Particle Coagulation of Emulsion Polymers
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2 a Primer on Polymer Colloids: Structure, Synthesis and Colloidal Stability
A. Al Shboul, F. Pierre, and J. P. Claverie 2 A primer on polymer colloids: structure, synthesis and colloidal stability 2.1 Introduction A colloid is a dispersion of very fine objects in a fluid [1]. These objects can be solids, liquids or gas, and the corresponding colloidal dispersion is then referred to as sus- pension, emulsion or foam. Colloids possess unique characteristics. For example, as their size is smaller than the wavelength of light, they scatter light. They also offer a large interfacial surface area, meaning that interfacial phenomena are of paramount importance in these dispersions. The weight of each dispersed particle being small, gravity and buoyancy forces are not sufficient to counteract the thermal random mo- tion of the particle, named Brownian motion (in tribute to the 19th century botanist Robert Brown who first characterized it). The particles do not remain in a dispersed state indefinitely: they will sooner or later aggregate (phase separation). Thus, thecol- loidal state is in general metastable and colloidal stability is one of the key features to take into account when working with colloids. Among all colloids, the polymer colloid family is one of the most widely inves- tigated [2]. Polymer colloids are used for a large number of applications, ranging from coatings, adhesives, inks, impact modifiers, drug-delivery vehicles, etc. The particles range in size from about 10 nm to 1 000 nm (1 μm) in diameter. They are usually spherical, but numerous other shapes have been observed. Polymer colloids are not uncommon in nature. For example, natural rubber latex, the secretion of the Hevea brasiliensis tree, is in fact a dispersion of polyisoprene nanoparticles in wa- ter. -
Controlled/Living Radical Polymerization in Aqueous Media: Homogeneous and Heterogeneous Systems
Prog. Polym. Sci. 26 =2001) 2083±2134 www.elsevier.com/locate/ppolysci Controlled/living radical polymerization in aqueous media: homogeneous and heterogeneous systems Jian Qiua, Bernadette Charleuxb,*, KrzysztofMatyjaszewski a aDepartment of Chemistry, Center for Macromolecular Engineering, Carnegie Mellon University, 4400 Fifth Avenue, Pittsburgh, PA 15213, USA bLaboratoire de Chimie MacromoleÂculaire, Unite Mixte associeÂe au CNRS, UMR 7610, Universite Pierre et Marie Curie, Tour 44, 1er eÂtage, 4, Place Jussieu, 75252 Paris cedex 05, France Received 27 July 2001; accepted 30 August 2001 Abstract Controlled/living radical polymerizations carried out in the presence ofwater have been examined. These aqueous systems include both the homogeneous solutions and the various heterogeneous media, namely disper- sion, suspension, emulsion and miniemulsion. Among them, the most common methods allowing control ofthe radical polymerization, such as nitroxide-mediated polymerization, atom transfer radical polymerization and reversible transfer, are presented in detail. q 2001 Elsevier Science Ltd. All rights reserved. Keywords: Aqueous solution; Suspension; Emulsion; Miniemulsion; Nitroxide; Atom transfer radical polymerization; Reversible transfer; Reversible addition-fragmentation transfer Contents 1. Introduction ..................................................................2084 2. General aspects ofconventional radical polymerization in aqueous media .....................2089 2.1. Homogeneous polymerization .................................................2089 -
„Polymer-Dispersionen“
„Polymer-Dispersionen“ Klaus Tauer Definitions Meaning & properties of polymer dispersions Preparation of polymer dispersions Polymer Dispersions Polymer: any of a class of natural or synthetic substances composed of very large molecules, called macromolecules, that are multiples of simpler chemical units called monomers. Polymers make up also many of the materials in living organisms, including, for example, proteins, cellulose, and nucleic acids. Dispersion: (physical chemistry) a special form of a colloid: i.e. very fine particles (of a second phase) dispersed in a continuous medium the most popular / famous / best-known case of a polymer dispersion is a LATEX a latex is produced by heterophase polymerization, where the most important technique is emulsion polymerization *) *) *) 1 DM = 1.95583 € Molecular Composition polymer dispersionen: high concentration of polymer with low viscosity thickener (BASF AG, Ludwigshafen) Virtual EASE 2003/1 „Thickening agent“ Sterocoll is an acidic aqueous polymer dispersion containing polymer particles rich in caroxylic acid groups. It is used as thickening agent. First the polymer dispersion is diluted with water to lower the polymer content from 30 % to 5 %. It is still a white liquid having low viscosity. By addition of a small amount of an aqueous sodium hydroxide solution the pH is increased and the caroxylic acid groups are negatively charged. This makes the polymer particles soluble in water and a polymer solution is formed. At the same time the viscosity strongly increases due to the unfolding of the polymer molecules. At the end a clear gel is obtained. important application properties: viscosity viscosity-psd dilatancy (BASF AG, Ludwigshafen) „Dilatancy“ Dilatancy is a rheological phenomenon. -
Initiator Systems Effect on Particle Coagulation and Particle Size Distribution in One-Step Emulsion Polymerization of Styrene
polymers Article Initiator Systems Effect on Particle Coagulation and Particle Size Distribution in One-Step Emulsion Polymerization of Styrene Baijun Liu 1, Yajun Wang 1, Mingyao Zhang 1,* and Huixuan Zhang 1,2 1 School of Chemical Engineering, Changchun University of Technology, Changchun 130012, China; [email protected] (B.L.); [email protected] (Y.W.); [email protected] (H.Z.) 2 Changchun Institute of Applied Chemistry, Chinese Academy of Sciences, Changchun 130022, China * Correspondence: [email protected]; Tel.: +86-431-8571-6465 Academic Editor: Haruma Kawaguchi Received: 6 December 2015; Accepted: 15 February 2016; Published: 19 February 2016 Abstract: Particle coagulation is a facile approach to produce large-scale polymer latex particles. This approach has been widely used in academic and industrial research owing to its higher polymerization rate and one-step polymerization process. Our work was motivated to control the extent (or time) of particle coagulation. Depending on reaction parameters, particle coagulation is also able to produce narrowly dispersed latex particles. In this study, a series of experiments were performed to investigate the role of the initiator system in determining particle coagulation and particle size distribution. Under the optimal initiation conditions, such as cationic initiator systems or higher reaction temperature, the time of particle coagulation would be advanced to particle nucleation period, leading to the narrowly dispersed polymer latex particles. By using a combination of the Smoluchowski equation and the electrostatic stability theory, the relationship between the particle size distribution and particle coagulation was established: the earlier the particle coagulation, the narrower the particle size distribution, while the larger the extent of particle coagulation, the larger the average particle size. -
Preparation of Ultra Fine Poly(Methyl Methacrylate) Microspheres in Methanol-Enriched Aqueous Medium
Macromolecular Research, Vol. 12, No. 2, pp 240-245 (2004) Preparation of Ultra Fine Poly(methyl methacrylate) Microspheres in Methanol-enriched Aqueous Medium Sang Eun Shim, Kijung Kim, Sejin Oh, and Soonja Choe* Department of Chemical Engineering, Inha University, Yonghyun 253, Namgu, Incheon 402-751, Korea Received March 17, 2004; Revised April 6, 2004 Abstract: Monodisperse PMMA microspheres are prepared by means of a simple soap-free emulsion polymerization in methanol-enriched aqueous medium in a single step process. The size and uniformity of the microspheres are dependent on the polymerization temperature. In a stable system, the uniformity is improved with the polymerization time. The most uniform and stable microspheres are obtained under mild agitation speed of 100 rpm at 70 oC. The monodisperse PMMA microspheres in the size range of 1.4-2.0 µm having less than 5% size variation are successfully achieved with varying concentrations of monomer and initiator. As the monomer and initiator concentrations increase, the larger microspheres with enhanced uniformity are obtained. However, the decreased amount of water induces the polydisperse PMMA particles due to the generation of secondary particles. Keywords: monodisperse microspheres, poly(methyl methacrylate), soap-free emulsion polymerization. Introduction micron-sized polymer colloids have been exploited and found that they allow to shift the stop-band in NIR and IR region.21 Since the seminal concept of the photonic band-gap In the synthesis of micron-sized polymer colloids via (PBG) crystals was proposed by Yablonovich1 and John,2 emulsion polymerization, several attempts have been made. explosive researches have been flushed in the fabrication Homola et al. -
Batch Emulsion Polymerization of Vinyl Chloride
Batch Emulsion Polymerization of Vinyl Chloride: Application of Experimental Design to Investigate the Effects of Operating Variables on Particle Size and Particle Size Distribution Mahdi Pourmehr, Amir H. Navarchian Department of Chemical Engineering, University of Isfahan, Isfahan, Iran Received 4 May 2008; accepted 7 July 2008 DOI 10.1002/app.29079 Published online 3 October 2008 in Wiley InterScience (www.interscience.wiley.com). ABSTRACT: In this article, the influences of operating effects in the range of levels investigated in this study. variables on the particle size (PS) and particle size distribu- Except initiator concentration, all factors have important tion (PSD) of emulsion poly(vinyl chloride) in batch reactor influence on the PSD (significance sequence: S > R > T > were investigated using Taguchi experimental design [E]). It is implied from the greater influence of agitation approach. The variables were temperature (T), water to speed relative to temperature on PSD that the shear coagula- monomer weight ratio (R), concentrations of initiator ([I]) tion predominates the Brownian coagulation in this system. and emulsifier ([E]), and agitation speed (S). Scanning elec- The relative optimum condition for a typical paste applica- tron microscope was used together with image analysis soft- tion was also determined using overall evaluation criteria. ware to determine the PS and PSD. Statistical analysis of VC 2008 Wiley Periodicals, Inc. J Appl Polym Sci 111: 338–347, 2009 results revealed that the PS of emulsion poly(vinyl chloride) -
Pre-Polymerised Inorganic Coagulants and Phosphorus Removal by Coagulation - a Review
Pre-polymerised inorganic coagulants and phosphorus removal by coagulation - A review Jia-Qian Jiang and Nigel J D Graham Environmental and Water Resource Engineering, Department of Civil Engineering, Imperial College of Science, Technology and Medicine, London SW7 2BU Abstract This paper reviews the use of pre-polymerised inorganic coagulants in water and waste-water treatment, and discusses the removal of phosphorus by chemical precipitation and coagulation. Commonly used inorganic coagulants are aluminium or iron (III) based salts, but a range of hydrolysed Al/Fe species, and not the Al/Fe salt itself, are responsible for the removal of impurities from water. By the development and use of polymeric inorganic coagulants, the coagulation performance can be improved significantly in some cases. Chemical precipitation and coagulation in phosphorus removal are two different processes, with the former related to the compound solubility and the latter depending on the destabilisation-adsorption mechanism. Presently, there is uncertainty concerning the mechanisms and overall performance of phosphorus removal by pre-polymerised metal coagulants. Introduction coagulants in water and waste-water treatment; to assess the present use of chemical precipitation and coagulation as a means Coagulants used for water and waste-water treatment are pre- for phosphorus removal; to evaluate the overall performance of dominantly inorganic salts of iron and aluminium. When dosed pre-polymerised coagulants in comparison with that of conven- into water the iron or aluminium ions hydrolyse rapidly and in an tional coagulants; and to discuss the relevant coagulation mecha- uncontrolled manner, to form a range of metal hydrolysis species. nisms for treating water and waste water. -
Polymer Colloid Science
Polymer Colloid Science Jung-Hyun Kim Ph. D. Nanosphere Process & Technology Lab. Department of Chemical Engineering, Yonsei University National Research Laboratory Project the financial support of the Korea Institute of S&T Evaluation and Planning (KISTEP) made in the program year of 1999 기능성 초미립자 공정연구실 Colloidal Aspects 기능성 초미립자 공정연구실 ♣ What is a polymer colloids ? . Small polymer particles suspended in a continuous media (usually water) . EXAMPLES - Latex paints - Natural plant fluids such as natural rubber latex - Water-based adhesives - Non-aqueous dispersions . COLLOIDS - The world of forgotten dimensions - Larger than molecules but too small to be seen in an optical microscope 기능성 초미립자 공정연구실 ♣ What does the term “stability/coagulation imply? . There is no change in the number of particles with time. A system is said to be colloidally unstable if collisions lead to the formation of aggregates; such a process is called coagulation or flocculation. ♣ Two ways to prevent particles from forming aggregates with one another during their colliding 1) Electrostatic stabilization by charged group on the particle surface - Origin of the charged group - initiator fragment (COOH, OSO3 , NH4, OH, etc) ionic surfactant (cationic or anionic) ionic co-monomer (AA, MAA, etc) 2) Steric stabilization by an adsorbed layer of some substance 3) Solvation stabilization 기능성 초미립자 공정연구실 기능성 초미립자 공정연구실 Stabilization Mechanism Electrostatic stabilization - Electrostatic stabilization Balancing the charge on the particle surface by the charges on small ions -
Emulsion Polymerization
Emulsion Polymerization Reference: Aspen Polymers: Unit Operations and Reaction Models, Aspen Technology, Inc., 2013. 1. Introduction Emulsion polymerization is an industrially important process for the production of polymers used as synthetic rubber, adhesives, paints, inks, coatings, etc. The polymerization is usually carried out using water as the dispersion medium. This makes emulsion polymerization less detrimental to the environment than other processes in which volatile organic liquids are used as a medium. In addition, emulsion polymerization offers distinct processing advantages for the production of polymers. Unlike in bulk or solution polymerization, the viscosity of the reaction mixture does not increase as dramatically as polymerization progresses. For this reason, the emulsion polymerization process offers excellent heat transfer and good temperature throughout the course of polymer synthesis. In emulsion polymerization, free-radical propagation reactions take place in particles isolated from each other by the intervening dispersion medium. This reduces termination rates, giving high polymerization rates, and simultaneously makes it possible to produce high molecular weight polymers. One can increase the rate of polymerization without reducing the molecular weight of the polymer. Emulsion polymerization has more recently become important for the production of a wide variety of specialty polymers. This process is always chosen when the polymer product is used in latex form. 2. Reaction Kinetic Scheme To appreciate the complexities of emulsion polymerization, a basic understanding of the fundamentals of particle formation and of the kinetics of the subsequent particle growth stage is required. A number of mechanisms have been proposed for particle formation. It is generally accepted that any one of the mechanisms could be responsible for particle formation depending on the nature of the monomer and the amount of emulsifier used in the recipe. -
The Influence of Inter-Particle Forces on Diffusion at the Nanoscale
www.nature.com/scientificreports OPEN The infuence of inter-particle forces on difusion at the nanoscale Francesco Giorgi1, Diego Coglitore2, Judith M. Curran1, Douglas Gilliland3, Peter Macko3, Maurice Whelan3, Andrew Worth3 & Eann A. Patterson1 Received: 18 March 2019 Van der Waals and electrostatic interactions are the dominant forces acting at the nanoscale and they Accepted: 12 August 2019 have been reported to directly infuence a range of phenomena including surface adhesion, friction, Published: xx xx xxxx and colloid stability but their contribution on nanoparticle difusion dynamics is still not clear. In this study we evaluated experimentally the changes in the difusion coefcient of nanoparticles as a result of varying the magnitude of Van der Waals and electrostatic forces. We controlled the magnitude of these forces by varying the ionic strength of a salt solution, which has been shown to be a parameter that directly controls the forces, and found by tracking single nanoparticles dispersed in solutions with diferent salt molarity that the difusion of nanoparticles increases with the magnitude of the electrostatic forces and Van der Waals forces. Our results demonstrate that these two concurrently dynamic forces play a pivotal role in driving the difusion process and must be taken into account when considering nanoparticle behaviour. Gold nanoparticles have attracted a growing interest in the scientifc community in recent years, especially for biological and medical applications. However, there is a lack of knowledge about the mechanisms that regulate their difusion through liquid media. It is well-known that two of the main forces acting on charged nanoparticles dispersed in a medium are Van der Waals and electrostatic forces, but their actual contribution to particle difu- sion has not been experimentally investigated. -
Principles and Applications of Emulsion Polymerization
PRINCIPLES AND APPLICATIONS OF EMULSION POLYMERIZATION Chorng-Shyan Chern A JOHN WILEY & SONS, INC., PUBLICATION PRINCIPLES AND APPLICATIONS OF EMULSION POLYMERIZATION PRINCIPLES AND APPLICATIONS OF EMULSION POLYMERIZATION Chorng-Shyan Chern A JOHN WILEY & SONS, INC., PUBLICATION Copyright © 2008 by John Wiley & Sons, Inc. All rights reserved Published by John Wiley & Sons, Inc., Hoboken, New Jersey Published simultaneously in Canada No part of this publication may be reproduced, stored in a retrieval system, or transmitted in any form or by any means, electronic, mechanical, photocopying, recording, scanning, or otherwise, except as permitted under Section 107 or 108 of the 1976 United States Copyright Act, without either the prior written permission of the Publisher, or authorization through payment of the appropriate per-copy fee to the Copyright Clearance Center, Inc., 222 Rosewood Drive, Danvers, MA 01923, (978) 750-8400, fax (978) 750-4470, or on the web at www.copyright.com. Requests to the Publisher for permission should be addressed to the Permissions Department, John Wiley & Sons, Inc., 111 River Street, Hoboken, NJ 07030, (201) 748-6011, fax (201) 748-6008, or online at http://www.wiley.com/go/permission. Limit of Liability/Disclaimer of Warranty: While the publisher and author have used their best efforts in preparing this book, they make no representations or warranties with respect to the accuracy or completeness of the contents of this book and specifi cally disclaim any implied warranties of merchantability or fi tness for a particular purpose. No warranty may be created or extended by sales representatives or written sales materials. The advice and strategies contained herein may not be suitable for your situation. -
Particle Aggregation During a Diatom Bloom. 11. Biological Aspects
MARINE ECOLOGY PROGRESS SERIES Published January 24 Mar. Ecol. Prog. Ser. Particle aggregation during a diatom bloom. 11. Biological aspects Ulf Riebesell Alfred Wegener Institute for Polar and Marine Research, Colurnbusstr., D-2850 Bremerhaven. Germany ABSTRACT: For a 6 wk period covering the time before, during, and after the phytoplankton spring bloom, macroscopic aggregates (20.5 mm diameter) were repeatedly collected and water column properties simultaneously measured at a fixed station in the Southern North Sea. Distinct changes in aggregate structure and composition were observed during the study. Predominantly detrital aggregates dur~ngthe early phase of the study were followed by diatom-dominated algal flocs around the peak of the bloom. Mucus-rich aggregates containing both algal and detrital components and with large numbers of attached bacteria dominated the post-bloom interval. The phytoplankton succession within the aggregates closely reflected the succession in the water column with a time delay of a few days. Algal flocculation did not occur as a simultaneous aggregation of the entire phytoplankton community, but as a successional aggregat~onof selected diatom species. Although the concentrations of ~norganicnutrients diminished considerably during the development of the phytoplankton bloom, the termination of the bloom appeared to be mostly controlled by physical coagulation processes. The importance of biologically-controlled factors for physical coagulation is discussed. INTRODUCTION stickiness, proposed that physical processes alone could determine the time and extent of algal aggregation. Mass flocculation during diatom blooms as predicted Based on a physical coagulation model, Jackson pre- by Smetacek (1985) has since been documented both in dicted that the rate of aggregation strongly depends on the field (Kranck & Milligan 1988, Alldredge & Got- algal concentration.