2002
DOI: 10.1002/pen.11108
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Development of a two‐stage, dual‐Arrhenius rheology model for a high‐performance phenylethynyl‐terminated poly(etherimide)

Abstract: A two‐stage, dual‐Arrhenius rheology model was successfully utilized to model the isothermal complex viscosity of a phenylethynyl‐terminated poly(etherimide) as a function of time and temperature over the experimental temperature range of 325°C to 350°C. Union of the dual‐Arrhenius model with a previously developed combination reaction kinetics model provided a chemoviscosity model giving viscosity as a function of degree of cure. A two‐stage, versus a single, dual‐Arrhenius model was used to accommodate a tra… Show more

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Cited by 13 publications
(12 citation statements)
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“…[10] Recent publications have gauged both reactive stability and defined flow and processing characteristics for reactive injection molding resins and other flowing resins. [11][12][13] Wong et al have targeted research tied to a range of microelectronics problems, including flip-chip assemblies and underfill, by studying different isothermal temperature gelation processes and the resulting network structure of epoxy resins, which are closely related to the reliability of those assemblies. [14,15] This was expanded on in a review published by Li and Wong.…”
Section: Introductionmentioning
confidence: 99%
“…[10] Recent publications have gauged both reactive stability and defined flow and processing characteristics for reactive injection molding resins and other flowing resins. [11][12][13] Wong et al have targeted research tied to a range of microelectronics problems, including flip-chip assemblies and underfill, by studying different isothermal temperature gelation processes and the resulting network structure of epoxy resins, which are closely related to the reliability of those assemblies. [14,15] This was expanded on in a review published by Li and Wong.…”
Section: Introductionmentioning
confidence: 99%
“…In this case, a phenomenological model as a relatively simple rate of equation represents the main features of the cure kinetics ignoring how the reactive species take part in the reaction 35. Although, a variety of phenomenological models have been proposed so far by different authors,35–37 all theories could be generally expressed as: where θ is the degree of curing used to indicate the extent of resin cross‐linking and can be obtained from the time‐dependent storage modulus ( G ') using the following equation: where G '( t ) is the value of the storage modulus at time t .…”
Section: Results and Disccussionmentioning
confidence: 99%
“…There are two primary mechanisms describing the cure kinetics of the most thermoset resins including n th‐order and auto‐catalytic theories 36. The n th‐order model assumes that the reaction rate is proportional to the concentration of unreacted material (1 − θ ), as shown in Eqn (4), where n is the order of reaction37: …”
Section: Results and Disccussionmentioning
confidence: 99%
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