A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation

In the polymer sheet processing industry, the primary objective when designing a coat-hanger die is to achieve a uniform velocity distribution at the exit of the extrusion die outlet. This velocity distribution depends on the internal flow channels of the die, rheological parameters and extrusion pr...

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Main Authors: Amin Razeghiyadaki, Dongming Wei, Asma Perveen, Dichuan Zhang
Format: Article
Language:English
Published: MDPI AG 2021-06-01
Series:Polymers
Subjects:
Online Access:https://www.mdpi.com/2073-4360/13/12/1924
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author Amin Razeghiyadaki
Dongming Wei
Asma Perveen
Dichuan Zhang
author_facet Amin Razeghiyadaki
Dongming Wei
Asma Perveen
Dichuan Zhang
author_sort Amin Razeghiyadaki
collection DOAJ
description In the polymer sheet processing industry, the primary objective when designing a coat-hanger die is to achieve a uniform velocity distribution at the exit of the extrusion die outlet. This velocity distribution depends on the internal flow channels of the die, rheological parameters and extrusion process conditions. As a result, coat-hanger dies are often designed for each polymer based on its individual rheological data and other conditions. A multi-rheology method based on a flow network model and the Winter–Fritz equation is proposed and implemented for the calculation, design and optimization of flat sheeting polymer extrusion dies. This method provides a fast and accurate algorithm to obtain die design geometries with constant wall-shear rates and optimal outlet velocity distributions. The geometric design when complemented and validated with fluid flow simulations could be applied for multi-rheological fluid models such as the power-law, Carreau–Yasuda and Cross. This method is applied to sheet dies with both circular- and rectangular-shaped manifolds for several rheological fluids. The designed geometrical parameters are obtained, and the associated fluid simulations are performed to demonstrate its favorable applicability without being limited to only the power-law rheology. The two such designed dies exhibit 32.9 and 21.5 percent improvement in flow uniformity compared to the previous methods for dies with circular and rectangular manifolds, respectively.
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spelling doaj.art-42aa1a0253b74edd840b044dccc55d062023-11-21T23:30:25ZengMDPI AGPolymers2073-43602021-06-011312192410.3390/polym13121924A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design EquationAmin Razeghiyadaki0Dongming Wei1Asma Perveen2Dichuan Zhang3Department of Mathematics, School of Sciences & Humanities, Nazarbayev University, Kabanbay Batyr 53, Nur-Sultan 0100000, KazakhstanDepartment of Mathematics, School of Sciences & Humanities, Nazarbayev University, Kabanbay Batyr 53, Nur-Sultan 0100000, KazakhstanDepartment of Mechanical & Aerospace Engineering, School of Engineering & Digital Sciences, Nazarbayev University, Kabanbay Batyr 53, Nur-Sultan 0100000, KazakhstanDepartment of Civil & Environmental Engineering, School of Engineering & Digital Sciences, Nazarbayev University, Kabanbay Batyr 53, Nur-Sultan 0100000, KazakhstanIn the polymer sheet processing industry, the primary objective when designing a coat-hanger die is to achieve a uniform velocity distribution at the exit of the extrusion die outlet. This velocity distribution depends on the internal flow channels of the die, rheological parameters and extrusion process conditions. As a result, coat-hanger dies are often designed for each polymer based on its individual rheological data and other conditions. A multi-rheology method based on a flow network model and the Winter–Fritz equation is proposed and implemented for the calculation, design and optimization of flat sheeting polymer extrusion dies. This method provides a fast and accurate algorithm to obtain die design geometries with constant wall-shear rates and optimal outlet velocity distributions. The geometric design when complemented and validated with fluid flow simulations could be applied for multi-rheological fluid models such as the power-law, Carreau–Yasuda and Cross. This method is applied to sheet dies with both circular- and rectangular-shaped manifolds for several rheological fluids. The designed geometrical parameters are obtained, and the associated fluid simulations are performed to demonstrate its favorable applicability without being limited to only the power-law rheology. The two such designed dies exhibit 32.9 and 21.5 percent improvement in flow uniformity compared to the previous methods for dies with circular and rectangular manifolds, respectively.https://www.mdpi.com/2073-4360/13/12/1924polymer processingsheet die designmanufacturing process designcoat-hanger diemodelingrheology
spellingShingle Amin Razeghiyadaki
Dongming Wei
Asma Perveen
Dichuan Zhang
A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
Polymers
polymer processing
sheet die design
manufacturing process design
coat-hanger die
modeling
rheology
title A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
title_full A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
title_fullStr A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
title_full_unstemmed A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
title_short A Multi-Rheology Design Method of Sheeting Polymer Extrusion Dies Based on Flow Network and the Winter–Fritz Design Equation
title_sort multi rheology design method of sheeting polymer extrusion dies based on flow network and the winter fritz design equation
topic polymer processing
sheet die design
manufacturing process design
coat-hanger die
modeling
rheology
url https://www.mdpi.com/2073-4360/13/12/1924
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