Introduction The rheology of two different semi-rigid “rod-like” polysaccharides in aqueous solutions, Xanthan gum (XG, Ketrol TF from Kelco) and Scleroglucan.

Slides:



Advertisements
Similar presentations
21 November 2007 Phys. Sc. & Engin. Grad School, Cardiff VISCOELASTIC FLUIDS: A BRIEF DESCRIPTION AND SOME MAIN FEATURES EXTRUDATE SWELL EXTRUDATE SWELL.
Advertisements

Workshop series 2013 SJU-AAPS Student Chapter St. John’s University Oct , 5:00 PM Tapan Parikh St. John’s University, Queens, New York
FINITE ELEMENT ANALYSIS OF MEMBRANE ACTION IN STEEL DECK PLATES AND FIBROUS CONCRETE SLABS.
STATICALLY DETERMINATE STRESS SYSTEMS
Luis Bastardo-Zambrano Lubricants Russia – Use of Super Heavy Naphthenics in Lubricant Formulations Luis Bastardo-Zambrano, PhD Nynas.
Microbial polysaccharides
UNIT 13 : HEAT 13.1 Thermal Conductivity 13.2 Thermal Expansion.
Introduction to Viscoelasticity
Stress Relaxation of Comb Polymers Keith M. Kirkwood a, Dimitris Vlassopoulos b,c, and L. Gary Leal a a Department of Chemical Engineering, University.
Rheological evaluation of the mechanical properties of equine synovial fluid from tarsocrural joints injected with hyaluronic acid (HA) Heidi Schmidt Advisors:
On the extensional rheology of human blood R J Poole a, A Swift a, T V How b a Department of Engineering, University of Liverpool, Brownlow Hill, Liverpool,
Utilizing rheological methods to examine mechanical properties of a triblock copolymer at the water/oil interface Jerome Nash and Prof. Kendra Erk Surface.
II. Properties of Fluids. Contents 1. Definition of Fluids 2. Continuum Hypothesis 3. Density and Compressibility 4. Viscosity 5. Surface Tension 6. Vaporization.
A unified normal modes approach to dynamic tides and its application to rotating stars with realistic structure P. B. Ivanov and S. V. Chernov, PN Lebedev.
Results References [1].Mendoza, J. D. Lab 9: Dynamic Mechanical Analysis, Iowa State University Time-Temperature Superposition (TTS) Using DMA Acknowledgments.
CE 230-Engineering Fluid Mechanics Lecture # 4and5 Fluid properties (2)
Turbulent flow of non-Newtonian liquids through an axisymmetric sudden expansion Rob Poole Department of Engineering, University of Liverpool Osborne Reynolds.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
EBB 220/3 PRINCIPLE OF VISCO-ELASTICITY
Fluid mechanics 3.1 – key points
Mechanics of Materials II
Jens Eggers Polymer threads: formation and instability.
CHAPTER TWO SOIL COMPRESSION.
By: Tina Coop and Priscilla Nguyen A closer look at the flow patterns of shampoos, conditioners, and gels.
Dispersed Systems FDSC Version. Goals Scales and Types of Structure in Food Surface Tension Curved Surfaces Surface Active Materials Charged Surfaces.
Reference Manual Chapter 9
Extensional viscosity measurements of drag-reducing polymer solutions using a Capillary Break-up Extensional Rheometer Robert J Poole , Adam Swift and.
T. A. Kowalewski A. L. Yarin S. Błoński NANOFIBRES
Rheological and Molecular Characterization of Equine Synovial Fluid
PTT 204/3 APPLIED FLUID MECHANICS SEM 2 (2012/2013)
Copyright © 2010 Pearson Education South Asia Pte Ltd
Chapter Six Non-Newtonian Liquid.
Poisson’s Ratio For a slender bar subjected to axial loading:
CE 230-Engineering Fluid Mechanics Week 1 Introduction.
Microbial polysaccharides. During the Second World War (1940), the usefulness of microbial polysaccharides was recognized with the discovery of dextran.
Chapter Five Vibration Analysis.
Mass Transfer Coefficient
Poisson’s Ratio For a slender bar subjected to axial loading:
The Hong Kong Polytechnic University Optics 2----by Dr.H.Huang, Department of Applied Physics1 Diffraction Introduction: Diffraction is often distinguished.
CTC / MTC 222 Strength of Materials Chapter 1 Basic Concepts.
Polish Academy of Sciences Institute of Fundamental Technological Research Break-up of liquid jet in co-flow experimental.
What is Fluid????? A fluid may be liquid, vapour or gas. It has no permanent shape but takes up the shape of a containing vessel or channel or is shaped.
Yield point and yield stress or strength,  y Offset method finds this yield stress by assuming a 0.2 % strain (.002).002 Big yielding region, large elongation.
Polymer Properties Exercise 4.
Efficient control of the bulk and surface rheological properties by using C8-C18 fatty acids as co-surfactants Zlatina Mitrinova,1* Zhulieta Popova,1.
Introduction to Manufacturing Technology –Lecture 4
Strength of Materials Malayer University Department of Civil Engineering Taught by: Dr. Ali Reza Bagherieh In The Name of God.
INTRODUCTION Strain gauge measurement is a point strain measurement method developed in the USA c.a independently by E. Simmons and A. Ruge. It.
Cyclic plastic deformation and damage in 304LN stainless steel --Surajit Kumar Paul et al. Reporter: Yong Wang Supervisor: Professor Xu Chen.
1 Oldroyd B Model Bead formation in filament stretching Stretching phase Capillary thinning phase Connection between the bead and filament becomes unstable.
Rheology At the completion of this section the student will be able to: describe Newtonian behaviour; illustrate and explain 3 different kinds of non-Newtonian.
Origin of strain hardening in melt extension Shi-Qing Wang, University of Akron, DMR Polymer melts with long chain branching show “strain hardening”
Short introduction into rheology
EBP 200/3 POLYMER RHEOLOGY DR AZURA A.RASHID Room 2.19 School of Materials And Mineral Resources Engineering, Universiti Sains Malaysia, Nibong Tebal,
©2007 John Wiley & Sons, Inc. M P Groover, Fundamentals of Modern Manufacturing 3/e MECHANICAL PROPERTIES OF MATERIALS 1.Hardness 2.Effect of Temperature.
Polymer Properties Exercise 4.
Dynamic mechanical analysis
Results and Discussion
Poisson’s Ratio For a slender bar subjected to axial loading:
Chapter 15 Oscillations.
Thin Walled Pressure Vessels
Poisson’s Ratio For a slender bar subjected to axial loading:
VISUAL AIDS for instruction in VACUUM TECHNOLOGY AND APPLICATIONS
326MAE (Stress and Dynamic Analysis) 340MAE (Extended Stress and Dynamic Analysis)
Material Testing.
Poisson’s Ratio For a slender bar subjected to axial loading:
Chapter 8 Introduction and Basic Fluid Properties
E =
Nanoscale Characterization for Improving Turbulent Drag Reduction with Polymers Matthew W. Liberatore, Department of Chemical Engineering, Colorado School.
Mathias Sander, Heike Dobicki, Albrecht Ott  Biophysical Journal 
Presentation transcript:

Introduction The rheology of two different semi-rigid “rod-like” polysaccharides in aqueous solutions, Xanthan gum (XG, Ketrol TF from Kelco) and Scleroglucan (SG, Tinocare GL from Ciba) were measuredover a wide range of concentration (0.01% % w/w). Xanthan gum is a polyelectrolyte produced using the bacterium Xanthomonas campestris. Scleroglucan is a non-ionic polysaccharide produced by the fungi of genus Sclerotium. The molecular weights of the polymers are reported by the suppliers to be in excess of 10 6 g/mol. The rheology of two different semi-rigid “rod-like” polysaccharides in aqueous solutions, Xanthan gum (XG, Ketrol TF from Kelco) and Scleroglucan (SG, Tinocare GL from Ciba) were measured over a wide range of concentration (0.01% % w/w). Xanthan gum is a polyelectrolyte produced using the bacterium Xanthomonas campestris. Scleroglucan is a non-ionic polysaccharide produced by the fungi of genus Sclerotium. The molecular weights of the polymers are reported by the suppliers to be in excess of 10 6 g/mol. XANTHAN GUM SCLEROGLUCAN Steady and oscillatory shear measurements Plotting  o versus concentration provides a convenient way of estimating c *, the so-called critical overlap concentration, for both polymers. Below c *, which for XG is approximately 0.067% (670 ppm) and for SG, 0.019% (190 ppm), both solutions are dilute and  o scales approximately as c 1.44, above the critical overlap concentration, interactions between the molecules occur and  o increases much more rapidly with concentration. SCLEROGLUCAN In this simple technique a cylindrical liquid bridge of the ‘test’ liquid is formed between two circular plates 4 mm in diameter. An axial step strain is then applied (i.e. the end plates are rapidly pulled apart to a fixed separation) which results in the formation of an elongated liquid thread. The thread diameter reduces due to surface tension and information about the extensional properties of the liquid can be deduced from the evolution of the filament midpoint diameter which is monitored using a laser micrometer. A simple one-dimensional analysis, neglecting axial curvature and assuming that the filament is axially uniform, shows that the filament can be characterised simply by its midpoint diameter: Alternatively you may calculate a Hencky strain at the midpoint, the strain rate and estimate an apparent ‘extensional viscosity’: Trouton ratio is calculated from: Newtonian-like linear thinning of the filament was observed sometime later after the initial step strain Steady uniaxial extensional viscosity increases with concentration The magnitude of the Trouton ratio confirms the non-Newtonian behaviour of both polymers as Tr >>3. However, the Trouton ratio exhibits a decrease in magnitude with increasing concentration Steady shear, small amplitude oscillatory shear and capillary break-up extensional rheology measurements of rod-like polymers Azuraien Robert J. Poole Department of Engineering, University of Liverpool, Brownlow Street, Liverpool, L69 3GH United Kingdom Methods Steady and oscillatory shear measurements TA Instrument Rheolyst AR 1000N controlled stress rheometerTA Instrument Rheolyst AR 1000N controlled stress rheometer Small amplitude oscillatory shear (SAOS) measurements only possible for higher concentration solutionsSmall amplitude oscillatory shear (SAOS) measurements only possible for higher concentration solutions All SAOS measurements were conducted in linear viscoelastic regionAll SAOS measurements were conducted in linear viscoelastic region Capillary break-up measurements ThermoHaake capillary break-up extensional rheometer (CaBER) with laser micrometer (resolution~10  m)ThermoHaake capillary break-up extensional rheometer (CaBER) with laser micrometer (resolution~10  m) High-speed digital imaging using Dantec Dynamics Nano Sense MKIII high-speed camera at 2000 frames per second with Nikon 60mm f/2.8 lensHigh-speed digital imaging using Dantec Dynamics Nano Sense MKIII high-speed camera at 2000 frames per second with Nikon 60mm f/2.8 lens Conclusions G  is greater than G until the crossover frequency, which increases as the concentration decreases indicating that the behaviour corresponds to semi-rigid polymer chains and some entanglements still exist, as suggested by Lee (2001).G  is greater than G until the crossover frequency, which increases as the concentration decreases indicating that the behaviour corresponds to semi-rigid polymer chains and some entanglements still exist, as suggested by Lee (2001). Due to the semi-rigid nature of the molecules, Newtonian-like linear filament thinning behaviour was observed in capillary break-up experiments.Due to the semi-rigid nature of the molecules, Newtonian-like linear filament thinning behaviour was observed in capillary break-up experiments. Steady uniaxial extensional viscosity increases almost linearly with concentration. These results suggest that as concentration increases, the polymer exhibits a more ordered molecular structure resulting in increase molecular contact between molecules which subsequently leads to stronger molecular interactions and hence greater extensional behaviour.Steady uniaxial extensional viscosity increases almost linearly with concentration. These results suggest that as concentration increases, the polymer exhibits a more ordered molecular structure resulting in increase molecular contact between molecules which subsequently leads to stronger molecular interactions and hence greater extensional behaviour. The magnitude of the Trouton ratio (>>3) confirms the non-Newtonian behaviour of these polymer even though Newtonian-like linear thinning was observed in the capillary break-up experiments.The magnitude of the Trouton ratio (>>3) confirms the non-Newtonian behaviour of these polymer even though Newtonian-like linear thinning was observed in the capillary break-up experiments. XANTHAN GUM Capillary break-up measurements h f  8.8 mm  f = h f / h 0 D MID (t) t =- 20 ms t > 0 D = 4 mm h 0 = 2 mm XANTHAN GUM 0.5% Xanthan gum at 20  C (  i,f =0.5, 2.2) SCLEROGLUCAN 0.5% Scleroglucan at 20  C (  i,f =0.5, 2.2) 0 s 0.02 s 0.04 s 0.06 s 0.08 s 0.10 s 0.12 s 0.14 s 0 s 0.02 s 0.04 s 0.06 s 0.08 s 0.10 s 0.12 s 0.14 s