| The production of polymer 
								nanocomposites using intensified modules   The advent of a new 
								generation of polymer nanocomposites in recent 
								years has resulted in the emergence of 
								substantially improved engineering and 
								structural materials with enhanced mechanical 
								properties. Such materials comprise a wide range 
								of conventional homopolymers and filler 
								materials such as treated clays, inorganic 
								particulates, carbon nanotubes and glass fibres. 
								To date, the focus of much of the literature has 
								been on the conception and testing of new 
								nanocomposites and their properties, 
								particularly clay-based systems, and to a lesser 
								extent particulates. However an efficient, 
								continuous method of generating such materials 
								has yet to be developed.    Process Intensification, 
								(PI), is a strategy which entails the reduction 
								of process volume without a decrease in product 
								throughput. Its aim is to enhance mixing and 
								improve mass and heat transfer rates and so 
								optimise the conditions for effective chemical 
								reactions. This should result in improved 
								conversion and product quality, as well as 
								reducing waste through improved selectivity. 
								   
												
																|  Fig. 1 - 
																Spinning Disc 
																Reactor
 |  Fig. 2 - Barium 
																Sulphate 
																Crystals (0.2 - 
																0.7 mm)
 |  
								  PI offers the potential to 
								produce particulate-based nanocomposites in a 
								continuous mode which optimises the necessary 
								conditions for the three key processes of 
								polymerisation, nanoparticle production and the 
								effective mixing of the two composite elements 
								of particle and polymer.    The Spinning Disc Reactor, 
								SDR (Figure 1), has been employed for the 
								synthesis of poly(methyl-methacrylate) by means 
								of photo-initiation under ultra-violet light at 
								25°C. It can be operated as a one-pass reactor 
								or used to recycle a polymerising mixture until 
								the desired mass yield and molecular weight 
								properties have been achieved. The aqueous 
								production of particles to sizes of the order 
								0.1- 0.7 mm, (Figure 2), has also been indicated 
								on SDR and spinning cone devices suggesting the 
								possibility of an integrated reaction and mixing 
								process where polymer and particle can be 
								generated and inter-dispersed simultaneously. 
								The development of such a process is the primary 
								objective of this project.   The project has been in 
								progress since November 2002 and is due for 
								completion in February 2006. The principal 
								sponsors are Protensive Ltd. and the Engineering 
								Physical Sciences Research Council, (EPSRC). 
								Additional collaborators include Drs. K.V.K. 
								Boodhoo, (supervisor) and W.A. Dunk, (Protensive 
								Ltd., Newcastle).   For more information please 
								contact Dr Kamelia 
								Boodhoo.  |