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Clarification of cashew apple juice by crossflow microfiltration: foulant fractions and interest of filterability tests

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ROSSFLOW

microfiltration (CMF) is more and more used for juices clarification and

sterilization. If this process presents many advantages (e.g. cold

operating conditions), the membrane fouling can limit considerably the

permeate flux during clarification operation. The objective of this study is first

to determine the main foulant fractions of cashew apple juice and then to

implement tests of filterability in order to predict the filtration performance during

filtration running’s.

Doudjo SORO

1,2

, Michèle DELALONDE

2

,

Christelle WISNIEWSKI

2

, Manuel DORNIER

2

1LAPISEN, Institut National Polytechnique Félix

Houphouët-Boigny (INP-HB), BP 1313 Yamoussoukro, Côte d’Ivoire

2 CIRAD, Univ. Montpellier 1, Montpellier SupAgro,

UMR Qualisud TA B-95/16, 73 rue J.-F. Breton 34398 Montpellier Cedex 5, France

C o n c e p ti o n : C IR A D , M ar t in e D up ort al , O c to b e r 2 0 1 2 — p h o to s © D . S o ro

Raw material: yellow and red cashew apples from Yamoussoukro (Côte d’Ivoire).

Crossflow microfiltration trials: 4 tubular ceramic membranes (55 cm2, 0.2 µm),

U = 6 m.s-1, T= 35 ± 2°C, TMP = 2 bar.

Three juices used to evaluate the foulant fraction (fig. 1).

Filterability tests:

• Specific resistance of filtration (SRF) with Amicon cell: cellulose acetate membrane, 0.2 µm, agitation, T= 35 ± 2°C, P = 2 bar.

• Capillary suction time (CST): CST-meter, Triton type 319 Multi-CST (Triton Electronics Limited); T= 35 ± 2°C.

All tannins, suspended insoluble solids and alcohols insoluble solids (mainly polysaccharides) were totally retained by the membrane. Sugars, ascorbic and other acids were preserved in the permeate (table I).

C

rossflow microfiltration can be used to clarify cashew apple juice (reduction of tannins and so

astringency). The main foulant substances seem to be colloids (54% of the fouling resistance). The

filtration performances cannot be predicted by filterability tests like CST or SFR. New filterability test has

to be developed. Further study is needed in order to better understand the fouling phenomena.

R

esults and discussion

C

onclusion

contact: manuel.dornier@supagro.inra.fr

M

aterials and methods

EFFoST Annual Conference

20-23 November 2012

Montpellier, France

1 nm 1 nm 1 nm 1 mm 1 µm 1 µm 100 µm 100 µm Solutes and Macromolecules Solutes and Macromolecules Solutes and Macromolecules Colloids Colloids Supra

colloids particlesSettled

Supra-colloids Juice extracted by a screw press Whole juice dacanted 12 h (4°C) Whole juice treated by CMF

(0.2 µm; 2 bar; 6 m.s-2; 35°C)

Whole juice

Decanted juice

Microfiltered juice

Ma

Juices Whole Decanted Microfiltered

pH 4.05 3.90 4.06

Titratable Acidity (g malic acid.kg-1) 29.4 26.1 26.6

Total Soluble Solids (g.kg-1) 52 56 56

Suspended insoluble solids (g.kg-1) 7.8 3.3 0

Tannins (g.kg-1) 23.1 2.1 0

Alcohols insoluble solids (g.kg-1) 3.8 0.3 0

Viscosity at 35°C (mPa.s-1) 1.2 1.1 1.1 Turbidity (NTU) 8 033 233 6 Ascorbic acid C (g.kg-1) 15.0 14.2 14.1 0 40 80 120 160 200 1 2 3 4 5 6 7 8 VRR Whole juice Decanted juice Microfiltered juice J p (L .h -1 .m -2 ) ** * * 0 2 4 6 8 10 12

Whole juice Decanted juice Microfiltered juice

CS T (s ) * ** *** 0 40 80 120

Whole juice Decanted juice Microfiltered juice

SR F (k g. m -1 )X 10 12 Rsoluble 37% Rinsoluble 9% Rcolloids 54%

No correlation between the filtration

performances and conventional filterability tests

The resistance in serial model was used to evaluate the contribution of the different foulant fractions (eq.1). We demonstrated the major role of

the colloidal fraction of cashew apple juice in membrane fouling (fig. 5). Rm: the membrane resistance (m-1); Rf: the fouling

resistance (m-1) ;µµµ: dynamic viscosity of the permeate (Pa.s)

Rf: TMP – Rm and Rf = Rsoluble + R colloids = Rinsoluble (eq. 1)

µxJp

Figure 2. Permeate flux (Jp) vs. volume

reduction ratio (VRR) for the cashew apple juices. Figure 3.with the different cashew apple juices.Capillary suction time obtained obtained with the different cashew apple juices.Figure 4. Specific resistance of filtration

Figure 5. Contribution of the different foulant fractions to the total hydraulic resistance during

CMF of the cashew apple juices (VRR 8).

Figure 1. The three types of juices treated.

Filterability tests:

• According CMF: whole juice = decanted juice < microfiltered juice (fig. 2). • According CST: microfiltered juice = decanted juice < whole juice (fig. 3). • According SRF: decanted juice > microfiltered Juice > whole juice (fig. 4).

Table I. Main characteristics of cashew apple juice.

Clarification of Cashew Apple Juice by Crossflow Microfiltration:

Foulant Fractions and Interest of Filterability Tests

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