Macromolecular Reaction Engineering最新文献

Methods for the evaluation of the Damkohler number for monomer transport during emulsion homopolymerization and copolymerization are extended to the analysis of gaseous monomers. Results indicate that the monomer transport limitation of gaseous monomers in both homo and copolymerization is strongly dependent on overall pressure through Henry's law relationship governing the concentration of monomer in the aqueous phase in equilibrium with monomer bubbles. At low pressures, most monomers studied exhibit monomer transport limitations; however, even at very high pressures, some gaseous monomers still exhibit monomer transport limitations.

Front Cover: In article number 2300031, Carlos Bruno Barreto Luna and co-workers develop reactive blends of polyamide 6 and acrylic acid-grafted polyethylene (PE-g-AA). The PE-g-AA carboxylic groups react with the amine terminal groups of polyamide 6, forming the amide group and interface stabilizing the PA6/PE-g-AA blend. This promote a refinement of the dispersed PE-g-AA particles in polyamide 6, generating high-performance in impact strength and elongation at break.

The mean-square radius of gyration of network polymers can be correlated with the graph diameter, and the fraction d of segments located in the diameter chain is used to investigate the dimensions of large-sized network polymers whose cycle rank is over 10³. A simplified Monte Carlo simulation model for the miniemulsion vinyl/divinyl copolymerization is used for the generation of large-sized network polymers, assuming the classical chemical kinetics are valid. Both conventional free-radical polymerization and living polymerization are considered, and the heterogeneity of network architecture is controlled by changing the reactivity ratio of double bond in divinyl monomer with respect to that in vinyl monomer. The network maturity index (NMI) which is the cycle rank per primary chain is used to represent the degree of development of the network architecture. As the NMI increases to be well-developed, the calibrated d, defined by d_c = d/f_d where f_d is a calibration constant that shows the degree of network heterogeneity, starts to follow the master curve. This characteristic behavior applies regardless of the polymerization mechanism and the heterogeneity of the formed network architecture. Detailed characteristics of the master curve and prospects for application to gel molecules are also discussed.

A multicomponent Flory-Huggins model is implemented and utilized to describe the liquid–liquid equilibrium phenomenon in mixtures of polypropylene and xylene, in the context of the well-known xylene solubles (XS) test. The XS experiment is a common procedure in many polymer laboratories, used to determine the percentage of xylene solubles in samples of polypropylene, which provides an approximate measure of the atactic and oligomeric chains. Despite the importance of the test, the literature lacks a thermodynamic perspective regarding the description of this extraction phenomenon. In the present study, the Flory-Huggins interaction parameter is adjusted in a multicomponent framework to ensure that equilibrium chain length distributions calculated with the proposed model best match experimental distributions. It is shown that the experimental data obtained from XS analyses can be accurately fitted by the proposed model and that the estimated Flory-Huggins interaction parameter is more sensitive to the polymer average molar mass than to the degree of tacticity, when a particular catalyst is considered.

This Macromolecular Reaction Engineering special issue is dedicated to Celebrate the 60^th birthday of José Carlos Pinto, or Zé, as he likes to be called by his friends and colleagues. We were honored and delighted to organize this special issue of Macromolecular Reaction Engineering with Dr. Spiegel to celebrate the importance of Zé’s contribution to developing polymer technology throughout his 35 working years.

José Carlos is now a full Professor of the Chemical Engineering Program at Instituto Alberto Luiz Coimbra de Pós-Graduação e Pesquisa em Engenharia (COPPE), Federal University of Rio de Janeiro, and a permanent member of the Graduate Program in Chemical and Biochemical Process Engineering at the School of Chemistry, Federal University of Rio de Janeiro. Zé has worked in modeling, simulation, and control of polymerization processes since 1987, published about 500 papers in refereed journals and deposited 50 patents during the supervision of more than 150 MSc Dissertations, 100 DSc theses, and hundreds of projects with industrial partners. He is currently a member of the editorial committee of the journal Polímeros: Ciência e Tecnologia (edited by Associação Brasileira de Polímeros (ABPol)) and a member of the Editorial Board of Macromolecular Reaction Engineering (published by Wiley) and Processes (published by MDPI). He has been a member of the Brazilian Academy of Sciences since 2010 and the National Academy of Engineering since 2014. Finally, he has deserved about 11000 citations in published materials, according to the “Google Scholar” database (consulted on February 13^th, 2023).

Prof. Pinto participated in industrial and academic research projects in 20 countries and 126 different institutions, as illustrated in Figure 1, reinforcing the relevance of this research in the global polymer scenario.

Zé has been a versatile researcher, as highlighted in Figure 2, presenting many keywords in his papers, totaling 726. As shown in Figure 2, his work has been focused on the general area of Chemical Engineering, with an emphasis on chemical reactors, particularly modeling, simulation, and control of polymerization systems. He has also been active in emerging technologies in polymer, motivating Brazilian researchers to work in eco-friendly polymers, biodegradable polymers, polymers for biomedical applications, polymer biodegradation and stabilization, and chemical recycling of polymer wastes. Zé dedication to the academia and to his students can be summarized in one of his sayings taken from a Djavan lyric: “if I had more soul to give, I would give it”.

Zé is versatile not only in his professional career but also in his personal life. Zé has written two poetry books! Besides, he has recorded a CD with his composed songs, “Turbilhão” being one of our favorites. And during the pandemic, he created a YouTube Chanel (“Falando Com Ciência”), to discuss scientific and

Front Cover: In article number 2200057, Arash Alizadeh, Vasileios Touloupidis, and João B. P. Soares have developed a thermodynamic simulation package for the catalytic polymerization of olefins in autoclave slurry, loop slurry, gas-phase, and autoclave solution reactors. The simulator uses the Sanchez–Lacombe theory as one of the major thermodynamic models in the polymer industry. Simulations under industrial conditions show why thermodynamic effects must be included in olefin polymerization models.

Back Cover: Polymer networks are synthesized to selectively target trans-resveratrol. By employing a statistical design of experiments, the polymerizations are conducted using ultraviolet light initiation, thus yielding materials with molecularly imprinted binding sites tailored for trans-resveratrol. These materials are successfully applied in purifying trans-resveratrol from winemaking residues, demonstrating their practical utility. This is reported by Amir Bzainia, Rolando C. S. Dias, and Mário Rui P. F. N. Costa in article number 2200076.

Herein, the poly(ɛ-caprolactone)-poly(ethylene glycol)-poly(ɛ-caprolactone) (PCL-PEG-PCL) macro xanthate reversible addition–fragmentation chain-transfer agent is obtained on the polyethylene glycol (PEG) (600, 1000, and 1500 g mol⁻¹) block, after the addition of ɛ-caprolactone via ring-opening polymerization. Then, poly (styrene-b-ɛ-caprolactone-b-PEG-b-ɛ-caprolactone-b-styrene) pentablock copolymer is synthesized reversible addition–fragmentation chain-transfer (RAFT) solution polymerization technique via mediated PCL-PEG-PCL xanthate macro-RAFT agents and 2,2′-azobisisobutyronitrile as initiator. The products are demonstrated using Fourier transform infrared spectrophotometer (FT-IR), proton nuclear magnetic resonance (¹H-NMR), carbon nuclear magnetic resonance (¹³C-NMR), differential scanning calorimetry (DSC), and gel permeation chromatography (GPC) analyses. First-order linear kinetic graphs of the reaction mechanism are observed with an increase in molecular weights (M_W) between 16 000 and 36 000 g mol⁻¹. The narrow dispersity (Đ = 1.40–1.48) polymer formation of styrene (St) controlled by RAFT polymerization confirms the increase in molecular weight according to the polymerization time. The reaction kinetics are first order and the rate constants are found to be k₁ = 6.16 × 10⁻⁴s⁻¹, k₂ = 6.91 × 10⁻⁴ s⁻¹ and k₃ = 7.33 × 10⁻⁴ s⁻¹. Thermal and spectroscopic analyses prove that the reactions are carried out successfully.