This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a hybrid (slurry/gas phase) polymerization process. The process examined is similar to Borealis BORSTAR process. This process is based on a dual reactor system (slurry and gas phase reactors). This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Dual Reactor System, Slurry Reactor, Tubular Reactor, Loop Reactor
The continuous growth of knowledege makes it very difficult for scientists to retrieve comprehensive and accurate data on viruses. The desired information is often dispersed in a variety of books, journals and online resources. This encyclopedia presents the latest facts about all known viruses in a standardized form created by hundreds of the world's leading virologists. Virus taxonomy represents the basic framework that allows an understanding of the complex evolutionary process that continuously takes place among viruses and their hosts. Each of the 300 taxonomically ordered chapters includes detailed information on individual genus members, historical events, the hosts they can affect (animal, man or plant), virion morphology, genome properties, replication strategy, properties of individual transcripts and proteins, sequence accession numbers, biological properties, diseases, recombinant vector constructs, vaccine strains, key references, as well as a high-resolution particle image and a drawing of the genome organization. Its high content of easily accessible detailed information makes this Encyclopedia an indispensable tool for both researchers and lecturers. The new edition includes the recent discoveries made in this field as well as new viruses which have been discovered.
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a bulk phase polymerization process. The process examined is similar to the processes LyondellBasell Spheripol and Mitsui Hypol II. This process is based on the polymerization of liquid PG propylene and PG ethylene in loop reactors. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Tubular Reactor, Liquid-Phase Polymerization
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to CB&I Lummus Novolen process. This process is based on the polymerization of gaseous PG propylene and PG ethylene in vertical stirred-bed reactors. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Gas-Phase Reactor, Vertical Stirred-Bed
This volume chronicles the proceedings of the Fourth International Symposium on Silanes and Other Coupling Agents held under the aegis of MST Conferences, LLC in Orlando, FL, June 11-13, 2003. Silanes have been used for about half a century as coupling agents / adhesion promoters to promote adhesion between dissimilar materials in a variety of situations, e.g., coating technology, adhesive bonding, and reinforced composites. However, recently silanes have found other applications, for example, as corrosion inhibitors. Lately there has been tremendous R&D activity in understanding the mechanisms by which silanes work as well as in devising new and improved silanes. This volume contains a total of 16 papers which were properly peer reviewed, revised and edited. The book is divided into two parts: 1. Silane Coupling Agents; and 2. Other Coupling Agents / Adhesion Promoters. Topics covered include: sterically hindered silanes; silane hydrolysis; silane oligomers; adsorption of silanes and their surface characterization; structure of bis-silane water-barrier films; silanes for improving adhesive bonding of aluminim, elastomer-to-metal adhesive bonds, and adhesion in silica-filler tire-tread compounds; electrodeposition of bis-silanes; silanes to provide corrosion resistance and as corrosion fatigue inhibitors; silane and other treatments for musical instrument strings; cyclic azasilanes as coupling agents for nanotechnology; hybrid polymers based on silanes for coating textile fabrics; plasma copolymers as adhesion promoters; organophosphate adsorption; and activation of wood fibres. This volume and its predecessors containing bountiful information should serve as a reference source for the latest R&D activity in the arena of coupling agents. Anyone interested or involved in promoting adhesion between dissimilar materials for any application should find this volume of great use and value.
Here is a thoroughly revised edition of the most comprehensive guide to plastics, elastomers and composites available today. A standard reference, it provides current data, costs & properties for all designers and manufacturers of plastic products.
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to LyondellBasell Spherizone process. This process is based on the polymerization of PG propylene and PG ethylene in a multi-zone circulating reactor. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, MZCR, Gas-Phase Reactor, Bimodal
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to Grace UNIPOL process. This process is based on the polymerization of gaseous PG propylene and PG ethylene in fluidized-bed reactors. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Dow, Gas-Phase Reactor, Fluidized Bed Reactor
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to the processes INEOS INNOVENE and JPP HORIZONE. This process is based on the polymerization of gaseous PG propylene and PG ethylene in horizontal stirred-bed reactors. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Gas-Phase Reactor, Tubular Reactor, Japan Polypropylene Corporation, JNC Petrochemical Corporation
The topic of silanes and other coupling agents/adhesion promoters is of tremendous contemporary interest because of their application in many and varied technologically important areas ranging from coatings to reinforced composites to dentistry to biomedical (e.g., for bonding nucleotides to the so-called a gene chipsa ). In addition to their tra
