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Page 1: ACKNOWLEDGEMENTS · 2017-01-05 · Introduction Rheology is a science in the early twentieth century. It’s dealt by an impressive number of specialists: engineers, chemists, physicists,

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Page 2: ACKNOWLEDGEMENTS · 2017-01-05 · Introduction Rheology is a science in the early twentieth century. It’s dealt by an impressive number of specialists: engineers, chemists, physicists,

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Page 3: ACKNOWLEDGEMENTS · 2017-01-05 · Introduction Rheology is a science in the early twentieth century. It’s dealt by an impressive number of specialists: engineers, chemists, physicists,

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ACKNOWLEDGEMENTS

I would like to thank to Mr. Acad. Bogdan C. Simionescu, scientific

adviser of this work, for the professionalism which he has guided me and for all

competent and valuable scientific advices.

I also remain grateful to Mrs. Conf. dr. ing. Constanţa Ibănescu for

the permanent encouragement that she has offered me and to the confidence

that she has granted me ever since the beginning of our collaboration. I also

thank for the valuable ideas and for a source of inspiration and knowledge that

contributed to my training as a scientist.

I would also to thank Mrs. Conf. dr. ing. Gabriela Lisa for useful

advice that she gave me every time she had the opportunity.

I also thank all my colleagues of department Naturals and Synthetics

Polymers, Technical University „Gheorghe Asachi” Iasi, for moral support

and encouragement offered to complete the thesis.

I would also to thank all my colleagues of Institute of Macromolecular

Chemistry „Petru Poni” Iasi for encouragement and understanding.

Last but not least, I whole-heartedly thank my family for love and trust

granted. Thank you for all the support you give me.

Thank you!

Maricel Danu

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THESIS CONTENTS

Part I. Literature data on rheological analysis of materials……………... 6 Chapter I. Rheology – basic concepts..................................................................... 6

I.1. Rheology, rheometry and viscoelasticity…………………………………….. 6 I.2. Deformation behavior and viscosity………………………………………….. 19

I.2.1. Strain and shear strain……………………………………………………. 19 I.2.2. Viscosity and viscosity coefficients……………………………………… 21

I.3. Flow behavior………………………………………………………………… 28 I.4. Elastic behavior and shear modulus………………………………………….. 30 I.5 Viscoelastic behavior………………………………………………………….. 31

I.5.1. Viscoelastic liquids………………………………………………………. 32 I.5.2. Viscoelastic solids………………………………………………………... 34

I.6. Oscillatory tests………………………………………………………………. 35 I.6.1. Introduction………………………………………………………………. 35 I.6.2. Basic concepts……………………………………………………………. 38 I.6.3. Amplitude sweep…………………………………………………………. 42 I.6.4. Frequency sweep…………………………………………………………. 45 I.6.5. Creep tests………………………………………………………………... 47 I.6.6. Temperature tests………………………………………………………… 51 I.6.7. Time tests………………………………………………………………… 52

I.7. Rotational tests……………………………………………………………….. 54 I.7.1. Flow curves………………………………………………………………. 55

I.8. Structure – rheological relationships in polymeric systems..………………… 57 I.8.1. Introduction………………………………………………………………… 57 I.8.2. Polymers rheology …………………………………………………………. 60 I.8.3. Zero shear viscosity………………………………………………………… 62 I.8.4. Determination of the molecular weight distribution using rheology….......... 66 I.8.5. Structure – rheological behavior relationships in multi-component polymer

systems……………………………………………….. 71

I.8.6. Correlation between the microstructure and linear/nonlinear viscoelastic behavior……………………………………………………………………..

76

I.8.7. Conclusions………………………………………………………………… 78 Bibliography……………………………………………………………………… 79

Part II. Original results on the structures – rheological properties relationship in polymer systems...................................................

86

Chapter II. The experimental part……………………………………………….. 86 II.1. Experimental techniques and recipes………………………………………... 86

II.1.1. Experimental methods and equipments…………………………………. 86 II.1.2. Materials and recipes……………………………………………………. 90

II.1.2.1. Synthesis of thermosensitive polymers by SET-LRP technique……. 90 II.1.2.2. Synthesis of grafted polysiloxane compounds (series of samples

MSi)………………………………………………………………………………… 93

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II.2. Studied polymer systems…………………………………………………….. 99 Bibliography……………………………………………………………………… 102

Chapter III. Oscillatory tests……………………………………………………... 104 III.1. Amplitude sweep……………………………………………………………. 104

III.1.1. Chapter objectives………………………………………………………… 104 III.1.2. Basic concepts…………………………………………………………….. 104 III.1.3. Structural information for different types of polymer systems…………… 105

III.1.3.1. Polymer melts………………………………………………………… 105 III.1.3.2. Polymer solutions…………………………………………………….. 114 III.1.3.3. Two- and three-dimensional networks based on protein –

polysaccharide………………………………………………………………………. 122

III.1.3.3.1. Gluten – starch networks…………………………………………. 122 III.1.3.3.2. Gelatin – starch networks………………………………………… 126

III.1.3.4. Hydrogels……………………………………………………………... 132 III.1.3.5. Cosmetic emulsions…………………………………………………... 135 III.1.3.6. Conclusions…………………………………………………………... 141

Bibliography……………………………………………………………………… 142 III.2. Frequency sweep……………………………………………………………. 146

III.2.1. Chapter objectives………………………………………………………… 146 III.2.2. Studies on different polymer systems…………………………………….. 146

III.2.2.1. Polymer melts………………………………………………………… 146 III.2.2.2. Polymer solutions…………………………………………………….. 159 III.2.2.3. Two- and three-dimensional networks based on protein –

polysaccharide………………………………………………………………………. 166

III.2.2.3.1. Gluten – starch networks…………………………………………. 166 III.2.2.3.2. Gelatin – starch networks………………………………………… 170

III.2.2.4. Hydrogels……………………………………………………………….. 172 III.2.2.5. Cosmetic emulsions…………………………………………………….. 176 III.2.2.6. Conclusions……………………………………………………………... 180 Bibliography……………………………………………………………………… 181

Chapter IV. Rotational tests – applications in the study of structure – rheological properties relationships …………………………………….………..

183

IV.1. Chapter objectives………………………………………………………….. 183 IV.2. Studies on different polymer systems………………………………….. 183

IV.2.1. Polymer melts………………………………………………………….. 183 IV.2.2. Polymer solutions………………………………………………………. 193 IV.2.3. Cosmetic emulsions……………………………………………………. 232 IV.2.4. Conclusions…………………………………………………………….. 233

Bibliography……………………………………………………………………… 233 Chapter V. Temperature tests……………………………………………………. 234

V.1. Chapter objectives…………………………………………………………… 234 V.2. Structural information for different types of polymer systems……………… 234

V.2.1. Polymer melts…………………………………………………………… 234 V.2.2. Grafted polysiloxane solutions………………………………………….. 243 V.2.3. Two- and three-dimensional networks based on protein - polysaccharide 256

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V.2.3.1. Gluten – starch networks……………………………………………. 256 V.2.3.2. Gelatin – starch networks…………………………………………… 260

V.2.4. Conclusions……………………………………………………………… 264 Bibliography……………………………………………………………………… 265

Chapter VI. Time tests............................................................................................. 271 VI.1. Chapter objectives………………………………………………………….. 271 VI.2. Structural information for polymer melts…………………………………... 271 VI.3. Conclusions………………………………………………………………… 277 Bibliography……………………………………………………………………… 277

Chapter VII. Rheo –SALS – the applications in the structure – rheological properties relationships …………………………………………………………...

278

VII.1. Chapter objectives…………………………………………………………. 278 VII.2. Basic concepts……………………………………………………………... 278 VII.3. Applications in the study of grafted polysiloxane polymer solutions……... 279 VII.4. Conclusions………………………………………………………………... 281 Bibliography……………………………………………………………………… 282

General conclusions……………………………………………………………….. 283 Scientific activity…………………………………………………………………... 285

This summary presented the concentrated form of the original results. Numbering of schemes, figures, tables and bibliography is corresponding indications of the thesis.

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Introduction

Rheology is a science in the early twentieth century. It’s dealt by an impressive number of specialists: engineers, chemists, physicists, geologists, mathematicians, etc. Each one develops methods of investigation, rheological models and tries to give definitions in the language of their specialties. This science can be regarded as a branch of mechanics. The basic tool which characterizing the rheology is the concept of the rheological model, in the other words, the mathematical expression between stress, answer and property.

In its origin, the term “rheology” has been related to flowing media, since the main root of the word means “to flow” (rheo in Greek). Currently, the term is used for any real material because sometimes it is very difficult to estimate whether a material is solid or fluid. As a result, the analytical methods used for both classes of media are very similar.

Rheology is a science concerned with the mechanical properties of various solid-like, liquid-like, and intermediate technological and natural products (materials). It accomplishes its goals be means of models representing principle peculiarities of behavior of these materials. The viscoelastic characteristic of material is a deformation - behavior relationship of behavior and deformations (or changes of shape) and a model gives a mathematical formulation of the relationship, rheological properties being expressed by the structure of a model (i.e., its mathematical image) and values of constants included in a model – characteristic for a material.

The results of macroscopic description of behavior of real engineering and biological media, based on their rheologial properties, are used in numerous applications related to technology of synthesis, processing, and shaping of different materials (plastics and ceramics, emulsions and dispersions in the chemical and food industries, pharmaceuticals, cosmetics, transport, oil industry, etc.), their long-term properties, natural phenomena, such as movement of mud streams and glaciers, and biological problems (dynamics of blood circulation, activitity of bones). We can conclude that the first goal of rheology is a search for stress versus deformation relationships for various technological and engineering materials in order to solve macroscopic problems related to continuum mechanics of these materials.

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The second goal of rheology consists in establishing relationships between rheological properties of a material and its molecular composition content. It is an important independent problem related to estimating quality of materials, understanding the laws of molecular movements and intermolecular interactions.

PhD thesis “Structure – rheological properties relationships in polymeric systems” is divided into two parts and contains seven chapters. The first part summarizes the literature data on the reological analysis of materials. The second part contains the original results on the structure – rheological properties relationships in polymeric systems.

Chapter I include the basic concepts of rheology. This chapter details some theoretical aspects of the strain and flow behavior of the materials, are described the types of rheological tests used in making a structure – rheological properties correlation and are presented some examples.

Chapter II contains data on polymer systems used in the PhD thesis and the conditions for achieving of rheological experiments on these systems. In this thesis were studied four groups of polymer systems: polymer melts, polymer solutions, two- and three-dimensional networks and cosmetic systems.

Chapters III – VII provide information about oscillatory tests, rotational tests, temperature tests, time tests and rheo-SALS performed on polymer systems. The relationship between the polymer rheology and their structure is of a special interest because the rheological experiments are very sensible at structural changes, as well as the possibility of using the structural characteristics of the systems in order to obtain products with controlled rheological properties.

The PhD thesis contains 291 pages, 71 tables, 197 figures, 5 schemes and 360 bibliographies.

Bibliografie selectivă

1. MALKIN, A. Y. Rheology Fundamentals. Toronto: ChemTec Publishing, 1994 4. HAE RYU, C., CHAN BAE, Y., HWAN LEE, S. Polymer, v. 39, n. 25, p. 6293-6299, 1998 9. DROZDOV, A. D. Eur. Polym. J., v. 36, n. 10, p. 2063-2074, 2000

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CHAPTER III. OSCILLATORY TESTS

III.1. Amplitude sweep III.1.1. Chapter objectives

The objectives of this chapter are: - to determine the linear viscoelastic range for analyzed systems; - analysis of the influence of certain factors (temperature, concentration, etc.) on the measured rheological parameters; - to obtain the information about the mechanical stability of the systems; - identification of the useful rheological information to describe the structure of the polymer when it isn’t known in detail; - to check the possible way to predict the rheological behavior of the polymer system when the structure is known; - to establish a correlation between the structure and rheological properties

of studied systems.

III.1.2. Basic concepts The oscillatory tests are very useful to describe the microstructure of

viscoelastic materials; it provides information about the structure and material elasticity [1]. Rheological parameters are the storage modulus G’ (a measure of the deformation energy accumulated during shear test, representing the elastic behavior of the material), loss modulus G” (a measure of the deformation energy used by the sample during shear test, representing the viscous behavior of the material), phase angle δ, damping factor or loss factor tan δ = G”/G’ (describes the ratio of the viscous and elastic component of the viscoelastic behavior) and the complex viscosity η* [2-5].

One of the most important oscillatory tests for establishing the correlation between the structure and the rheological properties of materials is amplitude sweep. In this test, the amplitude is varied and the frequency is maintained constant (figure 3.1a). [4]. Amplitude sweep is used to determine the linear viscoelastic (LVE) range of the material, so being able to set the correct parameters for subsequent oscillatory tests (figure 3.1b). [6]

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a b

Figure 3.1. Amplitude sweep

The maximum deformation to which the storage modulus value G’ remains constant is called the critical strain and it defines the limit of the linear viscoelastic (LVE) range. The critical strain indicates the minimum of energy required to destabilize the structure of the material.

III.1.3. Structural information for different types of polymer systems

The oscillatory tests allow investigating a large range of the viscoelastic materials: polymer melts, polymer solutions, pastes, gels and other rigid materials. The relationship between the polymer rheology and their structure is of a special interest because the rheological experiments are very sensible at structural changes.

III.1.3.1. Polymer melts For polymer melts, the study of the rheological behavior allows depth

analysis of the behavior at processing and understanding of the induced structural changes by the thermo-mechanical stress. On the other hand, the rheological tests of the polymer melts have a significant contribution to the overall macroscopic behavior of polymer melts [8].

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0.01 0.1 1 10 100100

1000

10000

100000Pa

MT1 MT2-10 MT2-20

Strain %

G'

G"

Figure 3.4. Amplitude sweep of the samples MT1, MT2-10 şi MT2-20

An investigation of the correlation between structure and rheological

properties by comparing the amplitude sweep of the samples MT1, MT2-10 and MT2-20 (figure 3.4) was performed. In the last two samples, the composition contains a solid phase consisting of the beads of PMMA and PBMA, 10% and 20%, dissolved in a liquid phase of MMA, it is noted from the experimental data that the presence of the PBMA in the copolymer structure determined the growth of the dynamic parameters G’ and G” and an increase in the linear viscoelastic range, suggesting to obtain some stable structure. It is due to the fact that, as in the chemical structure of the PBMA is observed, there is an increase in the side chains of the polymer system resulting in an increase of the intramolecular hydrogen bonds.

With the Rheoplus software the rheological parameters of the amplitude sweep were calculated (table 3.3). These parameters are absolutely necessary in achieving a correlation structure – rheological properties.

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Table 3.3. The rheological parameters of the amplitude sweep for samples: MT1, MT2-10 şi MT2-20

Sample γL (%) τL(Pa) γc.o. (%) τc.o.(Pa) G’ = G” (Pa) MT1 0,5 149 22,2 1581 5020

MT2-10 5 2420 46,9 2337 3506 MT2-20 5 4160 39 4961 8893

III.1.3.2. Polymer solutions

For the polymer solutions, the molecules are significantly different as against particles in that the polymer backbone are continuously rotating and while the molecules have a form and an average orientation, its configuration and orientation changes in the smaller scale until they reach an equilibrium shape.

Under the influence of strain, polymer molecules change their orientation and the shape. In dilute solution, the rheology of solution is dependent only on the individual movement of the chain and the number (concentration) of chain in the system. At high concentration, in the range of the entangled solution, the interaction between polymer molecules due to the entangled polymer chain significantly affects the rheological behavior. Most researchers believe that entangled polymer chains lead to the formation of a particular type of network. Molecular weight and polymer concentration significantly influences the rheological behavior of polymer solutions [8].

The polysiloxanes are a class of polymers with unique properties: low value of Tg, the high flexibility of chain, good thermal resistance, stable at the action of oxidants and UV radiation, hydrophobicity, etc. For the polymer solution based on PSI-g-poly (NIPAM-co-DMA) or PSI-g-NIPAM (table 3.10), to determine the linear viscoelastic range the amplitude sweep was performed [9].

Table 3.10. Polymer parameters PSI-g-poly (NIPAM-co-DMA) Sample Tg (oC) Polymerization degree at the

side chain Molecular weight

MS1 124,8 10 NIPAM/ 3 DMA 60150 MS2 87,1 62 NIPAM 49104 MS3 85,6 24 NIPAM/ 32 DMA 24320

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The linear viscoelastic range limit of the analyzed solutions as

maximum deformation of 1% was determined (figure 3.11). From the diagram there is a good stability of these solutions due to the fact that the two dynamic moduli are parallel on the entire measurement domain.

0.1 1 10 1001E-7

1E-6

1E-5

1E-4

1E-3

0.01

0.1

1Pa

MS1 MS2 MS3

Strain %

G'

G"

Figure 3.11. Amplitude sweep for MS1, MS2 and MS3 samples at

concentration 1mg/ml

III.1.3.3. Two- and three-dimensional networks based on protein - polysaccharide

III.1.3.3.1. Gluten – starch networks Between cereal flours, only wheat flour mixed with water a viscoelastic

three-dimensional network can form. The rheological tests in the linear viscoelastic range have been used for an understanding the three-dimensional network based on protein – polysaccharide structure and properties and to study the ingredient functions of the system [23].

The dough exhibits a viscoelastic behavior combining the properties of the viscous fluid and the elastic solid. Flour and water are essential ingredients in the dough. Each ingredient plays an important role to define the dough

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structure and rheological properties. The main components of flour, gluten and starch, have a great influence on the final product properties, but also the presence of gas bubbles influence this behavior. So, the final product quality depends on the protein content, product volume and the dough texture.

Basic mechanical properties of the wheat flour dough are very important because the behavior of handling during processing and also the interaction between dough components is affected of this [29]. The diversity of food structures is based on only two kinds of macromolecules: proteins and polysaccharides. Although many food components participate in the formation of structural and textural features of foods these two biopolymers are the most important constructional materials [30]. Also the dynamic tests have proved useful for establishing the dough viscoelastic properties [31].

Starch – gluten three-dimensional networks are remarkably important for the overall behavior of wheat flour – water systems. Rheological behavior of such systems helps in getting essential information about the material’s structural properties and processing conditions. Flour has two main components, starch and gluten, but small quantities of fat, enzymes, minerals and water can be also evidenced. The proportion and quality of these components are responsible for the processability and acceptability of the final product by consumer.

The oscillatory strain test was performed to determine the limits of the linear viscoelastic domain, important information regarding the mechanical stability of the developed dough structure can also obtained. Figure 3.19 presents the results of the amplitude sweep test for the three samples, at 20 oC, with a different content of gluten: 30%, 40% and 50%. At low strain domain, in the so called linear viscoelastic range, both the G’ and G” curves are showing constant plateau values, mostly on different levels. High G’ values are an indication there is a stable internal network of force inside of the sample [33]. For starch – gluten three-dimensional network, the limit of the linear viscoelastic range usually is deformation of 0.1% [34, 35].

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0.01 0.1 1 10 100103

104

105

G'

G"

MG1-30 MG1-40 MG1-50

Strain%

Pa

Figure 3.19. Amplitude sweep for samples: MG1-30, MG1-40 and MG1-50

As shown in the figure, the values of the storage and loss modulus are

relatively constant at deformation less the 0.1%. After this deformation, both moduli decrease, indicating the beginning of the nonlinear behavior. Decrease of the dynamic moduli becomes more pronounced at higher deformation of 1%, suggesting the destruction of the network structure.

The limits of the linear viscoelastic region for all the analyzed samples in terms of deformation between 0.1% and 1% and the corresponding values for G’ were recorded (table 3.11). The increase in the amount of gluten extends the linear viscoelastic range but generates lower G’ and G” values within the linear viscoelastic region, suggesting more stable and flexible structures. The gluten three-dimensional network including starch granules is well developed and stable allowing air bubbles to be entrapped and generating a desirable texture [33].

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Table 3.11. The parameters of the linear viscoelastic region for samples: MG1-30, MG1-40 and MG1-50

Sample Strain, % Strain stress (Pa) Storage modulus, G’ (Pa)

MG1-30 0,1 76,13 7,019·104 MG1-40 0,1 45,16 4,096·104

MG1-50 1 286 2,637·104

III.1.3.3.2. Gelatin – starch networks

The interest for gluten free dietary products has increased in the last period due to the negative effect of gluten in different gastrointestinal diseases. When the structural and textural properties of different foods are considered it is worth to mention the large variety of products is mainly based on two types of macromolecules: proteins and polysaccharides [30]. Each type of biopolymer has a specific influence on the overall proprieties of foods and the different kinds of achievable structures and textures are the result of the vast diversity of possible intra- and intermolecular bonds. In flour based foods gluten is essential for the global viscoelastic behavior. Replacing gluten is not an easy task without affecting the global rheological properties of the final product and its texture and acceptance by the consumer. Experiments have been performed, as well, to obtain and characterize different types of gelatin based networks useful both in food and biomedical applications.

The formation of the gel or the paste, which is a determinant factor of the food texture, depends not only on the starch concentration, but also on the structure of the swollen starch granules, the amount of the amylopectin and the amylase, the interactions between amylase, amylopectin and granules, and the heating conditions (temperature, heating time and heating rate) [49-52].

Rheological characterization of food can provide essential information about the material structure, as well as processability, sensory perception, handling capacity, shape stability [40].

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0.01 0.1 1 10 100

0.01

0.1

1

10

G'

Strain (%)

MG2-A3 MG2-AG1 MG2-AG2 MG2-AG3 MG2-AG4 MG2-AG5 MG2-AG6 MG2-AG7 MG2-AG8 MG2-AG9 MG2-G

Pa

Figure 3.23. Amplitude sweep for analyzed samples (the storage modulus)

0.01 0.1 1 10 100

0.1

1

Strain (%)

MG2-A3 MG2-AG1 MG2-AG2 MG2-AG3 MG2-AG4 MG2-AG5 MG2-AG6 MG2-AG7 MG2-AG8 MG2-AG9 MG2-G

G''

Pa

Figure 3.24. Amplitude sweep for analyzed samples (the loss modulus)

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In the figures 3.23 and 3.24, the evolution of the storage and loss moduli for all the prepared samples is presented as resulted from the amplitude sweep tests (constant frequency of 1 Hz and variable strain between 0.01 and 100 %). The behavior of all analyzed systems varies from solid-like (G’>G”) (samples MG2-A3 to MG2-AG7) to liquid-like (G’<G”) (samples MG2-AG8 to MG2-G) with special mention of sample MG2-AG7 for which G’ is almost equal to G” on the entire deformation range. Furthermore, the strength of the gels decreases with the increase in gelatin content. It is worth to mention that adding small amounts of gelatin to starch gels improves the mechanical properties of the resulting system. Moreover, adding gelatin to the systems extends the linear viscoelastic range and makes the network more flexible and resistant to deformation. The increase in the gel strength could be explained through the increase of the amount of crosslinks induced by gelatin and the rearrangements of the biopolymers chains. As far as gelatin becomes predominant in the system, the starch network is disturbed and the system needs special conditions for gelification. The liquid-like mixtures are flexible and stable due to the weak physical interactions. [40]

III.1.3.5. Cosmetic emulsions The emulsions are widely used in the cosmetic industry to prepare the

lotions and the cosmetic creams. Rheological characteristics that can control the most sensory properties are determined by oscillatory tests [56].

Comparative rheological studies have been carried out for three cosmetics emulsions based on oil/water emulsions were added the xanthan gum (MC1), starch (MC2) and carbomer (MC3).

Analyzing the figure 3.29, it’s observed that the sample with xanthan gum (MC1) show an increase in stiffness due to the higher value of the storage modulus G’ and a lower limit of the linear viscoelastic range is determined. So, this sample shows an increase in consistency, but its structure is unstable and susceptible to mechanical deformation.

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0.01 0.1 1 10 10010

100

1000

10000

G'

G"

MC1 MC2 MC3

Pa

Strain%

Figure 3.29. Amplitude sweep tests for cosmetic emulsions

The presence of starch in the formulation of smaple MC2 increases the

limits of the linear viscoelastic range with no significant influence on the consistency. The samples containing carbomer as a rheological modifier exhibits the highest limiting value of the shear strain. This extension of the linear viscoelastic range is due to the crosslinked acrylic polymer (carbopol), being well known that the polymer solution characterized by strong intermolecular associations have longer viscoelastic zones. Such a structure confers higher mechanical stability to the formulation and thus the linear viscoelastic domain is enlarged.

Taking into consideration the limits of the linear viscoelastic domain and the difference in magnitude between G’ and G” for the three cosmetics systems, the sample with carbomer proved to be the most stable system. This observation is supported by the magnitude of the yield stress (τc) (table 3.14), usually correlated to the strength of the interparticle interaction in the three-dimensional microstructure of cosmetics systems. Sample MC3is characterized by a yield stress value two times higher than the two other samples, indicating

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more contact surfaces, stronger packing between particles and a lower tendency for bridging flocculation.

Table 3.14. Rheological parameters of cosmetics systems Sample LVE range γL (%) τc (Pa)

G’ (Pa) G” (Pa) MC1 6698,79 2029,9 0,1 42,12 MC2 2755,97 735,47 0,5 40,83 MC3 719,55 132,66 1 98,06

Oscillatory rheological tests can offer valuable information about the

cosmetics emulsions structure and stability. Sensory perception proved to be in good correlation with the rheological measurements and rheology offers a versatile tool to appreciate the behavior of a cream when applied on skin. The lower strain necessary to break down the structure is a desirable feature since it simulates the onset of spreading of cream in the skin and allows a better absorption. The higher the percent strain, the stronger the cream structure and mechanical stability, but the greatest strain is needed to cause effective spreading. Sample MC3 proves the best structure stability but needs greater strain to completely spread on the skin. The lower G’ and G” values are indication of smooth feeling. The sample MC1 needs lower strain and easily spreads on the skin, but higher G’ and G” values indicate a tough feeling. The sample MC2 exhibits a balance between samples MC1 and MC3 and seems to combine a pleasant feeling with a good structure stability and spreadability on the skin. Therefore, knowledge of viscoelastic parameters of cosmetics can be used to predict the performances of different cosmetic emulsions and the possibility to use them for specific applications.

III.1.3.6. Conclusions

The limit of the linear viscoelastic range is determined by the amplitude sweep tests. These tests allowed the analysis of the influence of the factors (temperature, concentration, etc.) on the dynamic moduli. At the very small strain, dynamic moduli have a linear behavior. In the nonlinear viscoelastic domain, the pseudoplastic behavior can be interpreted by destroying and

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rebuilding the internal structure of the material as a response to imposed stimuli. If the storage modulus is greater than the loss modulus, the material presents a rheological behavior prevails against the elastic of viscous properties.

Selective bibliography

1. RUSU HODOROG, A. D., IBĂNESCU, C., DANU, M., SIMIONESCU, B. C., ROCHA, L., HURDUC, N., Polym. Bull., v. 69, n. 5, p. 579-595, 2012 2. IBĂNESCU, C., DANU, M., NANU, A., LUNGU, M., SIMIONESCU, B. C., Rev Roum. de Chim., v. 55, n. 11-12, p. 933-940, 2010 9. GE, Z., ZHOU, Y., TONG, Z., LIU, S., Langmuir, v. 27, n. 3, p. 1143-1151, 2011 29. UPADHYAY, R., GHOSAL, D., MEHRA, A., Journal of Food Engineering, v. 109, p. 104-113, 2012 33. DANU, M., ROTARU, I., IBĂNESCU, C., HURDUC, N., IBĂNESCU, S. A., SIMIONESCU, B. C., Environ. Eng. Manage. J., v. 11,n. 11, p. 1883-1888, 2012 40. SIMIONESCU, A.B., IBĂNESCU, S. A., DANU, M., ROTARU, I., IBĂNESCU, C., Revista de Chimie, 2013

III.2. Frequency sweep III.2.1. Chapter objectives

Frequency sweep tests are widely used for polymers, especially for its ability to measure the changes in the elastic and viscous behavior of the material, thereby achieving the important information about the internal structure, molecular weight and long-term stability. The frequency sweep diagrams are defined as “fingerprint” of the viscoelastic behavior of the material and provide opportunities for good correlation between viscoelastic behavior and material composition.

III.2.2. Studies on different polymer systems In the frequency sweep test a sinusoidal strain with constant amplitude

(depending on the limits of the linear viscoelastic range for each sample) is applied, the oscillation frequency being varied. This test provides important information about the internal structure, molecular weight and long-term stability of the studied compound. The storage modulus (G’) gives information

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about the elastic behavior of the sample obtaining the information on the structural strength of the sample (stiffness) and the loss modulus (G”) describes the viscous behavior (flexibility). High G’ values provides information about the presence of the stable internal network of force inside of the sample, which indicates its mechanical and structural stability [1,2].

III.2.2.1. Polymer melts An investigation of the structure – rheological properties correlation by

comparing the frequency sweep for sample MT1, MT2-10 and MT2-20 (figure 3.34) was done. Analyzing the frequency sweep diagram is observed the influence of the amount of the PBMA of the solid polymer phase on the viscoelastic behavior of the tested samples. In this case, besides the Crossover model, can be applied Carreau-Yasuda model to calculate the characteristic parameters η0, λ and a. These parameters are absolutely necessary in achieving a structure – rheological properties correlation for studied polymers (table 3.20).

101

102

103

104

105

106

0.1 1 10 100100

101

102

103

104

105

MT1 MT2-10 MT2-20

l*l

G'

G"

PaPa s

1/sFrecventa

Figure 3.34. Frequency sweep tests for samples: MT1, MT2-10 and MT2-20

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Table 3.20. Rheological parameters of Carreau-Yasuda and Crossover models for samples: MT1, MT2-10 and MT2-20 Sample Zero shear

viscosity, η0 (Pa s)

Infinite shear

viscosity, η∞ (Pa s)

Carreau-Yasuda parameters

Crossover

λ (sec) a n ω (rad/s)

G’=G” (Pa)

MT1 50344 1,597 474,54 0,71 0,0926 28,23 213,2

MT2-10

4,07·106 193,1 474,54 0,523 0,1729 - -

MT2-20

5,2·1010 532,08 0,0014 0,0689 -0,969 - -

III.2.2.2. Polymer solutions

After the determination of the limit of the linear viscoelastic range by means of amplitude sweep, a characterization of polymer solutions using the frequency sweep below the critical strain, γc, can be performed. This test gives information about the effect of the colloidal forces and the interactions between particles.

0.1 1 10 1001E-7

1E-6

1E-5

1E-4

1E-3

0.01

0.1

1

Pa MS3 1mg/ml

Angular frequency

G'

G"

1/s

Figure 3.43. Frequency sweep for sample MS3 with concentration of 1mg/ml

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For polymer solution based on PSI-g-poly (NIPAM-co-DMA) (sample MS3), the frequency sweep show a stable structure type pseudo gel due to intermolecular hydrogen bonds. It shows good long-term stability of the sample (figure 3.43) because the both dynamic moduli are parallel throughout the studied frequency range. A smaller value of the dynamic moduli suggests a low intensity of the interactions between polymer solution components [8].

III.2.2.3. Two- and three-dimensional networks based on protein - polysaccharide

III.2.2.3.1. Gluten – starch networks Frequency sweep can explain the importance of interactions between the

components and their role in dough processing [12]. Due to its ability to measure the changes of the material viscous and elastic behavior, the frequency sweep test became the most used oscillatory tests [13]. Frequency sweep provides opportunities for a better correlation between rheological behavior and material composition [14].

0.1 1 10 100103

104

105

106

104

105

106

l*l

G' G"

Angular frequency, 1/s

Pa sPa

MG1-30

Figure 3.50. Frequency sweep for sample MG1-30

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0.1 1 10 100102

103

104

105

106

103

104

105

l*l

G' G"

Angular frequency, 1/s

Pa sPa

MG1-40

Figure 3.51. Frequency sweep for sample MG1-40

0.1 1 10 100102

103

104

105

106

103

104

105

l*l

G' G"

Angular frequency, 1/s

Pa sPa

MG1-50

Figure 3.52. Frequency sweep for sample MG1-50

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Frequency sweep (mechanical spectra) (figures 3.50, 3.51, 3.52) show

the stability of the protein – polysaccharide three-dimensional networks (gluten – starch networks), both dynamic moduli was parallel throughout the measured frequency range.

For protein – polysaccharide three-dimensional networks, frequency sweep evidences the network stability, the storage and loss modulus being almost parallel on the entire measuring domain. The two moduli are clearly dependent on frequency. The increase of dough gluten content diminishes both G’ and G” values and the complex viscosity [15]. The decrease of dynamic moduli determines a decrease of the network consistency and elasticity [16] because the polysaccharide particles are entrapped in a protein network with a greater flexibility. The variation of both moduli with frequency suggests the presence of a three-dimensional network with solid-like viscoelastic behavior [17,18]. The high values of the storage modulus G’, and the difference between G’ and G” are a clear indication for the formation of a stable network with high elasticity [3,4].

By applying the Carreau – Yasuda model on the experimental data of the frequency sweep for samples MG1-30, MG1-40 and MG1-50, the values of the zero shear viscosity can be calculated (table 3.33). The increase in the protein content of the network composition determines a decrease in the value of the zero shear viscosity. Table 3.33. Carreau – Yasuda parameters for samples: MG1-30, MG1-40 and

MG1-50 Sample Zero shaer

viscosity, η0 (Pa s)

Carreau – Yasuda parameters

Correlation factor

λ (sec) n R R2 MG1-30 2,31·107 474,54 0,066 0,921 0,849

MG1-40 4,87·106 474,54 0,15 0,876 0,767

MG1-50 2,53·106 474,54 0,207 0,939 0,883

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III.2.2.3.2. Gelatin – starch networks If analyzing the frequency sweep of the gelatin – starch networks (figure

3.55), we can deduce interesting observation about the influence of the added gelatin on the structural and rheological properties of the final system. At samples with gelatin amount greater than starch (MG2-AG6, MG2-AG7, MG2-AG8 and MG2-AG9), the added gelatin increases the stability and the degree of organization of the resulting gels.

G'

G"

MG2-A3 MG2-AG1 MG2-AG4 MG2-AG9 MG2-G

0.1 1 10 1001E-3

0.01

0.1

1

10

Angular frequency

Pa

1/s

Figure 3.55. Frequency sweep for sample: MG2-A3, MG2-AG1, MG2-AG4,

MG2-AG9 and MG2-G

The network stability and flexibility increases by adding the gelatin, results a pleasant texture and a soft feel. By adding a larger amount of gelatin, gels are soft and tend to “melt” under the mechanical action, the characteristic which is used to obtain the special desserts. It is important to note that by manipulating the ratio starch: gelatin it is possible to adjust the structure, the gel strength and thus the texture and the sensory perception of the product. The values of the storage modulus depend on the gelatin content in the starch: gelatin networks [20].

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III.2.2.5. Cosmetic emulsions

Frequency sweep is widely used rheological test in cosmetic products, especially cosmetic creams. These tests revealed a predominantly elastic behavior (solid-like) for all three samples with G’>G” values throughout the measured frequency range. Figures 3.60, 3.61 and 3.62 show the frequency variation of dynamic parameters (G’, G” and complex viscosity η*) for three analyzed samples.

Frequency sweep can be used to evaluate the sample consistency at rest, in other words, the long-term behavior, and the behavior of the separation of the dispersion (sedimentation, flotation or syneresis). In the case of stable dispersions and gels, the intermolecular interaction forces form a three-dimensional network. These materials exhibit the G’>G” throughout the measured frequency range. Therefore, the G’ and G” curve are parallel on the entire frequency range. The G’ value at low frequency (ω ≤ 0.1 rad/s) provides the information about the behavior “at rest” (G’0).

0.1 1 10 100102

103

104

105

103

104

105

l*l

G' G"

Angular frequency, 1/s

Pa sPa

MC1

Figure 3.60. Frequency sweep for MC1

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0.1 1 10 100101

102

103

104

105

102

103

104

l*l

G' G"

Angular frequency, 1/s

Pa sPa

MC2

Figure 3.61. Frequency sweep for MC2

0.1 1 10 100100

101

102

103

104

2x102

4x102

6x102

8x102

103

l*l G' G"

Angular frequency, 1/s

Pa s

Pa

MC3

Figure 3.62. Frequency sweep for MC3

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As can see from figures 3.60, 3.61 and 3.62, the G’ curve has a small slope. Based on experiments, it can be stated that if in the case of dispersions and gels we have G’>10 Pa at frequency of ω = 0.1 rad/s, then the material is stable. For all three samples, the G’0 is 2.450 Pa for MC1, 1.185 Pa for MC2 and 637 Pa for MC3, resulting a good stability for all three analyzed samples. By applying the Carreau – Yasuda model can determine the zero shear viscosity values (η0), these values can be correlated with the sensory perception of the creams (table 3.36). The highest value of the zero shear viscosity was obtained for MC1 (η0 = 1.25·106 Pa·s) and the lowest for MC3 (η0 = 2.3·105 Pa·s). These values correlate well with the tough perception of MC1 and the pleasant feeling of MC3 [19]. Table 3.36. Carreau – Yasuda parameters for samples: MC1, MC2 and MC3 Sample Zero shear

viscosity, η0 (Pa s)

Regression parameters Correlation factor

λ (sec) a n R R2 MC1 1,25·106 474,54 0,347 0,149 0,993 0,987

MC2 3,76·105 474,54 0,653 0,137 0,999 0,999

MC3 2,3·105 467,31 8,061 0,033 0,985 0,971

III.2.2.6. Conclusions

Frequency sweep provides valuable information about the internal structure, molecular weight and the long-term stability of analyzed compound. High values of the storage modulus suggest a stable internal network of force inside of the sample, which indicate a mechanical and structural stability. By applying the rheological models can be calculated zero shear viscosity, η0, and the characteristic relaxation time, λ, which can be correlated with molecular weight Mw, and the regression parameter a (from the mathematical expression of the Carreau – Yasuda model) can be correlated with polymer polydispersity. For polymer solutions, the frequency sweep provides the information about the effect of the colloidal forces and the interaction between particles. The stability of the protein – polysaccharide two- and three-dimensional networks is

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evidenced through frequency sweep tests, both dynamic moduli being parallel on the entire measured frequency range.

Selective bibliography 1. NOR, I., SANDU, V., IBĂNESCU, C., HURDUC, N., e-Polymers, v. 138, 2008 14. STEEPLESS, S., „Rheological characterization of four Kansas hard red winter wheat flour-water dough systems”, Thesis, Kansas State University, Manhattan, Kansas, 2010 19. IBĂNESCU, C., DANU, M., NANU, A., LUNGU, M., SIMIONESCU, B. C., Rev Roum. de Chim., v. 55, n. 11-12, p. 933-940, 2010 20. SIMIONESCU, B., IBĂNESCU, S. A., DANU, M., ROTARU, I., IBĂNESCU, C., Revista de Chimie, 2013

CHAPTER IV. ROTATIONAL TESTS – APPLICATIONS IN THE STUDY OF RELATIONSHIPS BETWEEN STRUCTURAL AND

RHEOLOGICAL PROPERTIES

IV. Chapter objectives The objectives of this chapter are:

- to achieve a deeper understanding of the rheological behavior of the analyzed samples;

- to highlight the both rheological behavior: Newtonian and pseudoplastic;

- to analyze the experimental data using rheological models: Carreau-Yasuda, Cross, Carreau, Krieger-Dougherty, Ostwald;

- to predict the sample viscosities according to the shear rate or shear stress by means of rheological models;

- to study of the influence of some factors (quaternization degree, the molecular weight, the solution temperature and concentration) of the measured rheological parameters.

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IV.2. Studies on different polymer systems IV.2.1. Polymer melts

Flow curves for samples MT1, MT2-10 and MT2-20 (figure 4.3) has been made at a temperature of 160 oC and has been shown the pseudoplastic behavior of these samples. The addition of PBMA in the solid polymer composition increases the system viscosity by about three orders of magnitude, such mixture has the property to cause the formation of the additional crosslink between the molecular chains of the system.

Experimental data were analyzed using rheological models (Cross, Carreau-Yasuda and Carreau), and the model parameters are summarized in table 4.2. These parameters are essential in achieving a structure – rheological correlation; the zero shear viscosity correlates with the molecular weight and the infinite shear viscosity with the polymer processability.

0.01 0.1 1 10 10010-2

10-1

100

101

102

103

104

105

106

Pa s

Viteza de forfecare, 1/s

MT1 MT2-10 MT2-20

Figure 4.3. Flow curve for sample: MT1, MT2-10 and MT2-20

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Table 4.2. Model parameters Cross, Carreau-Yasuda and Carreau for samples

MT1, MT2-10 and MT2-20 Sample Rheological

model Zero shear viscosity, η0

(Pa s)

Infinite shaer viscosity, ηinf

(Pa s)

R R2

MT1 Carreau-Yasuda

3453,8 5,0593·10-9 0,9316 0,8679

Carreau 204,19 5,0593·10-9 0,8396 0,7049 Cross 267,34 5,0593·10-9 0,7321 0,536

MT2-10 Carreau-Yasuda

491730 3,8294 0,8994 0,8090

Carreau 2,504·1017 3,8294 0,8994 0,8090 Cross - 2,652·10-6 0,9904 0,9810

MT2-20 Carreau-Yasuda

780260 95,963 0,9173 0,8414

Carreau 1,42·1016 1,457·10-5 0,8352 0,6977 Cross - 1,457·10-5 0,8106 0,657

IV.2.2. Polymer solutions From flow curves of the polymer solutions based on PSI-g-poly

(NIPAM-co-DMA) we can observe that the solution viscosity of the sample MS1 decreases slightly at low shear rate and then remain constant (figure 4.8). On the entire analyzed domain is also evidenced an increase of the shear stress. At shear rate greater than 10 s-1, the viscosity is constant. At a high shear rate prevail the hydrodynamic force and the viscosity of the polymer solution is independent of the size of the particles [2]. So, the polymer solution at low shear rate has a pseudoplastic behavior and at high shear rate (above 10 s-1) they have a Newtonian behavior [3].

To study the nature of the polysiloxane grafted thermosensitive solutions an analysis on the temperature influence on the viscosity was performed. So, the flow curves of the MS2 sample at two temperatures were compared; one temperature above LCST and one higher than the LCST (figure 4.9).

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1E-3

0.01

0.1

1

1 10 1001E-4

1E-3

0.01

MS1 1mg/ml

PaPa s

Viteza de forfecare1/s

Figure 4.8. Flow curve of sample MS1 1mg/ml

1 10 1001E-4

1E-3

0.01

0.1

MS2 1mg/ml25 oC 35 oC

Viteza de forfecare1/s

Pa s

Figure 4.9. Flow curves for MS2 1 mg/ml at two temperature: 25 oC and 35 oC

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At 25 oC is observed the two behaviors, pseudoplastic at low shear rate and Newtonian at high shear rate. At 35 oC, the temperature higher than the LCST, there is a pseudoplastic behavior mainly due to the dissolution of the intermolecular aggregates under the shear forces influence.

To describe the flow behavior of polymer solutions have been proposed the various rheological models (Carreau, Carreau-Yasuda, Cross, Krieger-Dougherty, Ostwald) which can be applied on the experimental data. The purpose of this model is to predict the viscosity of samples based on the shear rate or shear stress. In this study the rheological models were used to investigate the flow behavior of the polymer solutions and we were compared with each other in order to choose the best model that describes the experimental data. The equation which achieved the best correlation between experimental data and rheological model is the Ostwald model, with a correlation factor R2 ≈ 0,999, very close to 1, which means that the correlation is proper to describe the rheological behavior of the polymer solutions (table 4.12).

Table 4.12. Correlation factors R2 of the rheological models for the polymer solutions at 25 oC

Sample Correlation factor R2 Cross Carreau Ostwald Carreau–

Yasuda Krieger - Dougherty

MS1 0,318 0,304 0,9988 0,225 0,01 MS2 0,593 0,565 0,9996 0,542 0,17 MS3 0,269 0,497 0,9995 0,511 0,057 MS4 0,507 0,482 0,9993 0,46 0,085 MS5 0,56 0,52 0,9993 0,511 0,042

IV.2.4. Conclusions

The rheological tests have allowed studying the flow behavior of the polymer systems and the Newtonian and pseudoplastic behavior was evidenced. The experimental data were processed using the rheological models and were calculated the rheological characteristics depending on the shear rate and the shear stress, parameters absolutely necessary in the structure – rheological properties correlations. Of all rheological models, the Ostwald

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model achieved the best correlation between experimental data and the applied model, with the correlation factor R2 very close to 1.

Selective bibliography 2. WANG, H. H., LI, X. R., FEI, G. Q., MOU, J., eXPRESS Polymer Letters, v. 4, nr. 11, p. 670-680, 2010 8. MARANGOCI, N., ARDELEANU, R., URSU, L., IBĂNESCU, C., DANU, M., PINTEALĂ, M., SIMIONESCU, B. C., Beilstein J. Org. Chem., v. 8, p. 1610-1618, 2012

CHAPTER V. TEMPERATURE TESTS

V.1. Chapter objectives The objectives of this chapter are:

- to study the thermosensitive behavior of the compounds based on the polysiloxane grafted with PNIPAM and PDMA;

- to describe the association/dissociation phenomena of the thermosensitive polymer solutions under the temperature and strain effect;

- to study of the temperature influence on the viscoelastic behavior of the polymer solutions;

- to study the influence of factors (quaternization degree, concentration) of the viscoelastic behavior of the polymer solutions;

- to study the viscoelastic behavior of polymer at melting and hardening;

- to obtain the glass transition temperature values, Tg, of the polymer melts based on the rheological parameters (G’, G” and tan δ);

- the rheological study of the influence of the polysaccharide (starch) and protein (gluten, gelatin) content on the viscoelastic properties of the protein – polysaccharide three-dimensional network.

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V.2. Structural information for different types of polymer systems V.2.1. Polymer melts

For polymer melts, the temperature tests were carried out in the temperature range 30 – 270 oC, with a heating rate of 5 oC/min, at a constant frequency f = 1 Hz and a constant strain γ = 0.1 % (within the linear viscoelastic range). Initially, the samples were melted at 200 oC under the nitrogen atmosphere to prevent the thermal degradation and then were cooled to 30 oC.

The temperature tests allow determining the phenomena transition of polymers. Especially we study the polymer behavior at melting and at hardening obtaining thus the useful information about the structure type of the materials.

The glass transition temperature (Tg) is the point where the storage modulus G’ or the loss tangent peak (tan δ) decrease. Below this temperature, the macromolecules are immobile and G’ > G”. The polymer is present as a rigid and brittle solid. The temperatures higher than Tg causes an increase in the polymer chains mobility. In the glass transition domain, the material is in a high-elastic state. So, for temperature tests are three different methods to estimate the Tg values: maximum of the G” curve, maximum of tan δ or the inflection point of the G’ curve. So every time to obtain the Tg value the method which has been calculated must be mentioned.

A class of polymer melts studied using temperature tests are the samples MT2, MT2-10 and MT2-20 (figures 5.7, 5.8 and 5.9).

For these samples are observed a high-elastic plateau with G’>G” in the temperature range 130 oC – 230 oC. Using these figures we can calculate the yield point (Tm – melting point) as the temperature value at the junction of two dynamic moduli and the glass transition temperature Tg as the temperature value at the peak of tan δ (table 5.3).

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0.1

1

10

50 75 100 125 150 175 200101

102

103

104

105

106

107

tan () G'

G"

Temperatura, oC

Pa

MT2

Figure 5.7. Temperature test for MT2

0.01

0.1

1

10

50 75 100 125 150 175 200 225102

103

104

105

106

tan () G'

G"

Temperatura, oC

Pa

MT2-10

Figure 5.8. Temperature test for MT2-10

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0.1

1

10

75 100 125 150 175 200 225 250102

103

104

105

tan () G'

G"

Temperatura, oC

Pa

MT2-20

Figure 5.9. Temperature test for MT2-20

Table 5.3. Tm and Tg values for samples MT2, MT2-10 şi MT2-20 obtained

from temperature tests Sample MT2 MT2-10 MT2-20 Tm (G’=G”), oC 39,66 120,4 118,9 Tg (maximum tan δ), oC 50 126 124

V.2.2. Grafted polysiloxane solutions

Temperature test allows the study of the thermosensitive behavior of the compounds based on polysiloxane grafted PNIPAM and PDMA by highlighting the association phenomena at increasing temperature.

To achieve an increase in the LCST values, the PNIPAM was copolymerized with PDMA, a polymer with high hydrophilic character, which is an adjustment variant of the LCST [94]. We were synthesized the copolymers PSI-g-poly (NIPAM-co-DMA), the sample MS1 with a ratio NIPAM/DMA = 3.3/1 and the sample MS3 NIPAM/DMA = 1/1.3 respectively.

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20 30 40 50 60 701E-7

1E-6

1E-5

1E-4

1E-3

0.01

0.1

1

G'

G"

MS1 MS3

TemperaturaoC

Pa

Figure 5.17. Temperature tests for MS1 and MS3 (G’ and G”)

Increasing the polymer hidrophobicity will lead to a decrease in the

LCST value (48 oC for sample MS1), and by increasing the polymer hydrophilicity will obtain an increase in the LCST value (51 oC for sample MS3) (figure 5.17 and table 5.5) [87,92]. Table 5.5. Temperature transition values for compounds based on PSI-g-poly

(NIPAM-co-DMA) Sample Copolymerization ratio Transition temperature, oC

Tcolaps Tagregare TG’=G”

MS1 3.3 NIPAM/ 1 DMA - 48 51 MS2 NIPAM 33 33 59 MS3 1 NIPAM/ 1.3 DMA - 51 54

The purpose of these rheological tests is to provide a description the

temperature influence of the thermosensitive polymer solutions association/dissociation phenomena. At temperatures lower than LCST value,

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the solutions behavior is specific to a viscoelastic liquid, G”>G’. The polymers have a stable structure because the both dynamic moduli are approximately parallel on this temperature range. Below LCST value, the polymer is in an extended configuration due to the hydrogen bond between the amide groups and water molecules. At temperature above LCST value occur suddenly intermolecular aggregates. This phenomenon is highlighted by the sudden increase of the elastic modulus on the rheological curve reflecting an increase in the PNIPMA - PDMA interactions [93].

V.2.3. Two- and three-dimensional networks based on protein - polysaccharide

V.2.3.1. Gluten – starch networks For the protein – polysaccharide three-dimensional networks the

temperature is very important because these systems have different rheological behavior according to temperature.

The temperature tests for all analyzed samples are presented in figures 5.21 and 5.22 for the considered temperature domain (0-90 oC). Two processes are responsible of the thermal behavior of protein – polysaccharide three-dimensional networks: starch gelatinization and protein denaturation. Analysing the modification of G’ and G” with temperature a small decrease in both dynamic moduli is noticed up to a certain temperature is reached. Lower values for the dynamic moduli could be a result if the reduction of the interations in system. It was suggested a correlation of this phenomenon with the polysaccharide – protein (starch – gluten) interactions. The starch granules, initially entrapped as filler in the gluten network, reinforce the network when they swell. When the system is heated the starch granules escape the network, so a decrease of both moduli is noticed [95, 96]. Thus there is a slight fluidizing of the protein – polysaccharide three-dimensional networks due to the temperature and weakening links between proteins [97,98].

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0 10 20 30 40 50 60 70 80 90104

105

106

107 MG1-30 MG1-45 MG1-35 MG1-50 MG1-40 MG1-55

Temperatura, oC

G'

Pa

Figure 5.21. Temperature tests for samples: MG1-30, MG1-35, MG1-40,

MG1-45, MG1-50 şi MG1-55 (the storage modulus G’)

The absorbed water is released and a minimum for G’ and G” is reached. Once the minimum is reached, both loss and storage modulus begin to increase to a maximum value. This stage corresponds to complete polysaccharide (starch) gelatinition and protein denaturation and the network is completely developed. The protein content has a higher influence in the initial heating stages while the starch gelatinition has a greater influence after the inflexion points of the dynamic moduli.

The temperature characteristic for the inflection point in the increase in G’ and G” may be related to the rise in viscosity due to amylase escaping from granules and forming a gel. Increasing gluten content has a significant influence on the crosslinking process after starch gelatinization. The resulting network is more stable and has increased mechanical properties and structure stability [96].

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0 10 20 30 40 50 60 70 80 90

104

105

106

MG1-30 MG1-45 MG1-35 MG1-50 MG1-40 MG1-55

Temperatura, oC

G"

Pa

Figure 5.22. Temperature tests for samples: MG1-30, MG1-35, MG1-40,

MG1-45, MG1-50 şi MG1-55 (loss modulus G”)

At high temperature (above the gelatinization temperature of the protein – polysaccharide three-dimensional networks) the systems become solid and the storage modulus G’ are much higher than G” [94,95]. This transition of three-dimensional network in a solid state can be caused by breaking sulfhydryl/disulfide bonds [99] or by the destruction of starch granules and the formation of amylase matrices or gels coupled with denaturating process of proteins [95]. At high temperature, gelatinized starch show a considerable influence on the viscoelastic properties of protein – polysaccharide three – dimensional networks.

Increase in G’ values can be attributed to the interactions of the induced protein (gluten) crosslinks during the formation of network structure. Protein – protein interactions increase the crosslinking degree resulting higher G’ values than of G”. The polysaccharides (starch) gelatinization, the protein crosslinking

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or both are the most accepted explanation for heat – induced rheological changes [100]. The viscosity and the storage modulus G’ values are increased by the amylose and amylopectin released from the starch particles. One of the possible effects of gelatinization can be the increase of the hydrogen bonds between the gluten polypeptides and starch molecules. As noted some researchers [100], the normal content of starch in the starch – gluten three – dimensional networks has a little effect on the storage modulus G’, however, the changes of G’ at high temperature are proportional to the content of starch in the system.

Dynamic rheological tests on the polysaccharide – protein three –dimensional networks are important to evaluate the quality of the final product and to establish the correlations between the fundamental rheological tests and the system composition. In conclusions, the starch granules are responsible for the emphasis of three –dimensional networks nonlinear behavior [102]. The quantity and quality of proteins greatly influences the rheological behavior of systems even if the oscillatory tests at small strain depend on the starch – starch and starch – protein interactions.

V.2.3.2. Gelatin – starch networks Important modifications are induced by the increase of gelatin content in

the composite gels (figure 5.25). The G’ and G” curves evolution suggests intermediate behaviors between classical curves characteristic for starch based gels and those of gelatin based gels, an indication of modification in a matrix structure. Sample MG2-A3 (starch) is characterized by a stable solid-like structure, with dynamic moduli G’ and G” almost parallel for the entire investigated temperature domain, while sample MG2-G (containing only gelatin) presents a characteristic stage of gel hardening at lower temperatures and a melting point situated around 27oC [104]. At the melting point, gelatin undergoes a helix-coi1 transition and thus the gel network collapses. In the case of starch – gelatin composite gels the gelatin is more rigid than the starch filler systems, thus, the moduli would be expected to be higher than for starch gels.

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G'

G"

MG2-A3 MG2-AG1 MG2-AG4 MG2-AG9 MG2-G

10 20 30 40 50 60 70 800.01

0.1

1

10

100

1000

10000

Temperature (oC)

Pa

Figure 5.25. Temperature tests for samples: MG2-A3, MG2-AG1, MG2-AG4,

MG2-AG9 şi MG2-G

Figure 5.25 shows the influence of gelatin content on the rheological characteristics of the system; when the gelatin content is increased the gelatin begins to dominate the rheology of the system with the characteristic increase in the gel rigidity at lower temperatures. The resulting curves for starch-gelatin indicate that the gelatin biopolymer dominates the rheology of the system up to a 8 : 2 starch to gelatin ratio determining a pronounced increase in storage and loss modulus under the melting temperature of gelatin. Above the melting temperature of gelatin the network structure is not destroyed, but the gel becomes softer and more flexible. Even if for large amounts of gelatin (starch - gelatin ratio = 1:9 – sample MG2-AG9) the two dynamic moduli are parallel and G’ is more than one order of magnitude higher than G”. Melted gelatin may act as a plasticizer of the whole network. This behavior is a result of the competitiveness between the two biopolymers for the continuous phase of the composite system and the way in which the free water is entrapped in a less or more densely packed network. For intermediate composition interpenetrated

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starch and gelatin network are developed. For samples with higher gelatin content a clear melting temperature of the gelatin phase could be evidenced [105].

V.2.4. Conclusions The study of the thermosensitive behavior of systems based on

polysiloxane grafted PNIPAM and PDMA was performed using the temperature test. In addition, these tests can explain the association/dissociation phenomenon under the temperature and shear strain action in the thermosensitive polymer solutions. Due to the complex interactions, the LCST of thermosensitive polymer solutions is a temperature range which for a given solvent will depend on several factors: concentration, molecular weight, the nature of the end groups, the comonomers content, etc. Viscoelastic behavior of the polymer to the melting or curing was studied using the temperature tests and the glass transition temperature by measuring rheological parameters was obtained. The influence of the polysaccharide and the protein content on the rheological properties of protein – polysaccharide bi- and three – dimensional networks by temperature tests was evidenced.

Selective bibliography 96. DANU, M., ROTARU, I., IBĂNESCU, C., HURDUC, N., IBĂNESCU, S. A., SIMIONESCU, B. C., Environmental Engineering and Management Journal, v. 11, n. 11, p. 1883-1888, 2012 98. MOREIRA, R., CHENLO, F., TORRES, M. D., International Journal of Food Science and Technology, v. 46, p. 2085-2095, 2011 102. YANG, Y., SONG, Y., ZHENG, Q., J. Food Sci. Technol., v. 48, n. 4, p. 489-493, 2011 105. SIMIONESCU, A. B., IBĂNESCU, S. A., DANU, M., ROTARU, I., IBĂNESCU, C., Revista de Chimie, 2013

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CHAPTER VI. TIME TESTS

VI.1. Chapter objectives Time tests are used to study the long-term stability of analyzed samples.

But the main objective of this chapter is to develop a monitoring of polymerization reactions with these tests.

VI.2. Structural information for polymer melts To highlight the influence of solid phase composition on the chemical

and physical processes that occur during the curing process of the polymer composition, we were comparing the rheological test for each of analyzed formulations without activator (to evidence the physical processes) and with the activator.

To determine whether the composition of solid phase polymer systems influences physical and chemical processes that occur during curing polymer the useful separate analysis of these processes was considered. The first group in which all components of the system have been introduced with the exception of the activator (DHEPT), in order to emphasize the influence of solid phase composition on the physical processes. In the second group, we have been introduced all system components, including the activator DHEPT, in order to follow the combined influence of the two groups of processes.

Figure 6.4 shows the time dependence of the complex viscosity (η*) for polymer systems MT1, MT2-10 and MT2-20, formulated without activator. Analyzing the evolution of these diagrams we conclude that for all these systems the complex viscosity increase with increasing the duration contact between the solid and liquid phase.

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0 100 200 300 400 500 600 700 800

0

250

500

750

1000

1250

1500

1750

2000

MT2-10 fara activator MT2-20 fara activator MT1 fara activator

sTimp

ll

Pa s

Figure 6.4. Time dependence of the complex viscosity for samples: MT1, MT2-

10 şi MT2-20, formulated without activator

The difference between the evolutions of complex viscosity for the analyzed systems due to different characteristics (molecular weight, particle distribution and size) of the polymers which it is the solid phase. The lower complex viscosity values of the samples MT2-10 and MT2-20, with only the copolymer in composition, is explained by the fact the polymer particles being larger are solvated and slowly dissolves in the liquid phase of the MMA.

Figure 6.5 shows the time dependence of the complex viscosity for analyzed polymer systems formulated with an activator (DHEPT). These diagrams show an initial stage in which the complex viscosity of analyzed mixture is growing relatively slow because the small particles are dissolved and large particles are solvated and then the complex viscosity increase due to the fast polymerization of MMA. The duration after which the sharp increase of the complex viscosity shows up is depending on the solid phase content.

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0 100 200 300 400 500 600 700 800 900

0

2000

4000

6000

8000

10000

MT2-10 cu activator MT2-20 cu activator MT1 cu activator

sTimp

ll

Pa s

Figure 6.5. Time tests for samples MT1, MT2-10 şi MT2-20 formulated with

activator

VI.3. Conclusions In conclusion, we performed a good monitoring of the polymerization

reaction using the time tests. Also, the time tests revealed the influence of polymer system composition and activator on the polymerization in-situ monitored on the rheometer.

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CHAPTER VII. RHEO –SALS – THE APPLICATIONS IN THE CORRELATIONS BETWEEN STRUCTURE AND RHEOLOGICAL

PROPERTIES

VII.1. Chapter objectives The objectives of this chapter are:

- the detailed investigation of structural – rheological properties relationships for complex fluids;

- to simultaneously obtain the structural information and rheological data.

VII.3. Applications in the study of grafted polysiloxane polymer

solutions For sample MS5, PSI-g-(NIPAM-co-DMA), the maximum intensity of

scattered light is reached at 40.2 oC (figure 7.1). After this temperature, the size of the aggregates decreases (see Rheo-SALS images).

36 oC 36,4 oC 36,7 oC 40,2 oC 41,7 oC 46,7 oC 55,5 oC Figure 7.1. Scattered light intensity of sample MS5, 1mg/ml, obtained from

Rheo-SALS In the polymer solution MS5 at room temperature, the PNIPAM chains

are easily solubilized in water. So, the amphiphilic block copolymer will assemble into core-shell micelles with the PDMA core and PNIPMA shell. The PNIPAM chains will extend through water molecules and the PDMA chains will form the micelle core. By increasing the temperature above the critical value (40 oC), the hydrogen bonds between water and polymer will break and PNIPAM becomes hydrophobic. At that moment, the aggregation phenomena appear and the PNIPAM chains will try to avoid the contact with water. At higher temperatures (55 oC) the uniform aggregate derived from the balance of the intermolecular hydrophobic interactions form (figure 7.2) [5].

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20 25 30 35 40 45 50 55 600.01

0.1

1

10

55,5oC

46,7oC

41,7oC

40,2oC

36,7oC

36,4oC

G' G"

Temperatura, oC

MS5 1mg/ml

36oC

Figure 7.2. Temperature test and the Rheo-SALS images for sample MS5

It is noted in figure 7.2 that around temperature 40 oC the formation of

the intermolecular aggregates occurs as a result of increases in temperature and strain, and the amount of scattered light intensity is higher. Above this temperature, the intensity decreases as a result of the breaking of the intermolecular bonds due to the action of temperature and shear forces.

VII.4. Conclusions Rheo-SALS is an innovative technique to determine the LCST value of

the polymer solutions of polysiloxane grafted with PNIPAM and PDMA. This technique allows the combination of SALS and rheometer devices, thereby achieving a direct correlation between the rheological behavior and microstructure of the sample. Rheological measurements provide information about the macroscopic behavior, and Rheo-SALS provide additional information about the internal structure of the sample.

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Selective bibliography

4. LAUGER, J., HEYER, P., PFEIFER, G., Annual Transactions of the Nordic Rheology Society, v. 12, p. 137-140, 2004 5. TANG, T., CASTELLETO, V., PARRAS, P., HAMLEY, I. W., KING, S. M., ROY, D., PERRIER, S., HOOGENBOOM, R., SCHUBERT, S., Macromol. Chem. Phys., v. 207, p. 1718-1726, 2006

GENERAL CONCLUSIONS

Thesis “Relationships between structure and rheological properties in polymer systems” has 291 pages and is divided into seven chapters that include 71 tables, 197 figures, 5 schemes and 360 bibliographic information. Studies of this thesis focused on achieving a correlation between structure and rheological properties of the studied compound classes and in monitoring how the rheological “footprint” gives us the valuable information about the structure, resulting in the following conclusions: Amplitude sweep was used to determine the limits of linear viscoelastic

range for studied systems, to analyse the influence of the certain factors (temperature, concentration) on the rheological parameters, to obtain the information about the mechanical stability and to establish a correlation between the structure and rheological properties of studied systems.

Both dynamic moduli, storage and loss modulus, show a linear behavior only at very small deformations. Such susceptibility to small deformation is attributed to the fragile structure of the network which has a low resistance to external strain.

For nonlinear viscoelastic behavior (pseudoplastic behavior), both dynamic moduli have similar strain dependence. This behavior can be interpreted by the internal structure destruction and rebuilding in response to external stimuli.

In the linear viscoelastic range, the greater values of the storage modulus than the loss modulus suggest that the studied systems have a rheological behavior predominantly elastic at the expense of viscous properties.

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For some studied systems, the difference between the two dynamic moduli gradually decreases with increasing deformation, and thereafter in the large deformation range the viscous behavior becomes higher than the elastic properties.

The material response at large strains can provide valuable information to better understand the complicated rheological behavior of semi-solid material.

Frequency sweep was used for polymer systems, especially due to its ability to measure the changes in the elastic and viscous behavior of the material. Also, we were obtained the important information about the internal structure, molecular weight and long-term stability. Frequency sweep provides opportunities for good correlation between viscoelastic behavior and material composition.

Rotational tests provided an opportunity to achieve a deeper understanding of the flow behavior of the analyzed samples, to highlight the both rheological behavior (Newtonian and pseudoplastic), to analyze the experimental data using rheological models (Carreau-Yasuda, Cross, Carreau, Krieger-Dougherty, Ostwald), to predict the sample viscosities according to the shear rate or shear stress by means of rheological models and to study the influence of some factors (quaternization degree, the molecular weight, the solution temperature and concentration) of the rheological parameters. Rheological models allow calculating the viscoelastic parameters; these parameters are absolutely necessary in the structure - rheological properties correlations.

The novelty of this study is analyzing of rheological models used to determine the rheological equation that achieved the best correlation between experimental data and model; this equation is Ostwald model with a correlation coefficient R2=0,999, very close to 1, which implies that this correlation is very suitable to describe the rheological behavior of the polymer solution.

Temperature tests are an innovative technique to study the thermosensitive behavior of polymer systems based on polysiloxane grafted with PNIPAM and PDMA, and allowed to describe the association/dissociation phenomena of the thermosensitive polymer

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solutions under the temperature and strain effect, and to study of the temperature influence on the viscoelastic behavior of the polymer solutions. Also, through these tests was performed an analysis of the factors influence (quaternization degree, concentration) on the rheological parameters, we have studied the viscoelastic behavior of polymer at melting and hardening and we have obtained the glass transition temperature values, Tg, of the polymer melts based on the rheological parameters (G’, G” and tan δ), we have analyzed the study of the influence of the polysaccharide (starch) and protein (gluten, gelatin) content on the viscoelastic properties of the protein – polysaccharide three-dimensional network.

The rheological behavior of thermosensitive polymers is influenced by molecular weight, hydrolysis degree, type and content of the hydrophobic groups, temperature and salinity.

The LCST of thermosensitive polymers is not only one characteristic value. Due to the complex interactions, the LCST is a temperature range which for a given solvent depends on the concentration, molecular weight, the nature of the end group, the comonomers content and distribution along the chain.

Dynamic rheological tests on the polysaccharide – protein three – dimensional networks are important for assessing the final product quality and to establish the relations between fundamental rheological tests and composition system. Starch granules are responsible for increase the nonlinear behavior of three – dimensional networks. The protein quantity and quality greatly influence the viscoelatic behavior, even if the oscillatory measurements at small strain are dependent on the starch – starch and starch – protein interactions.

The time test proved to be a specific rheological method for monitoring the polymerization reactions.

Rheo-SALS allowed to obtain structural information together with rheological experimental data and also allowed to perform a detailed investigation of the relationship structure – rheological properties of studied systems.

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The original results of this PhD thesis have been published in 13 papers (9 ISI papers) and 15 communications:

Published papers: 3D- Physical network based on gelatin and azo-polysiloxanes, Iulian

Rotaru, Luiza Epure, Elena Resmerita, Maricel Danu, Nicolae Hurduc, Constanţa Ibănescu, e-Polymers, 2013 (submitted)

Rheology of gelatin – starch. I. Influence of system composition, Ana Bogdana Simionescu, Sorin Alexandru Ibănescu, Maricel Danu, Iulian Rotaru, Constanţa Ibănescu, Revista de Chimie, 64 (8), 909-913 (2013)

Stimuli responsive graft polysiloxanes, Anca Daniela Rusu, Constanţa Ibănescu, Elena Resmeriţă, Bogdana Simionescu, Maricel Danu, Vlad Hurduc, Sorin Alexandru Ibănescu, Revista de Chimie, 64 (6), 667-671 (2013)

Ionically and covalently crosslinked hydrogels based on gelatin and chitosan, A.N. Jătariu, M. Danu, C. A. Peptu, G. Ioanid, C. Ibănescu, M. Popa, Soft Materials, 11 (2013), 45-54,

Gluten content influence on rheological behavior of starch-gluten networks, Maricel Danu, Iulian Rotaru, Constanţa Ibănescu, Nicolae Hurduc, Sorin Alexandru Ibănescu, Bogdan C. Simionescu, Environ. Eng. Manage. J., 11 (2012), 1883-1888

Polysiloxane ionic liquids as good solvents for β-cyclodextrin-polydimethylsiloxane polyrotaxane structures, Narcisa Marangoci, Rodinel Ardeleanu, Laura Ursu, Constanţa Ibănescu, Maricel Danu, Mariana Pinteală, Bogdan C. Simionescu, Beilstein J. Org. Chem., 8, 1610-1618, 2012

Thermo-sensitive polymers based on graft polysiloxanes, Anca Daniela Rusu Hodorog, Constanţa Ibănescu, Maricel Danu, Bogdan C. Simionescu, Licinio Rocha, Nicolae Hurduc, Polym. Bull., 69 (5), 579-595 (2012)

Rheogical modifiers of natural origins used in cosmetic formulations, Andrei Roşu, Maricel Danu, Gina Amărioarei, Alina Nanu, Constanţa Ibănescu, Maria Lungu, Bul. Inst. Polit. Iaşi, 2011, Tom LVII (LXI), Fasc. 1, 53 – 63

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Stability of disperse systems estimated using rheological oscillatory shear tests, Constanţa Ibănescu, Maricel Danu, Alina Nanu, Maria Lungu, Bogdan C. Simionescu, Revue Roumaine de Chimie, 2010, 55(11-12), 933-940

Rheological behavior of some cosmetic systems in oscilatory shear, Alina Nanu, Maria Lungu, Constanţa Ibănescu, Maricel Danu, Andrei Roşu, Revista SRCC, volumul 9, Nr. 1-2 / 2009

Rheological characterization of binders for alkyd resin coatings, Constanţa Ibănescu, Maricel Danu, Sorin Alexandru Ibănescu, Maria Lungu, Bogdan C. Simionescu, Journal of Colloid and Surface Chemistry, volum 8, nr. 2, 2008

Testele reologice în aplicaţii cosmetice, Maria Lungu, Constanţa Ibǎnescu, Alina Nanu, Maricel Danu, Sorin Ibǎnescu, Revista SRCC, volumul 8, Nr. 1, martie 2008

Oral communications:

Centenary of education in chemical engineering, Romania, Iasi, 28 – 30 November, 2012, „Gluten content influence on rheological behavior of starch-gluten networks”, Maricel Danu, Iulian Rotaru, Constanţa Ibănescu, Nicolae Hurduc, Sorin Alexandru Ibănescu, Bogdan C. Simionescu

Centenary of education in chemical engineering, Romania, Iasi, 28 – 30 November, 2012, „Amphiphilic graft polysiloxanes capable of self-assembling into thermo-sensitive micelle”, Anca Daniela Rusu, Maricel Danu, Constanţa Ibănescu, Nicolae Hurduc, Licinio Rocha

Fourth Cristofor I. Simionescu Symposium, Frontiers in Macromolecular and Supramolecular Science, May 31 – June 1, 2011, Iasi, Romania, „Viscometric and rheological behavior of some pendant polycations as a function of charge density”, Ionel Adrian Dinu, Maricel Danu, Constanţa Ibănescu, Ecaterina Stela Drăgan

Dynamics of Complex Fluids, May 5-7, 2011, Iaşi, Romania, „Viscometric and rheological behavior of progressively quaternized poly(dimethylaminoethyl methacrylate) as a function of charge

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density”, Ionel Adrian Dinu, Maricel Danu, Constanţa Ibănescu, Ecaterina Stela Drăgan

Zilele Facultăţii de Inginerie Chimică şi Protecţia Mediului, Ediţia a VII-a, Iaşi, 17-19 noeimbrie 2010, „Caracterizarea reologică a unor derivaţi de chitosan pentru tratarea la suprafaţă a hârtiei”, Mihai Lupei, Maricel Danu, Raluca Nicu, Constanţa Ibănescu, Elena Bobu

Zilele Facultăţii de Inginerie Chimică şi Protecţia Mediului, Ediţia a VII-a, Iaşi, 17-19 noiembrie 2010, „Modificatori reologici de origine naturală utilizaţi în formulări cosmetice”, Andrei Roşu, Maricel Danu, Gina Amărioarei, Constanţa Ibănescu, Maria Lungu

1-st SRR – Summer School of Rheology, Cluj-Napoca, 26 – 29 august, 2010, „Structure – rheological properties relation in polymeric systems”, Maricel Danu, Constanţa Ibănescu, Bogdan C. Simionescu

International Conference Biomaterials and Medical Device, Bucharest, 13 – 16 november 2008, „Hydrogel based on p(HEMA) with application in tissue engineering of articular cartilage”, L. Bostan, M. I. Popa, C. Ibănescu, M. Danu, L. Verestiuc

Posters:

The X Romanian International Symposium on Cosmetic and Flavor Products, May 31 – June 3, 2011, Iasi, Romania – poster, „Poly(vinyl alcohol), Pectin and Carrageenan based mixed gels”, Andrei Roşu, Maricel Danu, Gabriela Andrei, Camelia Mihăilescu, Maria Lungu

Dynamics of Complex Fluids, May 5-7, 2011, Iaşi, România – poster, „Rheological characteristics of some polymer systems used as vehicles for cosmetic and household actives”, Andrei Roşu, Constanţa Ibănescu, Maricel Danu, Maria Lungu

Al IX – lea Simpozion Internaţional de Produse Cosmetice şi Aromatizante, 2 – 5 iunie 2009, Iaşi, România – poster, „Proprietăţile reologice şi atributele senzoriale ale unor produse de îngrijire a pielii”, Alina Nanu, Maria Lungu, Constanţa Ibănescu, Gabriela Andrei, Maricel Danu

Second Cristofor I. Simionescu Symposium, Frontiers in Macromolecular and Supramolecular Science, 1 iunie, Bucureşti, 2 -3 iunie, 2009, Iaşi,

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România – poster, „Rheological properties of modified polysiloxanes sensitive to external stimuli”, Iulian Nor, Anca Daniela Rusu, Maricel Danu, Vlad Hurduc, Gabriela Lisa, Maria Bercea, Constanţa Ibănescu

International Conference on Materials Science and Engineering, 26 – 28 februarie, Bramat 2009, Braşov – România, poster, „Thermo-rheological studies of different types of gluten”, Maricel Danu, Constanţa Ibănescu, Bogdan C. Simionescu, Georgiana Codină

A XXX-a Conferinţă Naţională de Chimie, 08-10 octombrie 2008, Călimăneşti-Caciulata, România, poster, „Studii asupra comportării reologice a glutenului”, Maricel Danu, Georgiana Codină, Constanţa Ibănescu, Dan Scutaru