Understanding Rheology

What is Rheology?
Rheology is the study of how a material deforms during and after a force is applied. Rheology directly affects product handling and flow characteristics. Some common measurements used to describe rheology are viscosity, thixotropic index, dispense rate, and sag resistance.
Why is Rheology Important?
Controlling rheological properties is essential for polymeric processing and application.
Mixing – Rheology effects ease of mixing whether by hand, with a premeasured package, or with a static mix tube.
Dispensing – Rheology dictates how a material is applied whether by spatula, spray, pump, syringe, cartridge, screen/stencil printing, or pouring. It is influenced by how rapidly viscosity changes once mixed due to the mixture’s chemistry.
Settling – Rheology affects the degree and rate at which fillers settle. Also important is filler type, particle size, shape, and size distribution. This is especially important for coatings and heavily filled encapsulants.
Flow Control – Rheology affects the way a material flows. High flow allows easy entry into intricate spaces versus a low flow which prevents flow into critical areas. Flow control is very important during initial application and during the curing process as well.
What Affects Rheology?
Resin – resin type and molecular weight affects viscosity and surface wetting.
Formulation – additives and fillers (type, shape, size, size distribution, and surface smoothness).
Temperature – with epoxies every 1°C change can cause up to a 5-10% change in viscosity.
Shear – the duration and amount of any force applied to the material. Shear rate measures a constant force.

To the layperson, rheology is
• Mayonnaise does not flow even under stress for a long time; honey always flows
• Silly Putty bounces (is elastic) but also flows (is viscous)
• Dilute flour-water solutions are easy to work with but doughs can be quite temperamental
• Corn starch and water can display strange behavior – poke it slowly and it deforms easily around your finger; punch it rapidly and your fist bounces off of the surface
To the scientist, engineer, or technician, rheology is
• Yield stresses
• Viscoelastic effects
• Memory effects
• Shear thickening and shear thinning

Rheological Classifications
There are two types of fluids: Newtonian and Non-Newtonian.
Newtonian Fluids
These are truly viscous “ideal liquids”, which means as the shear rate changes the viscosity remains constant (water, oils, solvents). Hence if you double the strain rate you will double the stress required.
Non-Newtonian Fluids
These fluids are affected by shear and are divided into Power Law Fluids (Pseudoplastic or Dilatant) and Time Dependent Fluids (Rheopectic or Thixotropic). Most polymers are pseudoplastic and thixotropic.
• Pseudoplastic: As shear increases, viscosity decreases. No matter how long a pseudoplastic material is sheared at a given shear rate, the viscosity will remain the same. Many polymeric systems are pseudoplastic, perhaps the most classic example is mayonnaise.
• Dilatant: These are the opposite of pseudoplastic that is, as shear increases the viscosity increases. Some highly filled materials are dilatant.
• Rheopectic : Viscosity increases as a function of time. Examples would be a mixed epoxy increasing in viscosity as curing takes place or a solvent based adhesive or coating where the viscosity increases as the solvent evaporates.
• Thixotropic: Viscosity decreases over time when using a constant shear rate. As shear rate decreases the material will gradually recover the original internal structure before shear, this can take seconds or days to fully recover. Many times, when a material sits, it will “structure”, this will give a “false” high viscosity reading if the material is not premixed.

Measuring Rheological Properties
Viscosity
A measure of the internal resistance of friction when a material moves against itself. Viscosity can be effected by the resin chemical structure, or the type and amount of filler added. The lowest viscosity materials are unfilled, short chained compounds.
The internal resistance or viscosity is typically measured using a rotating spindle instrument such as a Brookfield viscometer. The amount of force needed to turn the spindle (torque) at a selected speed (RPM) is measured. A simple calculation converts this “internal resistance” to viscosity. There are different surface area spindles used to measure different viscosity ranges.
The higher the torque value, the higher the viscosity. The force is measured as Pascal seconds, Poise or Newton seconds per meter2. One milliPascal second (mPas.) equals one centipoise (cP) or 1×10-4 Newton seconds per meter2. ASTM D 2393 is an example of a common viscosity test procedure used in North America.
Rotational spindle viscometers and cone and plate viscometers are used for most adhesives, encapsulants , inks, and some coatings. The Zahn Cup, Ford Cup, DuPont Parlin, and ISO Cup are some of the methods commonly used for coatings. Their general principal is to measure the time it takes a given volume to gravity feed through a given orifice.
Viscosity Profiles: A viscosity value is usually just one reading taken at a specific shear and temperature. The most descriptive method is the viscosity profile. Cone and plate viscometers can provide continuous, precise measurements over a wide range of shear rates and temperatures.
Viscosity profiles can also be very useful for knowing how viscosity changes during cure. This can be essential in some applications with tightly toleranced flow properties.
Thixotropic Index
A more accurate term would actually be “Pseudoplastic Index”, however, thixotropic index or shear thinning index (STI) have become accepted terms. It gives an indication as to how stiff and non-sag a material will be. A common measurement runs viscosity at two different shear rates such as 1 RPM and 10 RPM. The value recorded at the higher RPM is divided into the value at the lower RPM to obtain the index. Generally materials have thixotropic index values between 1 (high flow) and 5 (low flow or non-sag).
Dispense Rate
A test that usually specifies the orifice size, dispensing pressure and dispensing temperature. Then one either measures the amount of material dispensed in a particular time or the time to dispense a particular amount. Press Flow (often for cartridges), orifice flow, and syringe dispense rate are common dispense rate tests.
Sag Resistance
A special rheological measure for highly thixotropic products. Sag resistance is a measure of the resistance to flow with no shear on the material. Generally a bead of material is applied to a flat surface and the final flow or spread is measured and recorded. The surface angle, temperature, and time are specified by the particular test method.

Source: www.emersoncuming.com and Michigan Tech Chemical Engineering

An Introduction to Rheology and Viscosity

 ViscosityViscosity is a measure of the resistance of fluid to an applied stress. In everyday terms it is like the “thickness” of a fluid or gas. For example, water has a low viscosity so it appears “thin”. In comparison, honey has a higher viscosity, so it appears “thick”. Viscosity essentially describes a liquids internal resistance to flow and may be thought of as a measure of its internal friction.
The measurement of viscosity is a fairly simple test and the result reported is generally a single number. For the results of a viscosity test to be relevant, they should be compared to the results of tests done at the same temperature. It is normal for fluids to become more viscous at colder temperatures and less viscous at higher temperatures.
What is rheology?
Rheology is a more complex study of the flow of matter; mainly liquids, but also soft solids, gels, pastes and even sold materials that exhibit some level of flow (ie. do not just deform elastically). Rheology applies to substances that have a complex structure, including: muds, sludges, suspensions, polymers, petrochemicals and biological materials. The flow of these complex materials cannot be characterized by a single value of viscosity, instead viscosity changes with changing conditions. For example, ketchup’s viscosity lowers when it is shaken and cornflour’s viscosity increases when it is struck.
In practice, rheology is concerned with materials whose properties are between purely elastic material and Newtonian fluids, where mechanical behavior cannot be described by classic theories.

Do I need a viscometer or a rheometer?
There are several ways to measure the viscosity and rheological properties of a material. In both cases the most common testing methods are based around rotational devices that rotate a spindle immersed in a sample. By applying a controlled force or strain and measuring the resulting force or strain, it is possible to understand measure viscosity and understand rheological properties of a material.
The difference between a viscometer and a rheometer is essentially the quality of components and control capabilities. Basically, a rheometer is more versatile and has a wider range of applications than a viscometer does.
A rotational viscometer is a simple device that rotates a spindle in a single direction. Most viscometers have mechanical bearings that limit the range of applications to more viscous materials. A viscometer is a low cost instrument that is suitable for simple material, process or production tests that require simple flow measurements. A viscometer is highly suitable for quality control testing and is often portable so offer the ability to do remote or field testing.
A rotational rheometer allows far greater characterization of flow and deformation behavior. Rheometers can apply oscillatory motion to the spindles and can also apply large step changes in stress and strain to determine viscoelastic properties as well as flow properties. Rheometers usually use ultra-low friction air bearings which enable much greater sensitivity for low viscosity samples to be measured. Rheometers also tend to offer a wider range of sampling accessories such as temperature control units to study materials under a wider range of conditions.
A rheometer usually represents a greater investment, but can be essential for the true simulation of real processes and complete material characterization. The increased versatility of a rheometer makes it an excellent tool for research, product and process development as well as quality control testing.
Both instruments are complimentary and it is not uncommon to see viscometers and rheometers in a single organization.

Source: www.zimbio.com/Rheology

French Romanian Summer School 2011 – PROGRAM

Summer School
‘’Structured materials : elaboration, rheology and applications”

28th August 2011 – 3rd September 2011

PROGRAM

Sunday, August 28 : arrival Bucharest

Monday, August 29, Bucharest

8h45-9h00

Introduction

Corneliu Balan and Alain Ponton

9h00-10h00

Plenary Conference

Rheology of yield stress fluids : experiments, constitutive relation, numerical simulations

Corneliu Balan

(Politehnica University of Bucharest)

10h00-11h00

Coffee break and discussions

11h00-12h00

Visit of Field Matter Interaction Laboratory

http://reorom.pub.ro/index.php/home

Politehnica University of Bucharest

12h30-14h30

Lunch

14h30-15h30

Plenary Conference

A new type of mixer / reactor elongational flow: application to mixtures of molten polymers in the emulsification of a monomer in aqueous phase

René Muller

(University of Strasbourg)

15h30-17h

Visit of Phenomena Interface Laboratory

http://dbb.pub.ro/bioingteh/

Politehnica University of Bucharest

17h

Visit of Palace of the Parliament

http://www.cdep.ro/pls/dic/site.page?id=10&idl=3; http://www.viaromania.eu/atractii.cfm/81-palatul_parlamentului_casa_poporului.html

 

Thuesday, August 30, Bucharest

9h00-10h00

Plenary Conference

Biodynamics: from kinetics of biointerfaces to biosensors

Eugen Gheorghiu

(Director of International Center of Biodynamics, Bucharest)

10h00-10h15

Coffee break

10h15-11h00

Oral communication

Material characterization with an advanced rheometer platform

István Albert

(ROFAROM S.C., Romania)

11h00-12h15

Visit of International Center of Biodynamics

http://www.biodyn.ro/

12h30-1400

Lunch

14h00-14h30

Oral communication

Micro and macro rheology of extra cellular matrix of Aurelia Aurita medusa

Camille Gambini

(University Paris Diderot, Sorbonne Paris Cité)

14h30-15h00

Oral communication

Wetting and impregnation of structured textile materials

Florence Biguenet

(University of Mulhouse)

15h00-15h30

Discussions and concluding remarks

16h

Visite of Cotroceni National Museum

http://www.muzeulcotroceni.ro/engleza/index_eng.html

Wednesday, August 31, Bucharest-Iasi

8h00

Departure to Iasi

14h-17h

Accomodation and lunch

17h

Visit of Iasi

 

Thursday, September 1st, Iasi

9h00-09h45

Plenary Conference

Petru Poni Institute: research and projects in european context

Bogdan C. Simionescu

(Director of Institute of Macromolecular Chemistry “Petru Poni”)

http://www.icmpp.ro

9h45-10h00

Coffee break

10h00-10h45

Plenary Conference

Magnetorheology of complex materials

Alain Ponton

(University Paris Diderot, Sorbonne Paris Cité)

10h45–12h15

Visit of Institute of Macromolecular Chemistry “Petru Poni”

12h30-14h30

Lunch

14h30-15h15

Plenary Conference

Rheology– trends and perspectives in the Training and Research Platform of the “Gheorghe Asachi” Technical University of Iasi

Constanta Ibanescu

(Faculty of Chemical Engineering and Environment, Gheorghe Asachi Technical University )

15h15-15h30

Coffee break

15h30-16h15

Oral communication

From elaboration to rheology of sol-gel materials

Alain Ponton

(University Paris Diderot, Sorbonne Paris Cité)

16h15-17h00

Oral communication

Time-evolution of the structure of organoclay/polypropylene nanocomposites and its influence on time-temperature superposition principle

Edith Peuvrel-Disdier

(Ecole des Mines Paris Tech)

17h00-18h00

Visit of Faculty of Chemical Engineering and Environment Laboratories

http://www.tuiasi.ro/facultati/ic/

18h00-18h30

Discussions and concluding remarks

Friday, 2 september: excursion

 Saturday, 3 september : departure to Bucharest and France

French Romanian Summer School 2011: Structured Materials: Elaboration, Rheology and Applications

French Romanian Summer School
Bucharest – Iasi, 28 August – 03 September 2011
“Structured Materials : Elaboration, Rheology and Applications”

organized by Romanian Society of Rheology (SRR) and University Paris Diderot, Sorbonne Paris Cité

Topics
The school will discuss recent research on multi-scale structured materials from the elaboration to the study of properties. In an interdisciplinary approach, this school will address the rapidly growing field interest in structured materials both experimentally and theoretically.

Romania

Bucuresti

Iasi

The program will consist of plenary conferences, oral presentations discussions and visits of laboratories in order to favor exchanges between participants. Social program will be also included.

 Invited speakers

  • Corneliu Balan, Politehnica University Bucharest
  • René Muller, University of Strasbourg
  • Eugen Gheorghiu, Director of International Center of Biodynamics, Bucharest
  • Bogdan C. Simionescu, Director of Institute of Macromolecular Chemistry “Petru Poni”, Iasi
  • Alain Ponton, University Paris Diderot, Sorbonne Paris Cité
  • Constanta Ibanescu, “Gheorghe Asachi” Technical University, Iasi

Contact Persons:

Prof. Diana Brooboana (PU Bucharest): diana.broboana@upb.ro (Phone:+40.744.353135)

Prof. Corneliu Balan (PU Bucharest): corneliu.balan@upb.ro (Phone: +40.744.910420)

Dr. Alain Ponton (University Paris Diderot): alain.ponton@univ-paris-diderot.fr

The school is sponsored by S.C. ROFAROM (Paar-Physica Romanian Representative) and DANTEC Representative Office in Romania.

Program – Dynamics of Complex Fluids Conference – May 5-7, 2011 – Iasi, Romania

You can download the full program of the conference if you click HERE.

Dynamics of Complex Fluids Conference

“Petru Poni” Institute of Macromolecular Chemistry
Iasi, ROMANIA
May 5-7, 2011

Conference Chair Persons: Acad. Bogdan C. Simionescu
Prof. Maria Lungu
Dr. Magdalena Aflori
Organizing Committee: Dr. Maria Bercea
Dr. Simona Morariu
Dr. Diana Ciolacu
Dr. Raluca-Nicoleta Darie
Dr. Loredana-Elena Nita
Dr. Mariana Cristea
Dr. Mihaela-Adriana Olaru
Drd. Cristina-Eliza Brunchi

Organized by:
ROMANIAN SOCIETY OF RHEOLOGY
http://reologie.ro
European Social Fund – “CRISTOFOR I. SIMIONESCU” Postdoctoral Fellowship Programme (POSDRU/89/1.5/S/55216), Sectoral Operational Programme Human Resources Development 2007–2013
http://www.postdoc-icmpp.ro/index.html
“PETRU PONI” Institute of Macromolecular Chemistry
http://www.icmpp.ro/
ROMANIAN CHEMICAL SOCIETY
http://www.schr.org.ro

CONFERENCE SCHEDULE

Thursday, 5 May 2011

8.00 – 9.00 Registration

9.00 – 9.30 Opening Ceremony

9.30 – 10.15 Plenary Conference

10.15 – 11.00 Plenary Conference

11.00 – 11.30 Coffee Break

11.30 – 13.00 Visit of “Petru Poni” Institute of Macromolecular Chemistry

13.00 – 14.00 Lunch

14.00 – 14.45 Plenary Conference

14.45 – 15.30 Plenary Conference

15.30 – 16.00 Coffee Break

16.00 – 17.20 Oral Presentations

17.20 – 18.50 Posters Session

19.00 Conference Dinner

Friday, 6 May 2011

9.00 – 9.45 Plenary Conference

9.45 – 10.30 Plenary Conference

10.30 – 11.00 Coffee Break

11.00 – 13.00 Oral Presentations

13.00 – 14.00 Lunch

14.00 – 18.00 Round Table

Saturday, 7 May 2011

9.00 – 10.00 Closing Remarks

10.00 – 18.00 Iasi Visit

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