By Gordon G. Wallace, Peter R. Teasdale, Geoffrey M. Spinks, Leon A. P. Kane-Maguire
Foam Extrusion: rules and perform combines the technology of froth with the engineering of extrusion procedures in a single finished quantity, becoming a member of medical rules and engineering perform. beginning with the basics after which relocating to section separation, the textual content lays the clinical origin in one of these demeanour that the microscopic transition from a nucleus to a void (nucleation) and macroscopic circulate from a void to an item (formation) are plausibly addressed. The final component of the ebook offers attention-grabbing foam extrusion advancements, demonstrating how clinical findings should be utilized to the engineering box, from rules to batch experimentation and non-stop foaming. every one bankruptcy concludes with a bit of references for additional learn, and so much comprise a nomenclature part and/or precis part in addition. Drawing from the event of the editor and the authors, Foam Extrusion: ideas and perform captures the fascinating evolution of froth extrusion, and provides an excellent starting place for destiny advancements. it's an informative advisor for an individual concerned with this box.
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Extra resources for Foam extrusion: principles and practice
An important consideration when making use of the Sanchez-Lacombe model, however, is that the binary interaction parameter ␦ij is temperature dependent. 8 shows solubility predictions using the Sanchez-Lacombe theory for CO2 in PS at different temperatures. These predictions are based on correlations found by Sato et al. with their experimental solubility data . The correlations show that the binary parameter ␦ij must be determined for each solubility isotherm. 8 Solubilities computed with Sanchez-Lacombe theory for carbon dioxide in polystyrene at 373, 413, and 453°K, using parameters reported by Sato et al.
3(b), a master curve could be constructed using reduced variables. 3 for mixtures of PS with HCFC 142b, expressed as a master curve using reduced axes. 7). 5 power of the polymer concentration. For amorphous polymers such as PS, at temperatures less than 100°C above their glass transition temperature, the WLF equation [Equation (4)] is used. 0 . The resulting 0 values were then fitted through this WLF equation. As stated before, this equation is governed by two variables: T and Tg. 8 Zero-shear viscosity values for mixtures of PS and HCFC 142b at different compositions and temperatures and fitted to the WLF equation [Equation (4)].
5%. The Xie-Simha parameters give a better fit in the low temperature region, but result in divergences above 290°K. Thus, the scaling parameters are sensitive to the data used to determine them. 5 Specific volume of carbon dioxide as a function of temperature along the saturated vapor curve. Line: actual data ; Open symbols: using parameters reported by Xie and Simha ; Closed symbols: derived using complete saturated vapor curve. 1; Open symbols: determined with parameters reported by Xie and Simha ; Closed symbols: this work.