2007
DOI: 10.1002/pen.20739
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Computer simulation of reactive extrusion processes for free radical polymerization

Abstract: The reactive extrusion for polymerization is an integrated polymer processing technology. A new semiimplicit iterative algorithm was proposed to deal with the complicated relationships among the chemical reaction, the macromolecular structure and the chemorheological property. Then the numerical computation expressions of the average molecular weight, the monomer conversion, and the initiator concentration were deduced, and the computer simulation of the reactive extrusion process for free radical polymerizati… Show more

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Cited by 10 publications
(15 citation statements)
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References 34 publications
(36 reference statements)
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“…An incremental theory is introduced to solve the above mentioned problems . Unfold the fluid flow space along the axial direction of the screw channel as a two‐dimensional axisymmetrical laminar flow model and then discretize it . Assuming that Xtrue(I,Jtrue) denotes the overall monomer conversion on the J th space point in the I th time step, Xtrue(I1,Jtrue) the overall monomer conversion on the J th space point in the (I1)th time step, and ΔXtrue(I,Jtrue) the increment of overall monomer conversion on the J th space point in the I th time step, the following equation can be obtained: Xtfalse|I,J=ΔX(I,J)Δt+O(Δt)=X(I,J)X(I1,J)Δt+O(Δt) where Δt denotes the time step, and O(Δt) the truncation error for the finite‐difference equation.…”
Section: Kinetic Modeling Of Aa Grafting Onto Lldpementioning
confidence: 99%
See 2 more Smart Citations
“…An incremental theory is introduced to solve the above mentioned problems . Unfold the fluid flow space along the axial direction of the screw channel as a two‐dimensional axisymmetrical laminar flow model and then discretize it . Assuming that Xtrue(I,Jtrue) denotes the overall monomer conversion on the J th space point in the I th time step, Xtrue(I1,Jtrue) the overall monomer conversion on the J th space point in the (I1)th time step, and ΔXtrue(I,Jtrue) the increment of overall monomer conversion on the J th space point in the I th time step, the following equation can be obtained: Xtfalse|I,J=ΔX(I,J)Δt+O(Δt)=X(I,J)X(I1,J)Δt+O(Δt) where Δt denotes the time step, and O(Δt) the truncation error for the finite‐difference equation.…”
Section: Kinetic Modeling Of Aa Grafting Onto Lldpementioning
confidence: 99%
“…In the simulation, the space of fluid flow was equivalently considered as a long axisymmetrical space, in which the effect of the axial motion of the solid wall on fluid flow was equivalent to the integrated effect of the screws and barrels on fluid flow. According to the construction method of the reactor model in our previous study, the equivalent length and radius of the model could be calculated.…”
Section: Setup Of Numerical Simulationmentioning
confidence: 99%
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“…One approach simplifies the extruder geometry into 1‐D or 2‐D model to reduce the computational load. Such approach has been adopted for the reactive extrusions of various polymerizations, including controlled degradation of polypropylene , free radical polymerization , graft copolymerization , and polymerization of L‐lactide , etc. The low dimensional models can provide average thermomechanical parameters along the extrusion, such as temperature, pressure, viscosity, etc.…”
Section: Introductionmentioning
confidence: 99%
“…The optimization methodology for reactive extrusion processes is still in its infancy and further researches should be performed. In our previous studies, we have built a 2D axisymmetrical model, introduced a semi‐implicit iterative algorithm and conducted the numerical simulation of reactive extrusion processes for polymerization . In this article, the reactive extrusion process for the free radical bulk polymerization was chosen as the optimization system.…”
Section: Introductionmentioning
confidence: 99%