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Influence of Emulsifiers on Stability and Rheological Properties of Concentrated Oil in Water Emulsions Masami Kawaguchi Division of Chemistry for Materials, Graduate School of Engineering, Mie University, 1577 Kurimamachiya, Tsu, Mie


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Influence of Emulsifiers on Stability and Rheological Properties of Concentrated Oil in Water Emulsions

Masami Kawaguchi Division of Chemistry for Materials, Graduate School of Engineering, Mie University, 1577 Kurimamachiya, Tsu, Mie 514-8507, JAPAN

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SLIDE 2

Outline

  • 1. Introduction
  • 2. Emulsions prepared by polymeric emulsifiers
  • 3. Conclusions for the emulsions prepared by

polymeric emulsifiers

  • 4. Pickering emulsions
  • 5. Conclusions for Pickering emulsions
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SLIDE 3

Introduction

Emulsions, i.e. dispersions of liquid droplets stabilized by emulsifiers in a continuous liquid medium, are very interesting objects for rheological investigations. Studies of emulsions under shear flow have long been a subject of both theoretical and experimental interest and various systematic results have been reported. Emulsions are not thermodynamically stable states and they are metastable dispersions.

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SLIDE 4

γ∆A increases -T∆S decreases

Droplets Two separate phases

∆G or ∆S Emulsification

A G S T A S T A G ∆ γ ∆ ∆ ∆ γ ∆ ∆ γ ∆ = ∴ >> − =

Diagram of the free energy and entropy change of a system during emulsification

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SLIDE 5

Since emulsions are metastable dispersions, instability of emulsions, such as Ostwald ripening and coalescence are not negligible.

Ostwald ripening Coalescence

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On the other hand, other instabilities such as creaming and aggregation also occur after preparation of emulsions. Creaming Aggregation

Emulsification C r e a m i n g A g g r e g a t i

  • n
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SLIDE 7

Dilute Concentrated

Randomly close Compressed

Changes in rheological properties by packing of droplets

φ: Volume fraction of droplets in emulsified phase

) ( ) 64 . ( 2

2 , 3

Weitz Bibette Mason D G

in sm

− − − = φ φ σ

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SLIDE 8

Characterization of emulsions

  • 1. Type of emulsions (Dilution method)
  • 2. Amounts of adsorbed emulsifiers

(Spectroscopic techniques)

  • 3. Droplet Size distribution (Coulter counter,

Optical microscope)

  • 4. Stability of emulsions (Optical methods)
  • 5. Interfacial properties

6. Emulsion rheology

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SLIDE 9

In this presentation, we will force on stability and rheological properties of silicone oil droplets stabilized by some emulsifiers such as water-soluble polymers and silica particles pre-adsorbed polymers in water. The respective emulsifiers were adsorbed on the silicone oil droplets. The resulting oil in water (O/W) emulsions were classified into concentrated emulsions because their volume fraction of oil droplets in the emulsified phase was greater than 0.6. Rheological properties of the corresponding O/W emulsions have been carried out by the measurements of stress-strain curve together with the optical microscopic observation of changes in oil droplets under shear flow, and oscillatory shear viscoelasticity.

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SLIDE 10

Emulsifiers

Polymeric emulsifiers: Hydroxyl propyl methyl Cellulose (HPMC), PEO-PPO-PEO, Poly-N-isopropyl acrylamide (PNIPAM) . Their aqueous solutions were surface active, leading to a decrease in the surface tension. Silica particles: Hydrophilic Aerosil130 fumed silica and hydrophobic Aerosil R-972 fumed silica (silane- coupling modification of silanol groups of 130 with dimethyldichlorosilane) Silica particles pre-adsorbed polymers: Aerosil 130 and Aerosil R-972 silica particles were pre-adsorbed by HPMC and PNIPAM below at the plateau region

  • f adsorption isotherm of the respective polymers.

The silica particles pre-adsorbed polymers were rinsed with water to remove the free polymers.

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Features of emulsions stabilized by polymeric emulsifiers

1) a lager effective volume fraction , where D is the droplet diameter (D>>h), 2) a decrease in the deformation of the interface, 3) an increase in the repulsive forces between droplets.

] / 3 1 [ D h

eff

+ ≈ φ φ

Formation of an adsorbed polymer film layer thickness h on droplet surface provides that

Adsorbed polymeric emulsifiers in the schematic representation is extremely exaggerated.

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SLIDE 12

HPMC: 60SH-400 Mw = 380 x 103 C* = 0.172 g/100 mL PEO-PPO-PEO: F-108, 80 wt% PEO, Mw = 15.5 x 103 Silicone oil: KF96L-1 (1 cSt), KF96-10 (10 cSt), KF96-100 (100 cSt), KF96-1000 (1000 cSt) Interfacial tensions of the oil/aqueous solution of HPMC and PEO- PPO-PEO are 17.3 and 8.4 mN/m, respectively. Preparation of emulsions: 25g of silicone oil were agitated with 50g of 0.5g/100 mL aqueous solution of HPMC or PEO-PPO-PEO for given times ranging from 10 s to 60 min at 8000 rpm and 25 oC.

Emulsions prepared by HPMC and PEO-PPO-PEO

O H O H O H O O-R H H H H H H O-R O-R CH 3-O-R O-R H CH 3-O-R n

R : -CH3, -CH2CH(OH)CH3, -H DS = 1.8 MS = 0.25

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Optical microscopic images of silicone oil droplets prepared by HPMC (I) and PEO-PPO-PEO (II): silicone oil with kinetic viscosity of 1 (a), 10 (b), 100 (c), and 1000 cSt (d).

a b c d

I II 50 µm

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SLIDE 14

Plots of Sauter size D3,2 of oil droplets of the emulsions prepared by HPMC as a function of agitation time for different silicone oils.

=

=

m 1 i 2 i i 3 i i 2 , 3

D n D n D

20 40 60 80 100 120 10 20 30 40 50 60 70

D3,2 (µm) time (min)

φ = 0.72

◇: 1 cSt △: 10 □: 100 ○: 1000

=

=

m 1 i 2 i i 3 i i 2 , 3

D n D n D

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SLIDE 15

Plots of the adsorbed amounts of HPMC on oil droplets as a function

  • f agitation time for different silicone oils.

1 2 3 4 5 6 10 20 30 40 50 60 70

A x 10-4 (g/g) time (min)

◇: 1 cSt △: 10 □: 100 ○: 1000

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SLIDE 16

Rheoscope1

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10-2 10-1 100 101 102 10-2 100 102 104 106

HPMC PEO-PPO-PEO

Shear stress (Pa) Strain (%)

Stress-strain curves of the emulsions prepared by HPMC and PEO-PPO-PEO for 1 cSt silicone oil, together with the optical microscopic images of the corresponding emulsions at given strains. A red circle in each image indicates the same oil droplet.

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SLIDE 18

10-2 10-1 100 101 102 103 10-2 10-1 100 101 102 103

HPMC-1 HPMC-100 F108-1 F108-100

Shear Viscosity (Pas) Shear rate (1/s)

Plots of shear viscosities of the emulsions prepared by HPMC (open symbols) and PEO-PPO-PEO (filled symbols) as a function of shear rate for different silicone oils:1 cSt (circles); 100 cSt (squares).

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SLIDE 19

10-3 10-2 10-1 100 101 102 10-1 100 101 102

G' HPMC-100 G" HPMC G' PEO-PPO-PEO G" PEO-PPO-PEO

G', G" (Pa) Frequency (rad/s)

Plots of G’ (open symbols) and G” (filled symbols) of the emulsions prepared by HPMC (circles) and PEO-PPO-PEO (squares) as a function

  • f frequency for 100 cSt silicone oil
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SLIDE 20

Comparison of the measured G’ and the calculated one of the emulsions prepared by HPMC for different silicone oils

Oil viscosity D3,2 Measured G’ Calculated G’ (cSt) (µm) at 1 rad/s (Pa) (Pa) 1 37.6 123 64.5 10 45.3 74.1 53.7 100 60.7 49.7 40.9 1000 85.9 34.2 31.5

Calculated G’ = φeff(φeff - φc)2σin/D3,2; φeff = φ(1 + 3h/ D3,2), where φc is the volume fraction of the random close-packing (0.64), σin is an interfacial tension (17.3 mN/m), φ is the volume fraction of the emulsion (0.72), and h is the adsorbed polymer layer thickness (20 nm).

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SLIDE 21

PNIPAM: PNIPAM-80 (Mw = 833×103, C* = 0.85 g/100 mL), PNIPAM-150 (1.54 x 106 , C* = 0.62 g/100 mL), PNIPAM- 1000 (1.01 x 107 , C* = 0.23 g/100 mL) Silicone oil: KF96L-1; Kinetic viscosity = 1 cSt Interfacial tension of oil/aqueous solution of PNIPAM = 12.3 mN/m Preparation of emulsions: 10g of silicone oil were agitated with 20g of aqueous solutions of PNIPAM with different concentrations for 30 min at 8000 rpm and 25 oC.

Emulsions prepared by PNIPAM

CH2 CH O N H C CH3 CH3 CH3 n

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SLIDE 22

100 µm 0.5g/100 mL PNIPAM-80

Just 1 week

D3,2 = 43.2 µm D3,2 = 34.1 µm D3,2 = 55.2 µm D3,2 = 35.7 µm Adsorbed amount of PNIPAM = 1.17 mg/g Adsorbed amount of PNIPAM = 1.78 mg/g 1.3g/100 mL PNIPAM-150

50 100 150 200

PNIPAM150 0.5wt% PNIPAM80 0.5wt%

1/(D3,2)2 x 104 (1/µm2) Time (h)

6 5 4 3

Deminiere et al. predicted a linear decreasing relationship between the reciprocal of square of the droplet size and the evolution time

Characteristics of the emulsions prepared by PNIPAM

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SLIDE 23

10-2 10-1 100 101 102 10-1 100 101 102 103 104 105 106

Stress (Pa) Strain (%)

Stress-strain curves of the emulsions prepared by 1.7 g/100 mL PNIPAM-80 (△), 1.3 g/100 mL PNIPAM-150 (□), and 0.5 g/100 mL PNIPAM-1000 (○), together with the optical microscopic images of the corresponding emulsions at given

  • strains. A red circle in each image indicates the same oil droplet. The respective

PNIPAM concentrations correspond to 2C*.

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SLIDE 24

10-2 10-1 100 101 100 101 102 103

0.5 g/100 mL PNIPAM-1000 0.5 g/100 mL PNIPAM-150 0.5 g/100 mL PNIPAM-80 1.3 g/100 mL PNIPAM-150 1.7 g/100 mL PNIPAM-80

Viscosity (Pa s) Shear Rate (1/s)

Shear viscosities of the emulsions prepared by PNIPAM

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SLIDE 25

100 101 102 103

10-1 100 101 102

G' :0.5 g/100 mL PNIPAM-1000 G': 1.3 g/100 mL PNIPAM-150 G': 1.7 g/100 mL PNIPAM-80 G": 0.5g/100 mL PNIPAM-1000 G": 1.3 g/100 mL PNIPAM-150 G": 1.7 g/100 mL PNIPAM-80

G', G" (Pa) Angular Frequency (rad/s)

Dynamic moduli of the emulsions prepared by PNIPAM

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Conclusions for the emulsions prepared by polymers

  • 1. HPMC, PEO-PPO-PEO, and PNIPAM are useful to prepare

O/W emulsions.

  • 2. The emulsions prepared by HPMC showed solidlike visco-

elastic responses, whereas the emulsions prepared by PEO-PPO-PEO indicated liquidlike viscoelastic behavior. Moreover, the simultaneous optical microscopic observation showed that the emulsions stabilized by HPMC do not flow below the yield stress and beyond the yield stress the movements of oil droplets occur first.

  • 3. The emulsions prepared at twice C* of PNIPAM showed

solidlike viscoelastic responses. On the other hand, below C* the emulsions cause coalescence.

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Pickering emulsions

Emulsions stabilized by solid particles are well- known as Pickering emulsions. The solid particles were ranged from inorganic materials to organic

  • nes. The contact angle θ between oil-water

interface is an important parameter to determine the type of Pickering emulsion.

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SLIDE 28
  • R. J. G. Lopetinsky, J. H. Maliyah, and Z. Xu,

in Colloidal Particles at Liquid Interfaces,

  • eds. B. B. Binks and T. S. Horozov,

Cambridge Univ. Press, p. 186 (2006).

Bilayer Stabilization Bridging by a single layer 2-D network 3-D network Domains of particles

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Aerosil-130: specific area = 130 m2/g, silanol density = 2.5/nm2 Aeosil-R972: specific area = 110 m2/g, silanol density = 0.2/nm2 Silicone oil: KF96L-1; Kinetic viscosity of 1 cSt Preparation of emulsions: 15 g of silicone oil were mixed with 30 g of water dispersions with 0.45g of Aeosil-130; 10 g of silicone oil dispersions with 0.3g of Aerosil-R972 were agitated with 20g of water for 30 min at 8000 rpm and 25 oC.

Emulsions stabilized by silica particles

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Emulsions prepared by Aerosil silica particles

100μm

R972: W/O emulsion 130: O/W emulsion Stress-strain curves

10-1 100 101 102 10-2 100 102 104 106

130 R972

Stress (Pa) Strain (%)

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Emulsions prepared by silica particles pre-adsorbed HPMC

Emulsifiers: Aerosil-130 particles pre-adsorbed by HPMC (Mw = 380×103, C* = 0.172 g/100 mL) below at the plateau region of adsorption isotherm of HPMC (0.14 g/g) were washed out to remove the free HPMC. Silicone oil: KF96L-1; Kinetic viscosity of 1 cSt Preparation of emulsions: 15 g of silicone oil were mixed with 30 g of water dispersions with 0.45 g of Aeosil-130 pre-adsorbed HPMC were agitated for 30 min at 8000 rpm and 25 oC.

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SLIDE 32

Optical microscopic images of the emulsions

100μm 100μm 100μm

Silica pre- adsorbed HPMC D3,2 = 81.4 µm D3,2 = 27.0 µm D3,2 = 14.5 µm

100μm 100μm 100μm

HPMC only D3,2 = 46.7 µm D3,2 = 50,4 µm D3,2 = 41.1 µm Silica only

100μm

D3,2 = 113 µm HPMC: 0.030g HPMC: 0.015g HPMC: 0.050g

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SLIDE 33

HPMC (g) Silica (g) φrel Ad (mg/g) D3,2 (µm) σin (mN/m) 0.015 0.0 1.0 1.0 50.4 17.3 0.030 0.0 1.0 2.0 46.7 17.3 0.050 0.0 1.0 3.3 41.1 17.3 0.0 0.45 0.8 0.0 113 36.8 0.015 0.45 0.95 17.2 81.4 36.6 0.030 0.45 0.89 22.4 27.0 36.3 0.050 0.45 0.82 30.4 14.5 20.5

Characteristics of the emulsions prepared by the hydrophilic silica particles pre-adsorbed HPMC

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101 102 103 10-1 100 101 102

45-0 0-1.5 0-3.0 0-5.0 45-1.5 45-3.0 45-5.0

G' (Pa) Angular frequency (rad/s)

G’ of the emulsions prepared by Aerosil-130 pre-adsorbed HPMC, HPMC, and Aerosil-130

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SLIDE 35

10-1 100 101 102 10-2 100 102 104 106

Silica-HPMC HPMC Silica

Shear stress (Pa) Strain (%)

Stress-strain curves of the emulsions prepared by silica (△)、 HPMC (□) and silica pre-adsorbed by HPMC (○). HPMC = 0.050g

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SLIDE 36

Emulsions prepared by Aerosil-130 and Aerosil- R972 silica particles pre-adsorbed P N I P A M

Emulsifiers: Aerosil-130 and Aerosil-R972 particles pre- adsorbed by PNIPAM below at the plateau region of adsorption isotherm (0.12 g/g) of PNIPAM (Mw = 492×103 and C* = 1.12 g/100 mL) were washed out to remove the free PNIPAM. Silicone oil: KF96L-1; Kinetic viscosity of 1 cSt Preparation of emulsions: 10 g of silicone oil were mixed with 20 g of water dispersions with 0.30g of Aeosil-130 and Aerosil-R972 pre-adsorbed PNIPAM were agitated for 30 min at 8000 rpm and 25 oC.

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SLIDE 37

100μm

PNIPAM: 0 g 0.00025

Optical microscopic images of the emulsions prepared by Aeosil-130 pre-adsorbed PNIPAM

0.0030 0.0100 0.0200

D3,2 = 122 µm 128 µm 85.3 µm 30.5 µm 15.7 µm

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SLIDE 38

Optical microscopic images of the emulsions prepared by Aeosil-R972 pre-adsorbed PNIPAM

0.0030 0.0150 0.0200 PNIPAM: 0 g 0.00025

100 µm

D3,2 = 46.0 µm 34.8 µm 34.9 µm 26.8 µm 24.0 µm

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SLIDE 39

PNIPAM (g) φrel Ad (mg/g) D3,2 (µm) φrel Ad (mg/g) D3,2 (µm) Aerosil-130 Aeosil-R972 0.0 0.72 0.0 122 1.00 15.0 46.0 0.00025 0.89 0.4 125 0.97 13.4 34.8 0.001 1.00 2.6 146 0.99 12.6 34.8 0.003 1.00 4.2 85.3 0.99 12.6 34.9 0.01 1.00 10.8 30.5 0.98 13.6. 34.8 0.015 1.00 14.6 19.3 1.00 19.2 26.8 0.02 1.00 17.9 15.7 0.82 26.8 24.0

Characteristics of the emulsions prepared by the hydrophilic and hydrophobic silica particles pre-adsorbed PNIPAM

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SLIDE 40

10-1 100 101 102 10-3 10-1 101 103 105 107

130 Only 0.003 g 0.01 0.02

Stress (Pa) Strain (%)

Stress-strain curves of the emulsions prepared by Aerosil- 130 pre-adsorbed PNIPAM

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SLIDE 41

100 101 102 103 104 10-1 100 101 102

30-0 30-0.025 30-0.30 30-1.0 30-1.5 30-2.0

G' (Pa) Angular frequency (rad/s)

G’ of the emulsions prepared by Aerosil-130 pre-adsorbed PNIPAM.

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SLIDE 42

10-1 100 101 102 103 10-3 10-1 101 103 105 107

R972 Only 0.00025 g 0.003 g 0.02 g

Stress (Pa) Stain (%)

Stress-strain curves of the emulsions prepared by Aerosil- R972 pre-adsorbed PNIPAM

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SLIDE 43

101 102 103 104 10-1 100 101 102

R 9 7 2 G ' R 9 7 2 G " . 2 5 G ' . 2 5 G " . 3 G ' . 3 G " . 2 G ' . 2 G "

G', G" (Pa) Angular frequency (rad/s)

G’ and G” of the emulsions prepared by Aerosil-R972 pre- adsorbed PNIPAM

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Conclusions for the emulsions prepared by silica particles pre-adsorbed polymers

  • 1. Silica particles pre-adsorbed HPMC and PNIPAM are useful

to prepare O/W emulsions. The hydrophilic silica particles pre-adsorbed PNIPAM can fully emulsify silicone oil.

  • 2. With an increase in the adsorbed amounts of polymers, the

emulsions prepared the hydrophilic silica particles pre- adsorbed polymers showed a decrease in the size of oil droplets and an increase in the elastic response.

  • 3. On the other hand, the emulsions prepared the hydrophobic

silica particles pre-adsorbed polymers showed little changes in the size of oil droplets and the viscoelastic response.

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SLIDE 45

Acknowledgements

  • Dr. Kazuhisa Hayakawa (Shin-etsu Chemical Co)
  • Mr. Kenji Kubota
  • Mr. Kazuma Ozawa
  • Mr. Noriaki Sugita
  • Mr. Chikara Morishita
  • Mr. Tomoyuki Suzuki