in Table 5, the effect of time on this index was not significant while temperature and
202
nanoparticle concentrations influenced it significantly. Acidity of unprocessed tomato juices was 0.421
203
mg/100g in terms of citric acid. Treatments No. 16 and 5 had the highest and lowest acidity rates with
204
0.42 and 0.35 mg/100g, respectively. The F values reveal that the effect of temperature was much
205
deeper than time and concentration on this index. For predicting the acidity, linear model was the most
206
appropriate model. Fig. 3a monitors simultaneous effect of temperature and concentration on acidity. 9
ACCEPTED MANUSCRIPT 207
The highest acidity belonged to the base fluid (water) at the lowest temperature, and the lowest acidity
208
to the 4% nanofluid at the highest temperature. As Fig. 3a indicates at low temperatures, a slight
209
reduction in acidity occurred when nanoparticle concentration decreased, attributed to longer time
210
needed at lower concentrations. Also, the slope of the graph clearly reveals the more profound effect of
211
temperature, compared with concentration, on this index.
212
Table 5
213
Fig. 3
214
Sherkat and Bor (1976) reported that escalating the temperature of hot break process from 64 to
215
104°C caused pH and acidity to raise and drop, respectively, probably due to rapid inactivation of
216
pectin esterase and polygalacturonase which hydrolyze pectic substances into pectic acid and
217
galacturonic acid, resulting in acidity decrease and pH increase. Edalatian et al. (2006) attributed high
218
acidity at low temperatures to production or increase in a series of organic acids during long time of
219
processing or storage; as an example, pyrrolidine carboxylic acid is produced during storage time.
220
Pectin breaking and producing miscellaneous acids were mentioned as other probable reasons.
221
3.4. Influence of nanofluids thermal processing on the pH values
222
Table 5 represents ANOVA results for pH changes in the products of different treatments. Only
223
significant factors were temperature and temperature-concentration. pH value for unprocessed tomato
224
juices was 4.4; the highest and lowest pH rates were 4.6 and 4.42 for treatments number 5 and 16,
225
respectively. It deserves to point out that the pH range of tomato juice after processing was narrow and
226
near to the pH value of unprocessed juice, indicating that natural pH value of tomato juice was
227
maintained through nanofluid thermal processing. Although nanoparticle concentration changes were
228
not effective on pH alterations, its interaction with temperature left significant effects on this index.
229
Linear effect of temperature had higher influence on pH rates than temperature-concentration with F
230
value of about 308.7. The latter issue could be recognized in the Fig. 3b in which the slope of graph is 10
ACCEPTED MANUSCRIPT 231
higher on temperature side than another side. The highest pH value was observed at the highest
232
temperature and lowest nanoparticle concentration in heating fluid; on the other hand, the least amount
233
was detected at the minimal concentration and temperature.
234
Our results of pH index were in correlation with acidity results; in other words, high acidities
235
accompanied by low pH values, and vice versa. pH drop at low temperatures could be ascribed to
236
microbial spoilage since microorganisms can ferment organic acids, reduce acidity and cause spoilage
237
in fruit juices simultaneously (Sodeko et al., 1987). Nevertheless, pH values were not impacted by
238
thermal treatments substantially, moving in the range of 4.4-4.6. Similarly, Elez-Martinez et al. (2006)
239
reported that thermal processing (at 90°C for 1 min) had minimal effects on physical properties
240
including pH and total soluble solids of orange juices. In the same way, Yeom et al. (2000) observed
241
that pH and total solids of orange juices were not affected by thermal processing at 94.6°C for 30 s.
242
Similar parallel studies confirmed our results as some indicators of food products, i.e. pH of
243
watermelon juice and TSS of tomato juice, were not impacted by nanofluids thermal processing
244
substantially (Jafari et al., 2017b,d).
245
3.5. Influence of nanofluids thermal processing on the process time
246
Both nanofluids and treated tomato juice through them reached the maximal temperature earlier than
247
base fluids and tomato juice treated by them when the pump turned on. A substantial reduction in
248
processing time could be observed from 54 min for hot water processing to 42 and 29% for 2 and 4%
249
nanofluids processing, respectively. Indeed, 22.2 and 46.3% drop in duration of thermal processing
250
were achieved when hot water was replaced with alumina nanofluids. In general, both temperature of
251
pasteurization and duration required for it were shortened by half when nanofluids, compared with
252
water, were applied.
253 254
Inherent properties of nanofluids and their impacts on thermal properties are responsible for reduction of processing times by nanofluids. The improvement in conductive heat transfer coefficient 11
ACCEPTED MANUSCRIPT 255
of nanofluids is due to the growth of their thermal conductivity, turbulence strengthening, Brownian
256
motion of spherical nanoalumina, cessation of boundary layer growth, homogenous dispersion of
257
suspended particles and their disordered shifting (Choudhury et al., 2014; Keblinski et al., 2002).
258
3.6. Modelling and optimization procedure
259
Optimization targets were defined as lycopene to be preserved at its maximum values, color values to
260
remain at higher rates than 1.8, and acidity and pH to be maintained in their conventional ranges.
261
Considering these conditions, provided that temperature, concentration and time are set at 70°C, 4%
262
and 30 s, overall desirability of 95% could be attained.
263
4. Conclusion
264
The highest lycopene content (45 mg/kg) in treated tomato juice were achieved when higher
265
nanoparticle levels and lower temperature or time during thermal processing were applied. Based on F
266
values obtained from ANOVA Tables, the impact of independent variables on color parameters (a*/b*
267
value) of tomato juice treated by nanofluids was in this order: temperature, nanoparticle concentration
268
and time. Our results suggested that increasing temperature decreased a* values while increasing b*
269
value. Concentration of nanoparticles did not change the original pH and acidity values of tomato juice
270
significantly, but higher lycopene content of tomato was maintained in treated tomato juice after
271
nanofluid processing compared with common thermal processing (with hot water). Linear models
272
could successfully fit the data related to changes in each response at different levels of independent
273
variables. For the first time, these results propose that quality of tomato juice could be improved if
274
nanofluid thermal technology is substituted for traditional thermal processing. Our future works include
275
application of this system for other sensitive food products (especially with microbial hazards e.g. milk
276
products); also, sensory analyses will be carried out to examine recognition of changes by consumers as
277
a step toward industrialization of nanofluids.
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Acknowledgment 12
ACCEPTED MANUSCRIPT 279
It is necessary to appreciate Iran National Science Foundation (INSF) for the financial support.
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ACCEPTED MANUSCRIPT Fig. 1. Intelligent thermal/heating system for nanofluids Fig. 2. Simultaneous effect of (a) temperature –time on lycopene changes and (b) temperature – concentration on color changes of treated tomato juices Fig. 3. Simultaneous effect of temperature –concentration on changes in (a) acidity and (b) pH values of treated tomato juice through nanofluids
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Fig. 1 Intelligent thermal/heating system for nanofluids (1) Insulated stainless steel shell and tube heat exchanger, (2) PT100 Sensors, (3) Nanofluid reservoir, (4) Food liquid reservoir, (5) Stainless steel centrifugal pump, (6) N700E vector inverter, (7) Digital contour, (8) PLC section
1
ACCEPTED MANUSCRIPT
(a)
(b) Fig. 2 Simultaneous effect of (a) temperature –time on lycopene changes and (b) temperature – concentration on color changes of treated tomato juices
2
ACCEPTED MANUSCRIPT
(a)
(b) Fig. 3 Simultaneous effect of temperature –concentration on changes in (a) acidity and (b) pH values of treated tomato juice through nanofluids
3
ACCEPTED MANUSCRIPT Highlights:
The main goal was thermal processing of tomato juice by nanofluids.
4% nanoflluid at 30°C for 30 s resulted in 96% lycopene retention.
Higher nanoparticle concentrations reduced the time needed for the process.
Nanofluid processing retained the natural pH, acidity and color of product.
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Table 1 Thermophysical properties of alumina nanoparticles used in this research Properties
Description
Average nanoparticle diameter (nm)
20
Density (kg m-3)
3890
Heat capacity (J kg-1 K-1)
880
Thermal conductivity (W m-1 K-1)
36
Base fluid
Water
Morphology
Nearly spherical
1
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Table 2 Design of experiments by central composite design for tomato juices treated by nanofluids at different concentrations, temperatures and time Number of treatment
Time (sec)
Temperature (°C)
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20
90 90 60 30 90 60 90 90 60 60 60 60 30 30 60 30 60 60 30 60
90 70 80 70 90 80 80 70 80 70 80 80 80 90 80 70 90 80 90 90
2
Nanoparticle concentration (%) 4 0 4 4 0 2 2 4 2 2 2 0 2 0 2 0 2 0 4 2
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Table 3 ANOVA data for changes in lycopene content and color (a*/b*) parameter of tomato juice induced by thermal processing through nanofluids Property of
Source
Sum of Squares
DF
Mean Square
F Value
Prob>F
Model
1.74
3
0.58
99.2
< 0.0001
x1
0.047
1
0.047
8.1
0.0117
x2
1.51
1
1.51
258.18
< 0.0001
x3
0.18
1
0.18
31.33
< 0.0001
Residual
0.093
16
5.83E-03
Lack-of-Fit
0.076
11
6.93E-03
2.03
0.2243
Pure Error
0.017
5
3.41E-03
Model
0.62
3
0.21
160.27
< 0.0001
x1
0.027
1
0.027
20.93
0.0003
x2
0.56
1
0.56
432.8
< 0.0001
x3
0.035
1
0.035
27.1
< 0.0001
Residual
0.021
16
1.29E-03
Lack-of-Fit
0.019
11
1.69E-03
4.05
0.0671
Pure Error
2.08E-03
5
4.16E-04
tomato juice Lycopene
a*/b* Value
3
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Table 4 Model coefficients and statistics indices of content changes induced by thermal processing through nanofluids Variable
Model
R2
Pred R2
SD
Lycopene content (mg/100gr)
9.18-0.002x1-0.038x2+0.067x3
0.94
0.91
0.0760
Color (a*/b*)
3.75-1.73x1-0.023x2+0.029x3
0.96
0.94
0.0360
0.62+0.002x1-0.00029x2-0.00017x3
0.91
0.81
0.0007
7.67x2-8.127 x2x3
0.96
0.85
0.0120
Acidity (mg/100gr) pH
4
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Table 5 ANOVA data for changes in acidity and pH values of tomato juice induced by thermal processing through nanofluids Property of tomato juice Acidity
pH
Source
Sum of Squares
DF
Mean Square
F Value
Prob>F
Model
8.88E-03
3
2.96E-03
54.42
< 0.0001
x1
3.60E-06
1
3.60E-06
0.066
0.8003
x2
8.76E-03
1
8.76E-03
161.06
< 0.0001
x3
1.16E-04
1
1.16E-04
2.13
0.046
Residual
8.70E-04
16
5.44E-05
Lack-of-Fit
7.39E-04
11
6.72E-05
2.56
0.155
Pure Error
1.31E-04
5
2.63E-05
0.049
6
8.12E-03
54.19
< 0.0001
x1
4.00E-05
1
4.00E-05
0.27
0.614
x2
0.046
1
0.046
308.66
< 0.0001
x3
9.00E-05
1
9.00E-05
0.6
0.4522
x1x2
1.13E-04
1
1.13E-04
0.75
0.4019
x1x3
1.13E-04
1
1.13E-04
0.75
0.4019
x2x3
2.11E-03
1
2.11E-03
14.1
0.0024
Residual
1.95E-03
13
1.50E-04
Lack-of-Fit
1.41E-03
8
1.77E-04
1.66
0.2996
Pure Error
5.33E-04
5
1.07E-04
Model
5