Название: The Rheology Handbook
Автор: Thomas Mezger
Издательство: Readbox publishing GmbH
Жанр: Химия
isbn: 9783866305366
isbn:
Table 2.1: Typical shear rates of technical processes | ||
Process | Shear rates γ ̇ (s-1) | Practical examples |
physical aging, long-term creep within days and up to several years | 10-8 ... 10-5 | solid polymers, asphalt |
cold flow | 10-8 ... 0.01 | rubber mixtures, elastomers |
sedimentation of particles | ≤ 0.001 ... 0.01 | emulsion paints, ceramic suspensions, fruit juices |
surface leveling of coatings | 0.01 ... 0.1 | coatings, paints, printing inks |
sagging of coatings, dripping, flow under gravity | 0.01 ... 1 | emulsion paints, plasters, chocolate melt (couverture) |
self-leveling at low-shear conditions in the range of the zero-shear viscosity | ≤ 0.1 | silicones (PDMS) |
mouth sensation | 1 ... 10 | food |
dip coating | 1 ... 100 | dip coatings, candy masses |
applicator roller, at the coating head | 1 ... 100 | paper coatings |
thermoforming | 1 ... 100 | polymers |
mixing, kneading | 1 ... 100 | rubbers, elastomers |
chewing, swallowing | 10 ... 100 | jelly babies, yogurt, cheese |
spreading | 10 ... 1000 | butter, spreadcheese |
extrusion | 10 ... 1000 | polymer melts, dough,ceramic pastes, tooth paste |
pipe flow, capillary flow | 10 ... 104 | crude oils, paints, juices, blood |
mixing, stirring | 10 ... 104 | emulsions, plastisols,polymer blends |
injection molding | 100 ... 104 | polymer melts, ceramic suspensions |
coating, painting, brushing, rolling, blade coating (manually) | 100 ... 104 | brush coatings, emulsion paints, wall paper paste, plasters |
spraying | 1000 ... 104 | spray coatings, fuels, nose spray aerosols, adhesives |
impact-like loading | 1000 ... 105 | solid polymers |
milling pigments in fluid bases | 1000 ... 105 | pigment pastes for paints and printing inks |
rubbing | 1000 ... 105 | skin creams, lotions, ointments |
spinning process | 1000 ... 105 | polymer melts, polymer fibers |
blade coating (by machine), high-speed coating | 1000 ... 107 | paper coatings, adhesive dispersions |
lubrication of engine parts | 1000 ... 107 | mineral oils, lubricating greases |
There is a linear velocity distribution between the plates, since the velocity v decreases linearly in the shear gap. Thus, for laminar and ideal-viscous flow, the velocity difference between all neighboring layers are showing the same value: dv = const. All the layers are assumed to have the same thickness: dh = const. Therefore, the shear rate is showing a constant value everywhere between the plates of the Two-Plates model since
γ ̇ = dv/dh = const/const = const (see Figure 2.3).
Figure 2.3: Velocity distribution and shear rate in the shear gap of the Two-Plates model
Both γ ̇ and v provide information about the velocity of a flowing fluid. The advantage of selecting the shear rate is that it shows a constant value throughout the whole shear gap. Therefore, the shear rate is independent of the position of any flowing layer in the shear gap. Of course, this applies only if the shear conditions are met as mentioned in the beginning of Chapter 2.2. However, this does not apply to the velocity v which decreases from the maximum value vmax on the upper, movable plate to the minimum value vmin = 0 on the lower, immovable plate. Therefore, when testing pure liquids, sometimes as a synonym for shear rate the term velocity gradient is used (e. g. in ASTM D4092).
b) Calculation of shear rates occurring in technical processes
The shear rate values which are given below are calculated using the mentioned formulas and should only be seen as rough estimations. The main aim of these calculations is to get merely an idea of the dimension of the relevant shear rate range.
1) Coating processes: painting, brushing, rolling or blade-coating
γ ̇ = v/h, with the coating velocity v [m/s] and the wet layer thickness h [m]
Examples
1a) Painting with a brush:
With v = 0.1 m/s and h = 100 µm = 0.1 mm = 10-4 m; result: γ ̇ = 1000 s-1
1b) Buttering bread:
With v = 0.1 m/s and h = 1 mm = 10-3 m; result: γ ̇ = 100 s-1
1c) Applying emulsion paint with a roller
With v = 0.2 m/s (or 5 s per m), and h = 100 µm = 0.1 mm = 10-4 m; result: γ ̇ = 2000 s-1
1d) Blade-coating of adhesive dispersions (e. g. for pressure-sensitive adhesives PSA):
With the application rate AR (i. e. mass per coating area) m/A [g/m2]; for the coating volume V [m3] applies, with the mass m [kg] and the density ρ [1 g/cm3 = 1000 kg/m3]: V = m/ρ
Calculation: h = V/A = (m/ρ)/A = (m/A)/ρ = AR/ρ; with AR = 1 g/m2 = 10-3 kg/m2 holds:
h =10-6 m = 1 µm; and then: γ ̇ = v/h. See Table 2.2 for shear rates occurring in various kinds of blade-coating processes [2.4] [2.5].
Table 2.2: Shear rates of various kinds of blade-coating processes for adhesive emulsions | |||||
Coating process | Application rateAR [g/m2] | Coating velocityv [m/min] | Coating velocityv [m/s] | Layer thicknessh [µm] | Approx. shear rate range γ ̇ [s-1] |
metering blade | 2 to 50 | up to 250 | up to 4.2 | 2 to 50 | 80,000 to 2 mio. |
roller blade | 15 to 100 | up to 100 | up to 1.7 | 15 to 100 | 10,000 to 100,000 |
lip-type blade | 20 to 100 | 20 to 50 | 0.33 to 0.83 | 20 to 100 | 3000 to 50,000 |
present maximum | 2 to 100 | 700 | 12 | 2 to 100 | 120,000 to 6 mio. |
future plans | up to 1500 | up to 25 | 250,000 to 12.5 mio. |
2) Flow in pipelines, tubes and capillaries
Assumptions: horizontal pipe, steady-state and laminar flow conditions (for information on laminar and turbulent flow see Chapter 3.3.3), ideal-viscous flow, incompressible liquid. According to the Hagen/Poiseuille relation , the following holds for the maximum shear stress τw and the maximum shear rate γ ̇ w in a pipeline (index w for “at the wall”):
Equation 2.4
τw = (R ⋅ Δp) / (2 ⋅ L)
Equation 2.5
γ ̇ w = (4 ⋅ V ̇ ) / (π ⋅ R3)
With the pipe radius R [m]; the pressure difference Δp [Pa] between inlet and outlet of the pipe or along the length L [m] of the measuring section, respectively (Δp must be compensated by the pump pressure); and the volume flow rate V ̇ [m3/s]. This relation was named in honor to Gotthilf H. L. Hagen (1797 to 1848) СКАЧАТЬ