Commodity Production Costs Report
Polyisoprene Production from Raw Sugar
Polyisoprene Operating Costs & Plant Construction Costs
This report presents the economics of Polyisoprene production from starting from raw sugar, based on a plant located in Germany. The process comprehends the hydrolysis of sucrose, the fermentation of the obtained invert sugars into isoprene and a typical solution polymerization process for converting isoprene to Polyisoprene.
The report provides a comprehensive study of Polyisoprene production and related Polyisoprene production cost, covering three key aspects: a complete description of the Polyisoprene production process examined; an in-depth analysis of the related Polyisoprene plant capital cost (Capex); and an evaluation of the respective Polyisoprene plant operating costs (Opex).
The Polyisoprene production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Polyisoprene plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Polyisoprene plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Key reference(s): ?
Product
Polyisoprene. Polyisoprene (a.k.a. IR, Synthetic Rubber) is a thermoplastic elastomer, and the main component of natural rubber. It is formed by polymerization of isoprene in the presence of Ziegler-Natta catalyst. Synthetic Polyisoprene and natural rubber have the same type of applications, being used mainly in tires, belts, gaskets, hoses, foam rubber, molded and mechanical goods, bottle nipples, gloves, caulking, sealants, etc.
Raw Material
Raw Sugar. Raw sugar is a commodity product which is light brown in color and presents from 96 to 99 wt% of sucrose. Since it is not an edible product, it must undergo a refining process to become a refined sugar (more than 99.9 wt% sucrose), a product suitable to food applications. This may be accomplished in the same sugar factory where raw sugar was produced or in stand-alone refineries. It is commercialized as a granular product, and can be produced either from sugarcane or sugarbeet, depending on climate conditions. Sugarcane is cultivated in tropical and subtropical areas, while sugarbeet is more suitable to temperate zones.
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Up-to-date Report
Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Polyisoprene production plant examined.
Plant Capital Cost Details
Detailing of fixed capital (ISBL, OSBL & Owner’s Cost), working capital and additional capital requirements.
Plant Cost Breakdowns
Breakdown of Polyisoprene process unit (ISBL) costs and infrastructure (OSBL) costs; plant cost breakdown per discipline.
Operating Costs Summary
Summary presenting the operating variable costs and the total operating cost of the Polyisoprene production plant studied.
Operating Cost Details
Detailing of utilities costs, operating fixed costs and depreciation.
Plant Capacity Assessment
Comparative analysis of capital investment and operating costs for different Polyisoprene plant capacities.
Production Process Information
Block Flow Diagram, descriptions of process unit (ISBL) and site infrastructure (OSBL).
Process Consumptions
Raw materials and utilities consumption figures, by-products credits, labor requirements
Process Diagrams
Process flow diagrams (PFD), equipment list and industrial site configuration
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Other Polyisoprene Production Cost Reports
Polyisoprene Production from Glucose
This report presents the economics of Polyisoprene production starting from glucose, based on a plant located in the United States. The process comprehends the fermentation of 70 wt% glucose-water syrup into isoprene, followed by solution polymerization step for converting isoprene to Polyisoprene.
Details: 50 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD
Polyisoprene Production from Isoprene
This report presents the economics of Polyisoprene production from isoprene in the United States, via a typical solution polymerization process. The Ziegler/Natta catalyst system used in the process yields predominantly cis-1,4 units.
Details: 25 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $999 USD
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L-Lysine-HCl Production from Raw Sugar
This report presents the economics of Lysine production from raw sugar (sucrose). Sucrose is initially hydrolyzed into glucose and fructose (invert sugar). The invert sugars are then fermented to produce L-Lysine, which is recovered as L-Lysine-HCl. The economic analysis provided assumes a plant located in Germany.
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