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Contribution to the optimization of clarification of cashew apple juices by tangential microfiltration: Identification of the foulant fractions and implementation of filterability tests

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Contribution to the optimization of clarification of cashew

apple juices by tangential microfiltration: identification of the

foulant fractions and implementation of filterability tests

Doudjo SORO, Michèle DELALONDE, Christelle WISNIEWSKI, Manuel

DORNIER

UMR Qualisud, Montpellier, France

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

CONTEXT

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

 To valorize cashew apple in juice

 Côte d’Ivoire product 3 million t/year

Almost all production is not utilized

cashew apple is rich in vitamin C, polyphenols

sugars

 To use Membrane process to clarify cashew apple

juice

 Cashew apple juice is astringent

OBJECTIVES

 To determine the main foulant fractions of cashew

apple juices

 To implement tests of filterability

Prediction of the filtration performance

EXPERIMENTAL APPROACH

Lab-scale experiments

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EXPERIMENTAL APPROACH

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

Raw cashew apple juices

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

Supra--collocolloïïdsds Settled particlesSettled particles Colloids Colloids 1 µm 1 nm 100µm Solutes Solutes and and Macromolecules Macromolecules Supra Supra--collocolloïïdsds Colloids Colloids

12 h settling

12 h settling

(Imhoff tanks)

200 nm 1 nm Solutes Solutes and and Macromolecules Macromolecules Colloids Colloids

Filtration

Filtration

(0.2 µm – 2 Bar)

Jb

Jd

Jf

EXPERIMENTAL APPROACH

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

Specific resistance to filtration (SRF)





Settleability parameters

Settleability parameters

0,0E+00 2,0E+07 4,0E+07 6,0E+07 8,0E+07 1,0E+08 1,2E+08 1,4E+08

0,00E+00 1,00E-05 2,00E-05 3,00E-05 4,00E-05 5,00E-05 6,00E-05 t/V (s/m3) V (m3) Filtration Phase Filtration Phase Compression Phase Compression Phase 2

A

P

2

SRF

*

W

×

×

×

×

µ

Cake filtration

Cake filtration

s Law

s Law

Stirred Ultrafiltration Cells

AMICON - Model 8010 Cellulose nitrate membrane 0,2 µm – 2 bar

EXPERIMENTAL APPROACH

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

Capillary Suction Time (CST)

Triton Type 319 Multi-purpose CST

The CST is derived from the time taken to draw a known volume of

filtrate from a suspension by the capillary suction pressure generated

from standard CST filter paper.

Capillary Suction Time has been established as a

reliable method for assessing sewage sludge

filterability.

However the CST technique can be used on any

colloidal aqueous suspension.

EXPERIMENTAL APPROACH

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

Clarification experiments – Pilot unit and operating conditions

Pilot Unit

 For clarification, a pilot of micro-filtration was used. It contains

four modules connected in series. Each module contained a ceramic

membrane of 0.2 µm of pore size.

 Operating conditions:

 Crossflow velocity: 6 m.s

-1

;

 Temperature: 35±2°C;

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RESULTS – Juice characteristics

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

JM

JB

JM

pH

4.05 (0.29)*

3.90 (0,21)*

4.06 (0.15)*

Titratable acidity

(g malic acid.kg TSS

-1

)

2.94 (0.08)*

2.61 (0,09)*

2.66 (0.05)*

Total soluble solids (TSS) (g.kg

-1

)

52 (2)*

56 (2)*

56 (2)*

Total Solids Content (TSC) (g.kg

-1

)

65 (2)

60 (2)

60 (2)

SIS (g.kg

-1

)

7.78 (0.46)

3.32 (0.19)*

0**

Tannins (g.kg TSS

-1

)

23.10 (0,13)** 2.1 (0,01)*

0

Alcohols-insoluble solids (AIS)

(g.kg TSS

-1

)

3.81 (0.15)**

0.25 (0.02)*

0

Viscosity (mPa.s

-1

)

1.24 (0.07)

1.05 (0.05)

1.13 (0.04)

Turbidity (UNT)

8 033 (907)**

233 (15)*

6 (<1)*

Vitamin C (g.kg TSS

-1

)

15.0 (0.5)

14.2 (0.1)

14.1 (0.7)

Total nitrogen (g.kg.TSS

-1

)

4.04

2.09

1.89

RESULTS – SRF

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

RESULTS – CST

RESULTS – Permeate flux

39 L.h

-1

.m

-2

41 L.h

-1

.m

-2

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RESULTS – DISCUSSION

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

 JB (Raw juice) : contains more tannins, total

nitrogène, AIS, SIS than JD (Decanted juice) one.

 JM (Clarify juice): not contains tanins, AIS and

SIS. Total nitrogène is reduced

 Jp of JM (116 L.h

-1

.m

-2

), is very raise than JB

(39 L.h

-1

.m

-2

)and JD (40 L.h

-1

.m

-2

).

RESULTS – DISCUSSION

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

 JD has a different behavior of other juice during

filtration with cell amicon. Its SRF is very high but its

permeate flux is the same than JB.

JB

JD

JM

Jp (L.h

-1

.m

-2

)

(3<VRR<8; TMP= 2bar)

39

40

116

SRF (Kg.m

-1

)

3.15 10

12

106 10

12

5.51 10

12

CST (s)

9.8 (0.9)

a

7.9 (0.7)

b

6.6 (0.9)

b

RESULTS – DISCUSSION

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

 The JB having the lowest SRF, should in

principle have the permeate flux is higher. But

this is not the case

 This means that we can not use the

filterability tests on Amicon cell to predict the

permeate flux of juice

 The values ​​of the Capillary Suction Time

(CST) of JD and JM are statistically identical.

However, the permeate flux are very different;

 We can not use the filterability tests on CST to

predict the permeate flux of juices

RESULTS – DISCUSSION

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

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CONCLUSION

International Conference on Membrane Science & Technology MST2012: Sustainable Energy and Environment

 This study shows that:

 simples filterability tests can not be used to

predict permeate flux during microfiltration;

The colloidal fraction is responsible for

membrane fouling in crossflow microfiltration;

Crossflow microfiltration removes the

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