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Optimization of polyphenols extraction from pomegranate peels –
drying, enzymatic pretreatment, extraction method, operating conditions
1Department of Chemical Engineering, School of Engineering, Aristotle University, 541 24 Thessaloniki,
Greece
2Department of Food Science and Technology, School of Agriculture, Forestry and Natural Environment,
Aristotle University, 541 24 Thessaloniki, Greece
L. Papaoikonomou1, K. Kaderides2, A.M. Goula2, K.G. Adamopoulos1
Introduction
Pomegranate
(Punica Granatum L.)
Usually cultivated in Mediterranean
climate (Spain, Turkey), many varieties
(Wonderful, Berri etc.)
Healing and medical properties, important
source of antioxidants
24% Peel 14% Seeds 62% Juice
ComponentContent
(g/100 g dry peel)
Total solids 94.50
Moisture 5.40
Total sugars 17.70
Protein 4.90
Fat 1.26
(Aguilar et al., 2008)
Composition of Pomegranate Peels
Phenolic
fraction
Content
(mg/g dry matter)Reference
Punicalagin 16.67-64.98 Li et al., 2015; Gullon et al., 2016
Ellagic acid 0.44-2.83Fisher et al., 2011;
Rowashed et al., 2013; Li et al., 2015
Caffeic acid 0.60 Rowashed et al., 2013
P-coumaric acid 0.18 Rowashed et al., 2013
Catechin 8.68-12.65 Rowashed et al., 2013; Li et al 2015
Cyanidin 0.22 Fisher et al., 2011
Pelargonidin 0.20 Fisher et al., 2011
Gallic acid 12.58-25.90Fisher et al., 2011;
Rowashed et al., 2013; Li et al., 2015
Total phenolics 49.00-181.00Al-Rawahi et al., 2013; Amani et al.,
2014; Kaderides et al., 2015
Biological Activity
Phenolic
compounds
Antioxidant activity (Cam et al., 2009)
Anticancer properties (Hamad & Al-Momene, 2009)
Reduce risk of coronary heart disease (Aviram et al., 2000)
Antimicrobial activity (Duman et al., 2009)
Methods of Phenolics Extraction from Pomegranate Peels
Technique of
extraction
Time
(min)
Yield
(g GAΕ/100 g dry matter) Reference
Normal Stirring 60 8.26 – 11.9Wang et al., 2011;
Pan et al., 2011
Pressurized liquid 15 25.8 – 26.4 Cam & Hisil, 2010
Ultrasound-assisted
(Continuous)
(Pulsed)
6
8
14.8
14.5
Pan et al., 2011
Microwave-assisted 1 21.5 Zheng et al., 2011
New ‘‘green’’ techniques – use less solvent and energy
Ultrasound-assisted Microwave-assisted
Objectives
To compare new methods for extraction of
phenolic compounds from pomegranate peels
• Microwave-assisted extraction
• Ultrasound-assisted extraction
To study the effect of peels moisture content on
extraction yield
To study the enhancement of the optimum
extraction treatment by enzymatic pre-treatment
To study the drying behavior of pomegranate peels
and the kinetics of total phenolics degradation
during the drying process
To propose an
optimum method
for isolation of
priced compounds
from pomegranate
peels
Materials and Methods
Washing
Microwave assisted extraction
Ultrasound assisted extraction
FiltrationFolin Ciocalteu
method
Determination of phenolic compounds
Pomegranate peels
Drying (40 οC, 48h) Grinding-Sieving
Process for Extraction of Phenolics from Pomegranate Peels
Sieving
Sieving of Peel Powder
Microwave-assisted Extraction
Microwave system (Multiwave B30MC030A)
(Anton Paar, Austria)
Parameters Levels
Solvent type (S) Water50% aqueous
EtOH
70% aqueous
EtOH
50% aqueous
MeOH
70% aqueous
MeOH
Power (W) 100 201 350 499 600
Liquid/solids ratio (LS, mL/g) 10 20 35 50 60
Experiment Design - Response Surface Methodology
Parameters
Extraction time
Microwave radiation power
Solvent type
Liquid/solids ratio
130 W, 20 kHz VCX-130 Sonics and Materials
(Danbury, CT, USA), Ti–Al–V probe (13 mm)
Extraction temperature
Solvent type
Liquid/solids ratio
Amplitude level
Pulse duration/pulse interval ratio
Extraction time
Parameters Levels
Solvent type (S) EtOH MeOH Water 50% aqueous
MeOH
Ethyl-
acetate
Extraction temperature (T, oC) 25 30 35 40 45
Liquid/solids ratio (LP, mL/g) 10/1 20/1 30/1 40/1 50/1
Amplitude level (A, %) 20 30 40 50 60
Pulse duration/pulse interval ratio (PULSE, -) 5/15 3/4 7/6 19/12 2/1
Experiment Design - Response Surface Methodology
Parameters
Ultrasound-assisted Extraction
Effect of Peels Moisture Content on Extraction Yield
Peels
Drying (40 oC)
at different
moisture contents
Ultrasound-assisted extraction
at the optimum conditions
Microwave-assisted extraction
at the optimum conditionsGrinding
0
20
40
60
80
100
120
140
0 10 20 30 40 50 60 70Yie
ld (
mg G
AE
/g d
ry
pee
l)
Peels moisture content (%)
Enzymatic Pre-treatment at the Optimum Conditions
Time of pre-treatment (min)
Enzyme concentration (% of dry matter)
Pectinase/Cellulase ratio
Liquid/solids ratio (mL/g)
Time (min) : 60 105 150 195 240
Enzyme concentration (% of dry matter) : 2 2.5 3 3.5 4
Pectinase/Cellulase ratio (% pectinase) : 0 25 50 75 100
Liquid/solids ratio (mL/g) : 20/10 30/10 40/10 50/10 60/10
Experiment Design - Response Surface Methodology
pH = 4.5-5.0
T = 50±2 oC
Parameters
Pomegranate Peels Drying
Pomegranate peels, with 75.28 ± 1.08% moisture
content, were used for all drying experiments
Pomegranate peels slabs of 6 mm thickness
30 x 19 cm aluminum dishes
In a tray dryer with an air velocity of 1.2 m/s
Five drying temperatures: 40, 50, 60, 70, 80 oC
At regular intervals, determination of:
The weight of the samples
The total phenolics content
2
2
2 4
8lnln
L
Dtπ
πMR
MR : moisture ratio
X0 : initial moisture content
X : moisture content at time t
Xe : equilibrium moisture content
L : slab thickness
Simplification for long drying periods
Kinetic Modeling of Drying
12
22
22
0 4
12exp
12
18
ne
e
L
Dtπn
nπXX
XXMR
y = -0.0039x - 0.0827
R² = 0.991
-3,0
-2,5
-2,0
-1,5
-1,0
-0,5
0,0
0 100 200 300 400 500 600 700 800
lnM
R
t (min)
lnMRexp.
Linear (lnMRexp.)
- Mechanistic model
Diffusion approach
ko : frequency factor
Ea : activation energy
X : peels moisture content
T : drying temperature
A1, A2, A3 : constants
t
TR
aE
tXAXAek
o
eC
C0
23210 dA
First order kinetic model for thermal degradation
of phenolic compounds during drying
Results
Microwave Extraction – Effects of Studied Factors
Nmax
Power : 499 W
S : 70% EtOH
L/S : 50/1 mL/g
5
5,5
6
6,5
7
7,5
8
8,5
9
9,5
0 4 8 12 16 20
Ex
trac
tion
yie
ld (
%)
Extraction time (min)
Optimum extraction time
4 min
Regression analysisDetermination of
statistically significant factors
Empirical modelling of
extraction yield
Y = 20.4395 – 0.0428 ∙ P
+ 0.0001 ∙ P2 + 0.7630 ∙ S2
– 0.0059 ∙ P∙S + 0.0003 ∙ P∙LP
R2 = 0.78
Microwave Extraction - Optimization
Y: g GAΕ/100 g
Statistically significant parameters:
Power (p = 0.002), Power2 (p = 0.044)
257.6
mg GAE/g dry peel
Ultrasound Extraction – Effects of Studied Factors
0
1
2
3
4
5
6
7
0 10 20 30 40 50 60 70
Extr
acti
on y
ield
(g G
AE
/100 g
)
Extraction time, t (min)
water, LP=20/1, A=40%, PUL=7/6, T=25oC
ethanol, LP=20/1, A =40%, PUL=7/6, T=25oC
methanol, LP=20/1, A=40%, PUL=7/6, T=25oC
Νmax
T : 35 ⁰C
A : 40%
PUL : 1.2
LP : 35/10
2
4
6
8
10
methanol ethyl acetate water ethanol 50% aqueous
methanol
Extr
acti
on
yie
ld
(g G
AE
/100 g
)
N: g GAΕ/100 g
Ultrasound Extraction - Optimization
R2 = 0.61
Statistically significant parameters: LP2 (p = 0.039), S2 (p = 0.020)
-2 : MeOH
-1 : Ethylacetate
0 : Water
1 : EtOH
2 : 50% aqueous MeOH
Y = - 88.056 + 3.417∙T + 1.197∙LP + 21.161∙PULSE - 0.048∙T2
– 0.018∙LP2 – 2.129∙S2 – 8.357∙PULSE2 + 0.041∙LP∙SY: g GAΕ/100 g
111.9
mg GAE/g dry peel
0
20
40
60
80
100
120
140
0 10 20 30 40 50 60 70 80
Ex
trac
tio
n y
ield
(m
g /
g d
ry p
eel)
Peels moisture content (% w.b.)
Microwave
Assisted
Extraction
Ultrasound
Assisted
Extraction
14 45
Effect of Peels Moisture Content on Extraction Yield
Enzymatic Pre-treatment - Microwave Assisted Extraction
Power = 600 W, Solvent/peels ratio = 60/1 mL/g, Extraction time = 4 min
Solvent = 50% aqueous EtOH, Peels moisture content = 45% w.b.
Optimum yield: 172.8 mg GAE/g dry peel
Pre-treatment time = 240 min
Enzyme concentration = 2% of dry matter
Enzyme type = 100% pectinase
Liquid/solids ratio = 20/10 mL/g
Enzymatic Pre-treatment-Ultrasound Assisted Extraction
Solvent = water, Solvent/peels ratio = 32.2/1 mL/g, amplitude level = 39.8%,
Pulse duration/pulse interval = 1.2, temperature = 34.7 oC, extraction time = 10 min
87.1 mg GAE/g dry peel
Pomegranate Peels Drying Behavior
0
10
20
30
40
50
60
70
80
0 200 400 600
Mois
ture
(%
w.b
.)
Drying time (min)
40
50
60
70
80
Drying temperature (oC)
The drying rate increased on
increasing the temperature
The drying occurred mostly in
the falling rate period
The controlling resistance to
mass transfer was internal
diffusion of moisture
0
10
20
30
40
50
60
70
80
0 1000 2000 3000
Mo
istu
re (
% w
.b.)
Drying time (min)
40
50
60
70
80
Drying
temperature (oC)
y = -3401.6x – 12.07
R² = 0.929
-23,2
-23,0
-22,8
-22,6
-22,4
-22,2
-22,0
-21,8
-21,6
-21,4
0,0028 0,0029 0,0030 0,0031 0,0032 0,0033
lnD
eff
(Def
fin
m2/s
)
1/T (K-1)
𝐃 = 𝐃𝟎𝐞𝐱𝐩(−𝐄𝐚𝐑𝐓
)
Pomegranate Peels Drying Behavior
Kinetics of Total Phenolics Degradation
• Higher temperatures caused more loss of
phenolics
• Drying of pomegranate peel can result in
significant phenolics degradation
Parameter Value
ko (min-1) 21.6∙10-5
Ea (kJ/mol) 15.8
A1 4084.5
A2 1932.3
A3 -58.4
R2 SSE
0.846 0.16
t
TR
aE
tXAXAek
o
eC
C0
23210 dA
0,0
0,2
0,4
0,6
0,8
1,0
1,2
1,4
0 200 400 600 800 1000 1200 1400
C/C
o
Drying time (min)
4050607080
Temperature (oC)
0,0
0,2
0,4
0,6
0,8
1,0
0,0 0,2 0,4 0,6 0,8 1,0
C/C
o -
exp
erim
enta
l
C/Co - predicted
40 oC50 oC60 oC70 oC80 oC
Conclusions
The optimum extraction yield by microwave extraction was 257.6 g
GAE/g dry peel at 600 W, 50% EtOH as solvent, liquid/solid ratio of
60/1 mL/g and extraction time of 4 min.
The optimum extraction yield by ultrasound extraction was 111.8 g
GAE/g dry peel at 34.7 οC, water as solvent, liquid/solid ratio of 32.2/1
mL/g, amplitude level up to 39.8%, pulse duration/pulse interval ratio of
7/6 and extraction time of 10 min.
The optimum moisture content in order to maximize the extraction
yield was 45% w.b. for the microwave extraction and 14% w.b. for the
ultrasound extraction.
The enzymatic pre-treatment using cellulase and pectinase did not
enhance the extraction.
Conclusions
The drying rate increased on increasing the temperature, whereas the
drying occurred mostly in the falling rate period.
The effective diffusivity values varied between 7.12∙10-9 and 2.68∙10-8
m2/s and the activation energy was found to be 28.28 kJ/mol.
Phenolics content of pomegranate peel decreased by 60-75% after
drying at 40-80 oC and higher temperatures caused more loss of
phenolic substance.
The degradation of phenolics during drying can be described by a 1st
order kinetic model.
Conclusions
Thank you
for your attention!