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Brochures:
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Brochure: Bohlin Gemini rotational rheometer
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Brochure: Rosand Capillary Rheometer
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Application Notes:
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Application Note: Download free book "Rheological Methods in Food Process Engineering"
Full edition provided with kind permission of James F. Steffe
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Application Note: Characterizing gelation time and strength
A Bohlin rheometer can be used to accurately quantify the gelation times of foods. The formulation can be optimized with regard to gelant dosing in the minimum of time.
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Application Note: Determining stand up characteristics of caramel and chocolate
The Bohlin rheometer can be used to assess the dynamic mechanical properties of foods very simply, making it an ideal tool to assist formulation without the need for extensive production trials.
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Application Note:
Overcoming slippage when characterizing concentrated suspensions
Slippage can occur in fibrous suspensions, concentrated particulate suspensions and materials susceptible to shear induced melting.
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Application Note:
Determination of butter spreadability and fat components
The spreadability of butter and margarine products can be easily assessed by measurement of its dynamic mechanical properties at different temperatures.
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Application Note:
A note on slippage during rheological measurements on concentrated dispersions
Measurements at low shear rates or shear stresses can reveal much information on both the application behavior and the microstructure of materials.
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Application Note: The rheological properties of mayonnaise
The dynamic mechanical properties of materials such as mayonnaise give an indication of this reproducibility and can be correlated with, for example, storage stability, ease of pumping and sensory perception (i.e. mouthfeel).
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Application Note:
The use of modern rheometers in characterizing the behavior of foods
Many foodstuffs are concentrated dispersions of solid particles in a liquid medium (e.g. tomato ketchup), or liquid droplets in a liquid medium (e.g. mayonnaise). The dynamic mechanical properties of these products has to be very reproducible in order to satisfy customer needs.
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Application Note:
Rheological evaluation of margarine spreads
The dynamic mechanical properties of margarine spreads are important both with regard to 'usability', i.e. how easily they spread and aesthetically, whether there is an unacceptably visible phase separation.
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Application Note:
Formulating soup mixtures to resist settling of solid components
The yield stress can be used to calculate whether a sample is likely to settle in-situ, or whether it will be difficult to start pumping or stirring. Good rheological product design will dramatically enhance processing and end use.
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Application Note:
Compilation of all the above food related application notes
Compilation of Bohlin application notes for the Food industry
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Application Note:
Characterizing ice cream using a rheometer
The dynamic mechanical properties of ice cream can be critical for good customer perception and acceptance of the product. The ease of scooping the product when it is removed from the freezer, the mouth feel and the creaminess are three aspects discussed in this application note.
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Web seminars available for play back:
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Web seminar: Interpretation of the Viscoelastic Spectrum - Part 1 - 13th Feb 2006
This first seminar will discuss the universal viscoelastic spectrum. The
spectrum can be divided into three regions. In general, the significance of
these regions gives valuable information in terms of the size of a flow unit,
molecular interactions, and identifies small molecular segments within the flow
units.
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Web Seminar: Interpretation of the Viscoelastic Spectrum - Part 2 - 27th Mar 2006
This part discusses the temperature- frequency dependence of the material
functions of a polymer melt. What can be learned about the structure, molecular
weight, molecular weight distribution, long and short chain branching,
entanglements, etc. What are some of the reasons a UVS can not be measured.
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Web Seminar: Interpretation of the Viscoelastic Spectrum - Part 3 - 11th April 2006
This part discusses the relationships between the frequency dependence of the
material functions in terms of the dispersed phase. The structure-rheology
relationships for data that exists within the three zones of the viscoelastic
spectrum. If the temperature dependence of the material can be measured what
additional information can be obtained about structure. What are some of the
reason a UVS can or can not be determined on liquid dispersions?
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Web Seminar: Rheology & Particle Characterization - 7th Mar 2006
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Web Seminar: Instabilities in Viscoelastic Flows: Destabilizing Forces, Stability Criteria,
and Implications for Rheometry and Processing - 14th Feb 2006
Significant progress has been made over the past 15 years in understanding
instabilities in viscoelastic flows, especially rheometric flows such as flow
between concentric cylinders and torsional flow between a cone and plate or
between parallel plates. We review the criteria for determining when these flows
will become unstable due to fluid elasticity (in the absence of fluid inertia),
discuss the generalization of these criteria to more complex processing flows,
and consider how fluid inertia and thermal sensitivity may also affect flow
stability. These stability criteria are important in avoiding rheometric
artifacts and in determining materials processing windows.
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Web Seminar: Measuring and interpreting the yield stress of colloidal dispersions - 17th Jan 2006
Many concentrated dispersions and emulsions show a yield stress, i.e. they
behave as soft solids below some critical value of the applied stress but flow
when the critical stress, the yield stress, is exceeded. The yield stress is an
important property in many practical applications. For example it is essential
that products like tomato paste, toothpaste and skin cream have a yield stress
so that gravity does not cause them to flow. For a dispersion or emulsion to
show a yield stress the particulate phase has to be able to support a certain
level of stress, which in turn means that the particles have to interact with
each other to sufficient degree. Either the particles or droplets have to be
close-packed, or they have to repel each other strongly at a distance, or they
have to be aggregated such that the particles form a continuous network. In the
case of such "particulate gels", there is evidence that the yield stress is proportional to the inter-particle contact force. There are various protocols that may be used to measure the shear yield stresses using a rheometer - these will be discussed, as will the nature of the flow above the yield stress.
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Web Seminar: Viscometry: Recognizing Measurement Artifacts - 17th June 2005
How do you know the viscometry measurements you are making are real? Does the
data include measurement artifacts that you are not aware of? This seminar will
explain how to recognize invalid data, and give advice on how to perform correct
measurements. In particular, the measurement of low viscosity fluids, sample
slippage, the effects of thixotropy and high shear rate testing are
discussed.
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Web Seminar: How to Establish Automated Test and Analysis Procedures Using the Bohlin Rheometer Software - 10th May 2005
The latest version of control and analysis software (version 6.40) for the
range of Malvern Bohlin rheometers incorporates many significant new features,
including more flexible data analysis set-up and automation. A new Template
Wizard provides easy set-up and storage of analysis routines, and operators can
add multiple analyses to the menus for re-use. This seminar will explain new
software features whilst leading the viewer through the Template Wizard and
model fitting capabilities.
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