1990
DOI: 10.1002/aic.690360203
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Melt blowing: General equation development and experimental verification

Abstract: A model has been developed for steady polymer melt blowing. This model includes the dominant effect that the forwarding air has upon the process. Inertial, gravitational and heat transfer effects are also included. The model equations are solved numerically with both Newtonian and viscoelastic (Phan-Thien and Tanner) constitutive equations. The predicted results compare favorably with actual experimental data.

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Cited by 138 publications
(217 citation statements)
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References 26 publications
(20 reference statements)
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“…Based on this theory, Shambaugh [17] analyzed the mechanics of the deformation of the filament flow during drawing by gas jet as shown in Fig. 3(b).…”
Section: Comparison Of Gas-jet/electrospinning With Electrospinningmentioning
confidence: 99%
“…Based on this theory, Shambaugh [17] analyzed the mechanics of the deformation of the filament flow during drawing by gas jet as shown in Fig. 3(b).…”
Section: Comparison Of Gas-jet/electrospinning With Electrospinningmentioning
confidence: 99%
“…For the PTT model, these quantities are governed (Uyttendaele and Shambaugh, 1990) by t zz Á exp½eDeðt zz þ2t rr Þ þDe @t zz @t þ v @t zz @z À2t zz @v @z…”
Section: Model Descriptionmentioning
confidence: 99%
“…We follow Kase and Matsuo (1965) who used g ¼ 0:42 and m¼0.334 for parallel air flow along the spinline in melt spinning. Uyttendaele and Shambaugh (1990) have also adopted the same set of parameters in modeling melt blowing. The relative Reynolds number of the air flow is Re rel ¼ r air v rel D=m air , where r air is the air density, m air is the air viscosity, D is the fiber diameter, and v rel ¼ v air Àv is the relative velocity of the air with respect to the fiber at a given z-location.…”
Section: Model Descriptionmentioning
confidence: 99%
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