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Minimum end time policies for batchwise radical chain polymerization—II A two-stage process for styrene polymerization

✍ Scribed by Show-An Chen; King-Fu Lin


Publisher
Elsevier Science
Year
1980
Tongue
English
Weight
988 KB
Volume
35
Category
Article
ISSN
0009-2509

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✦ Synopsis


For styrene polymenzatlon, a two-stage process IS consldered The first stage, nntlated by mltlator, IS operated along the best rsothermal policy for a predetermined number average molecular weight and monomer conversion at end of the stage as described m the previous paper The second stage IS operated at higher temperature level at which thermal nutlatlon polymenzatlon IS sqqnticant A mathematical model IS proposed for descnbmg the changes of conversion and number average molecular weight wkth hme m the second stage based on the expenmentaf data obtained All parameters mvolved m the model are calculable usmg the kinetic constants of the mltlator untlatlon system and the thermal mltlatlon system Expenmental venticatgon on the optimal temperature pohcies for the second stage shows promlsmg Further calculations indicate that the optlmal two-stage process can be slgnrficantly better than the optimal process of mltlator uutlatlon or thermal mltlatlon polymenzation


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Minimum end time policies for batchwise
✍ Show-an Chen; Nae-wen Huang 📂 Article 📅 1981 🏛 Elsevier Science 🌐 English ⚖ 853 KB

For batchwise radical chain solution polymerization, the minimum end time problem is studied by considering the initiator concentration (or feed rate) and temperature as two control variables. The kinetic model used is based on a general mechanism and involving the gel effect. It is found that the o

Minimum end-time policies for batchwise
✍ Keh-Ying Hsu; Show-an Chen 📂 Article 📅 1988 🏛 Elsevier Science 🌐 English ⚖ 940 KB

For the radical chain polymerization in a presence of chain transfer agent, piecewise initiator addition and piecewise reaction temperature are considered as two control actions in XV unequal time intervals for minimizing the total reaction time under a given final monomer conversion and the number