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en:materialdaten:rheologische_materialdaten [2025/02/27 19:40] – [Pressure shift factor β] neelesten:materialdaten:rheologische_materialdaten [2025/05/15 15:49] (aktuell) – [Pressure shift factor β] cschall
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 ======Rheological material data====== ======Rheological material data======
  
-===== Input dialogue =====+===== Material data - Rheology =====
  
 The rheological data of the material is entered in the ‘Rheology’ tab: The rheological data of the material is entered in the ‘Rheology’ tab:
   * **Pressure shift factor beta**, this input is optional. Without an input value, the pressure dependence of the viscosity is neglected.   * **Pressure shift factor beta**, this input is optional. Without an input value, the pressure dependence of the viscosity is neglected.
-  * **Reference temperature T_B**, the values entered in the viscosity approach are valid for this temperature. +  * **Reference temperature T_B**, the values entered in the viscosity law are valid for this temperature. 
-  * **Temperature approach**, the temperature dependence of the viscosity can be modelled here. The temperature shift is calculated using //PAM//. The following modelling options are available+  * **Temperature law**, the temperature dependence of the viscosity can be modelled here. The temperature shift is calculated using //PAM//. The following modelling options are available
     * **WLF (Tb, Ts)**: Temperature shift by specifying the standard temperature T_S     * **WLF (Tb, Ts)**: Temperature shift by specifying the standard temperature T_S
     * **WLF (C1, C2)**: Temperature shift due to the constants C1 and C2     * **WLF (C1, C2)**: Temperature shift due to the constants C1 and C2
     * **Arrhenius**: Temperature shift due to activation energy E     * **Arrhenius**: Temperature shift due to activation energy E
-  * **Viscosity approach**, the equation for describing the viscosity can be selected here. The following models are available:+  * **Viscosity law**, the equation for describing the viscosity can be selected here. The following models are available:
     * **Carreau**: Input of the 3 parameters a, b and c     * **Carreau**: Input of the 3 parameters a, b and c
-    * **Potency**: Input of the parameters K and n +    * **Power law**: Input of the parameters K and n 
-  * **Wall sliding**: If the checkbox is selected, the critical shear stress at 2 temperatures must be entered. See [[en:berechnungen:wandgleitende_materialien|calculation of wall sliding]]+  * **Wall slipping**: If the checkbox is selected, the critical shear stress at 2 temperatures must be entered. See [[en:berechnungen:wandgleitende_materialien|calculation of wall sliding]]
  
 {{ :materialdaten:rex171_mat_en_004.png?nolink |}} {{ :materialdaten:rex171_mat_en_004.png?nolink |}}
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 with shear stress $τ$, the viscosity $η$ and the shear rate $\dotγ$. with shear stress $τ$, the viscosity $η$ and the shear rate $\dotγ$.
  
-This law states that there is proportionality between the shear stress and the shear rate, whereby the proportionality factor is the viscosity. This flow behaviour only occurs in polymer liquids or melts at very low shear rates and possibly at very high ones. Deviations are expressed in the so-called structural viscosity, dilatancy or the presence of a yield point. +This law states that there is proportionality between the shear stress and the shear rate, whereby the proportionality factor is the viscosity. This flow behaviour only occurs in polymer liquids or melts at very low shear rates and possibly at very high ones. Deviations are expressed in the so-called pseudoplasticity (shear thinning), dilatancy or the presence of a yield point. 
  
 {{ :materialdaten:abb_stoffverhalten_en.svg?nolink&600 |}} {{ :materialdaten:abb_stoffverhalten_en.svg?nolink&600 |}}
  
-The flow behavior of polymer melts is characterised in the shear rate ranges that +The flow behavior of polymer melts in practically relevant shear rate ranges is characterized by so-called pseudoplasticity (shear thinning). This describes a deviation from Newtonian fluid behavior, where the viscosity is no longer constant but decreases with increasing shear rate.
-exist in practice by structural viscosity. This describes a flow behavior which deviates +
-from that of Newtonian fluids, where the viscosity is no longer constant but highly +
-dependent on the shear rate. +
  
 The following figure shows the basic viscosity curve as a function of the shear rate. The following figure shows the basic viscosity curve as a function of the shear rate.
  
-{{ :materialdaten:abb_viskositaetsverlauf_de.svg?nolink&600 |}}+{{ :materialdaten:abb_viskositaetsverlauf_en.svg?nolink&600 |}}
  
 For shear rate ranges that are not too large, this behaviour can be described by the empirically found power flow law according to OSTWALD and DE WAELE:  For shear rate ranges that are not too large, this behaviour can be described by the empirically found power flow law according to OSTWALD and DE WAELE: 
  
 $$τ=K\cdot\dotγ^n$$ $$τ=K\cdot\dotγ^n$$
-resp.+respectively
 $$\eta=a_T \cdot K \cdot \gamma^{n-1}$$ $$\eta=a_T \cdot K \cdot \gamma^{n-1}$$
  
 where $n$ is the exponent of the flow law and $K$ is the consistency factor. where $n$ is the exponent of the flow law and $K$ is the consistency factor.
  
-Due to the simple structure of this approach, almost all flow problems that can be analysed for Newtonian fluids can be treated analytically. In double logarithmic representation, a straight line results for the power approach. For the Newtonian range, this results in $n=1$ and $K=\eta_0$. In the structurally viscous range, the viscosity curve in small ranges can also be approximated by the power law. This results in a shear rate-dependent $n<1$.+Due to the simple structure of this approach, almost all flow problems can be treated analytically. In double logarithmic representation, a straight line results for the power law. For the Newtonian range, this results in $n=1$ and $K=\eta_0$. In the pseudoplastic range, the viscosity curve in small ranges can also be approximated by the power law. This results in a shear rate-dependent $n<1$.
  
 {{ :materialdaten:abb_potenz_naeherung_en.svg?nolink&600 |}} {{ :materialdaten:abb_potenz_naeherung_en.svg?nolink&600 |}}
  
-The CARREAU approach offers a better description over wide ranges of the viscosity function, especially for materials with a pronounced transition from the Newtonian to the structural viscosity range: +The CARREAU approach offers a better description over wide ranges of the viscosity function, especially for materials with a pronounced transition from the Newtonian to the pseudoplastic range: 
  
 \[η = \frac {A \cdot a_T} {(1+a_T \cdot B \cdot \dotγ)^C}\] \[η = \frac {A \cdot a_T} {(1+a_T \cdot B \cdot \dotγ)^C}\]
  
-Where $A$ is the zero viscosity, $B$ is the reciprocal transition shear rate and $C (= 1-n)$ is the gradient. +Where $A$ is the zero-shear viscosity, $B$ is the reciprocal transition shear rate and $C (= 1-n)$ is the gradient. 
  
 {{ :materialdaten:abb_carreau_en.svg?nolink&600 |}} {{ :materialdaten:abb_carreau_en.svg?nolink&600 |}}
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 The temperature dependence is taken into account by the temperature shift factor $a_T$, which can be described in three different ways The temperature dependence is taken into account by the temperature shift factor $a_T$, which can be described in three different ways
  
-===Carreau-WLF ((T_B, T_S))===+===Carreau-WLF (T_B, T_S)===
  
 \[log(a_T) = \frac {C_1\cdot(T_B-T_S)} {C_2+(T_B-T_S)} - \frac {C_1\cdot(T-T_S)} {C_2+(T-T_S)}\]  \[log(a_T) = \frac {C_1\cdot(T_B-T_S)} {C_2+(T_B-T_S)} - \frac {C_1\cdot(T-T_S)} {C_2+(T-T_S)}\] 
  
-$T_B$, $T_S$ are given, $C_1 = 8,86$, $C_2 = 101,6$+$T_B$, $T_S$ must be provided, $C_1 = 8,86$, $C_2 = 101,6$
  
 with: $T_B$ = reference temperature, $T_S$ = standard temperature, $T$ = current temperature with: $T_B$ = reference temperature, $T_S$ = standard temperature, $T$ = current temperature
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 \[ln(a_T) = - \frac {C_1 \cdot (T-T_B)} {C_2+(T-T_B)}\]  \[ln(a_T) = - \frac {C_1 \cdot (T-T_B)} {C_2+(T-T_B)}\] 
  
-$C_1$, $C_2$, $T_B$ are given +$C_1$, $C_2$, $T_B$ must be provided
  
-**with**: $T_B$ = reference temperature, $T_S$ = standard temperature, $T$ = current temperature+**with**: $T_B$ = reference temperature, $T$ = current temperature
  
 === Carreau-Arrhenius (E, T_B) === === Carreau-Arrhenius (E, T_B) ===
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 $$ln(a_T)=\frac{E}{R} (\frac{1}{T}-\frac{1}{T_B}) $$ $$ln(a_T)=\frac{E}{R} (\frac{1}{T}-\frac{1}{T_B}) $$
  
-**with**: $E$ = activating energy, $R$ = gas constant, $K_{0T}$ = physical size at the temperature $T_0$, $T_0$ = reference temperature (in kelvin) +**with**: $E$ = activating energy, $R$ = gas constant, $T_B$ = reference temperature (in kelvin), $T$ = current temperature (in kelvin) 
- +
-With the Carreau-law the polymer specific material behavior can be described over +
-large shear rate and temperature areas. +
  
 ==== Pressure shift factor β ==== ==== Pressure shift factor β ====
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 $$ a_p = exp(\beta \cdot (p-p_B))$$ $$ a_p = exp(\beta \cdot (p-p_B))$$
  
-with the pressure displacement factor $\beta$, the pressure $p$ and the reference pressure $p_B$.+with the pressure shift factor $\beta$, the pressure $p$ and the reference pressure $p_B$.
  
 {{ :materialdaten:abb_viskositaet_druckabhaengig_en.svg?nolink&600 |}} {{ :materialdaten:abb_viskositaet_druckabhaengig_en.svg?nolink&600 |}}