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http://path.web.ua.pt Universidade de Aveiro Departamento de Química Extraction of Phenolic Compounds with Aqueous Two-Phase Systems Trabalho realizado por: Ana Filipa Cláudio Orientação: Prof. João Coutinho e Dra. Mara Freire Aveiro, 2010

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Page 1: Extraction of Phenolic Compounds with Aqueous Two-Phase ...path.web.ua.pt/file/TeseAnaFilipa_ppt.pdf · Extraction of Phenolic Compounds with Aqueous Two-Phase Systems Trabalho realizado

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Universidade de Aveiro

Departamento de Química

Extraction of Phenolic

Compounds

with Aqueous Two-Phase

Systems

Trabalho realizado por: Ana Filipa Cláudio

Orientação: Prof. João Coutinho e Dra. Mara Freire Aveiro, 2010

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Contents

1. Introduction

1.1. Scopes and Objectives

1.2. Aqueous Two-Phase Systems (ATPS)

1.3. Ionic Liquids (ILs)

1.4. Phenolic Compounds (PhCs)

2. Extraction of vanillin in ATPS with ILs

2.1. Vanillin

2.2. Experimental Section

2.3. Results and Discussion

2.4. Conclusions

3. Extraction of gallic acid in ATPS with ILs

3.1. Gallic acid

3.2. Experimental Section

3.3. Results and Discussion

3.4. Conclusions

4. Future Work

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1. Introduction

1.1. Scopes and Objectives:

Use of aqueous two phase systems (ATPS) composed by ionic liquids (ILs) and

typical inorganic salts to develop more benign extraction techniques than those used

nowadays;

ILs appear as potential and alternative replacements for VOCs due to their

negligible vapor pressures and intrinsic character of “designer solvents”;

PhCs present general attractive properties, such as their antioxidant, anti-

inflammatory, anti-microbial and anticarcinogenic capacities, among others.

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1.2. Aqueous Two-Phase Systems (ATPS)

Consist in two aqueous-rich phases mutually incompatible, containing

polymer/polymer, polymer/salt or salt/salt combinations;

Simple method and easiness in scale-up operations;

Used to recover and separate a wide range of biomolecules;

The partitioning of the biomolecule depends on the biomolecule size, surface

properties, molecular weight, temperature, pH, type of inorganic salts, type of

interactions involved, among others.

1. Introduction

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1.3. Ionic Liquids (ILs)

Catalysis;

Organic synthesis;

Chemical reactions;

Chromatographic separations;

Extraction of metal ions;

Separation of biomolecules.

+

Chara

cte

ristics Constituted by large and organic cations and organic or inorganic anions;

Melting point below 100 ºC;

Negligible flammability and vapour pressure;

High chemical stability in a wide range of temperature;

Easiness in recovery and recycling them;

Most of ILs don´t denature biomolecules;

“Benign solvents”;

Tunnable solvents “Designer solvents”

Applic

ations

1. Introduction

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1.4. Phenolic Compounds (PhCs) Present in wood, fruits, vegetables and residues from the industrial or agricultural activities;

PhCs have a special properties, such as:

• High antioxidant capacity;

• Ability of lowering cholesterol;

• Depression of hypertension;

• Protection against cardiovascular disease and human leukemia cells;

•Toxic to bacteria.

Gallic acid Ellagic acid QuercetinVanillin

1. Introduction

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2. Extraction of vanillin in ATPS with ILs

2.1. Vanillin

Major compound of vanilla

Used in foods, beverages, pharmaceutical products and fragrance

industry.

Due to the scarcity of vanillin in natural sources, the synthesis and

recovery of this component is very important.

pKa= 8.2 at 298 K

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2.2. Experimental Section

2. Extraction of vanillin in ATPS with ILs

IL

+

K3PO4

+

vanillin

43POK

ILVan

Van

VanK

IL- rich phase

Salt - rich phase

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Effect of IL Cations in Vanillin Partitioning at 298.15 K

36.49

44.98

49.59

42.39

2.72

44.19

36.45

22.95

0

10

20

30

40

50

60

KVan

Alkyl side chains Surface tension KVan

Alkyl side chains Dispersive interactions KVan

Additional double bounds, aromatic or

hydroxyl groups

Affinity for water Do not improve the

vanillin extraction

The cation-anion interaction strengths

are the major forces driving the partitioning

of vanillin.

2.3. Results and discussion

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Effect of IL Anions in Vanillin Partitioning at 298.15 K

N+

NX-

44.98

31.87

25.6622.74

9.756.94 6.64

0

10

20

30

40

50

KVan

Vanillin partitions preferentially for IL-rich

phases composed by Cl-, Br-, or [N(CN)2]-.

The fluorination of [C4mim][CH3SO3]

to give [C4mim][CF3SO3]

Hydrophobicity KVan

[CH3SO3]- and [CH3CO2]

- are strongly

salting-out inducing ions

KVan

High charge density ions

2.3. Results and discussion

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Effect of Temperature in Vanillin Partitioning

[C4mim]Cl [C4mim][CH3SO4] [C7H7mim]Cl [amim]Cl

21.46

44.98 45.97

30.90

19.26

15.27

22.74 22.03

17.3514.63

29.25

44.19

30.52

27.09 26.99

33.74

36.45

21.83 22.03

13.55

0

10

20

30

40

50

288.15 298.15 308.15 318.15 328.15

KVan

T / K

Temperature greatly influences

the vanillin partitioning

Maximum values in KVan

Energetic and entropic contributions

2.3. Results and discussion

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Termodynamic parameters of transfer - Van´t Hoff approach

R

S

TR

HK

0

mtr

0

mtrVan

1)ln(

0

mtr

0

mtr

0

mtr STHG

)ln( Van

0

mtr KRTG

[C4mim]Cl [C4mim][CH3SO4]

y = 1.5181x - 1.9159

y = 2.8458x - 5.5936

0

1

2

3

4

5

3.0 3.1 3.2 3.3 3.4

ln(K

Va

n)

1 / T [103 K-1]

[C7H7mim]Cl [amim]Cl

y = 1.5859x - 1.6203

y = 2.8975x - 6.1702

0

1

2

3

4

5

3.0 3.1 3.2 3.3 3.4

ln(K

Van)

1 / T [103 K-1]

ln(Kvan) versus T-1 exhibits linearity

0

mtrG < 0Spontaneous

process

0

mtrH < 0 Exothermic process

Favourable vanillin-IL interactions

Depends on anion nature and

more complex cations

0

mtrH

2.3. Results and discussion

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Effect of Concentration in Vanillin Partitioning

[C4mim]Cl [C4mim][CH3SO4] [C7H7mim]Cl

33.09

44.98

57.02

88.3098.08

17.97 22.74

35.04 36.19

21.31

44.19

60.00

79.58

98.69

0

20

40

60

80

100

120

0.5 1.0 2.5 5.0 7.5

KVan

[Van] /(g·dm-3)

KVan[Van]

IL cation influences the

dependency of the partitioning of

vanillin with the solute content.

2.3. Results and discussion

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Viscosity of Systems

1

3

5

7

9

295 300 305 310 315 320 325 330

η/ m

Pa

.s

T / K

1.4

1.8

2.2

2.6

3.0

3.4

3.8

290 300 310 320 330

[C7H7mim]Cl [OHC2mim]Cl [amim]Cl [C4mim]Cl

1

3

5

7

9

11

13

15

295 300 305 310 315 320 325 330

η/

mP

a.s

T / K

[C2mim]Cl [C4mim]Cl [C6mim]Cl [C7mim]Cl [C10mim]Cl

[C4mim]Br [C4mim][CH3SO4] [C4mim][CH3SO3] [C4mim][N(CN)2]

1

2

3

4

295 300 305 310 315 320 325 330

η/

mP

a.s

T / K

[C4mim][CF3SO3] [C4mim]Cl [C4mim][CH3CO2]

1

3

5

7

9

295 300 305 310 315 320 325 330

η/

mP

a.s

T / K

IL-rich phase (full symbols) and K3PO4-rich phase (open symbols)

2.3. Results and discussion

22 wt % PEG2000 + 10 wt % K3PO4

η = 18.94 mPa.s

19 wt % PEG4000 + 9 wt % K3PO4

η = 40.06 mPa.s

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3. Extraction of gallic acid in ATPS with ILs

3.1. Gallic acid

Characterists: antioxidant, anti-inflammatory, antifungal, anti-

tumor, diuretic, depurative, intestinal antiseptic, bacteriostatic,

bactericidal and anti-arthritic.

Pharmaceutical, nutraceutical and cosmetic applications

Treatment of gastric tonus problems, anorexia, bloating, gases,

urinary diseases gout, skin repairer and as sedative.

Gallic acid is present in fruits (grapes), pomegranate husk, vegetables, green and

black teas, oak wood and residual waste.

pKa= 4.4 at 298 K

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3.2 Experimental Section: Phase Diagrams

Na2SO4 + H2O H2O

IL

+

H2O

3. Extraction of gallic acid in ATPS with ILs

Anions or cations with more hydrophobic characteristics have a greater capacity to promote ATPS

ILs containing the anions [N(CN) 2]- and [CF3SO3]

- or larger alkyl side chains at the cation

[C2mim][CF3SO3]

[C4mim][C2H5SO4]

[C4mim][TOS]

[C4mim][CH3SO4]

[C4mim][N(CN)2][C4mim][CF3SO3]

[C7mim]Cl

[C8py][N(CN)2] X[C7H7mim][C2H5SO4]

[C4mim]Br + [C7H7mim]Cl [C8mim]Cl

0

2

4

6

8

0.0 0.5 1.0 1.5 2.0

[IL

] /

(mo

l·k

g-1

)

[Na2SO4] / (mol·kg-1)

Biphasic Region

Monophasic

Region

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[C2mim][CF3SO3]

[C4mim][C2H5SO4]

[C4mim][TOS]

[C4mim][CH3SO4]

[C4mim][N(CN)2][C4mim][CF3SO3]

[C7mim]Cl

[C8py][N(CN)2] X[C7H7mim][C2H5SO4]

[C4mim]Br + [C7H7mim]Cl [C8mim]Cl

0

2

4

0.1 0.3 0.5 0.7 0.9

[IL

] /

(mol·

kg

-1)

[Na2SO4] / (mol·kg-1)

Phase Diagrams

3. Extraction of gallic acid in ATPS with ILs

Higher capability by ILs to promote ATPS

with stronger salting-in inducing behavior

Fixing [C4mim]+

[CF3SO3]- > [TOS]- > [N(CN)2]

-

> [C2H5SO4]- > [CH3SO4]

- > Br-

Fixing [C7H7mim]+

[C2H5SO4]- > Cl-

longer alkyl chains

ability of the IL for ATPS formation

alkyl chain in anion or cation

ability of the IL for ATPS formation

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10.25

20.73

18.12

21.23 20.84

29.58

21.94

19.39

0

10

20

30

KGA

Effect of IL ions in the acid gallic partitioning

Alkyl chains cation or anion Surface tension KGA

Alkyl side chains Dispersive interactions KGA

3.3. Results and discussion

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Effect of pH in the acid gallic partitioning

3.3. Results and discussion

IL+inorganic salt + water Na2SO4 K2HPO4/KH2PO4 K3PO4

[C2mim][CF3SO3]Salt-rich phase 3.32 7.28 13.09

IL-rich phase 2.71 7.57 13.15

[C4mim][CF3SO3]Salt-rich phase 3.04 7.10 12.85

IL-rich phase 3.12 7.37 13.10

[C7mim]ClSalt-rich phase 4.16 7.22 12.85

IL-rich phase 4.15 7.45 12.99

pH at the salt-rich phase ≈ pH at the

IL-rich phase for the same system;

The cation alkyl chain length does

not significantly contributes for

differences in pH;

Changing the anion from [CF3SO3]- to

Cl- guides to slightly differences in the

acidity of both aqueous phases.

0.76

4.25

0

1

2

3

4

5KGA

25 30wt % [C4mim][CF3SO3]

[C2mim][CF3SO3] [C4mim][CF3SO3] [C7mim]Cl

Na2SO4

K2HPO4/

KH2PO4

K3PO4

10.25

20.7321.94

0.91 0.76

11.59

0.58 0.18

8.16

0

10

20

KGA

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4. Future Work

Extend this type of study to other phenolic compounds and test more conditions in

order to optimize extraction routes;

Determine the pH of both rich phases for some systems already evaluated in this

work;

In order to better evaluate the effect of pH on the phenolic compounds extraction it

will be important to extend the study for more systems based on different ILs;

Use the knowledge acquired to proceed to more practical and real experiments

attempting direct extractions from biomass, such as the extraction of phenolic

compounds from wood, plants or wastewater effluents.

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Thank you for your attention!