The Wiley Database of Polymer Properties 1999
DOI: 10.1002/0471532053.bra048
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PVTRelationships and Equations of State of Polymers

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Cited by 5 publications
(4 citation statements)
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“…This behavior is typical for ceramic injection molding feedstocks because their polymeric binder consists of more than one component, typically a low melting wax based part to increase flow-ability of the compound and a thermoplastic part that increases the stability during demolding. Standard mathematical methods like the two-domain Tait equation (McKinney and Simha 1997;Cho and Sanchez 1999;Beret and Prausnitz 1975) that allow the implementation of state of matter diagrams in CFD tools (e.g., MOLDFLOWÒ) cannot describe multi-phase compounds correctly.…”
Section: Injection Molding Experimentsmentioning
confidence: 99%
“…This behavior is typical for ceramic injection molding feedstocks because their polymeric binder consists of more than one component, typically a low melting wax based part to increase flow-ability of the compound and a thermoplastic part that increases the stability during demolding. Standard mathematical methods like the two-domain Tait equation (McKinney and Simha 1997;Cho and Sanchez 1999;Beret and Prausnitz 1975) that allow the implementation of state of matter diagrams in CFD tools (e.g., MOLDFLOWÒ) cannot describe multi-phase compounds correctly.…”
Section: Injection Molding Experimentsmentioning
confidence: 99%
“…If the swollen P(EA–MMA) and PEA formed fully IPN structure with homogeneous mixing, volume fraction of P(EA–MMA) in the particle can be calculated by using the swelling ratio l / l 0 of CP( x )-S and expected volume change from EA to PEA (density ρ = 0.92 and 1.12 g/cm 3 , respectively) by polymerization and evaluated to be 0.21–0.36. These low values suggest that the P(EA–MMA) particles may be softened at room temperature by mixing with PEA having low T g , which means that all of the colloidal crystal elastomer is in the rubbery state.…”
Section: Discussionmentioning
confidence: 97%
“…One thing that all of the equation of states have in common is that the dimensionless variables of temperature, pressure, and volume are obtained by dividing the real p , V , and T data by reducing the parameters p *, V *, and T * in the form of trueV˜= V/V*, trueT˜= T/T*, and truep˜= p/p*. Overviews of reduced parameters and their underlying theories and approaches can be found in handbooks and reviews [4,5,6]. All of the fitting procedures have the disadvantage that they are only valid for equilibrium states, and that the fitting result depends on the set of data points used.…”
Section: Introductionmentioning
confidence: 99%