Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 201
ICC - Report ID: 201-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Ethylene Propylene Rubber Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 172-B,172-A,039-B,039-A,246-C,379-A,246-A,230-B,230-A
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"currency":"USD"}
ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/201-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>EPDM Rubber</b></p></b></p> <h6>Raw Materials</h6> <p><b>Propylene</b></p>, <p><b>Ethylene</b></p>, <p><b>Hydrogen</b></p>, <p><b>Chemicals</b></p>, <p><b>Ethylidine Norbornene</b></p>, <p><b>Toluene</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/201-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Polymerization; (2) Purification; and (3) Finishing.</p><p>Polymerization. Initially, the monomers are treated and mixed is continuously supplied to a stirred, jacketed reactor, as well as a solution with the catalysts. The reaction occurs substantially in the liquid phase, with an excess of liquid propylene –used as diluent. The rate of polymerization is controlled by the rate of catalyst addition, while temperature control is readily accomplished by controlled evaporation of the propylene. As the polymer is formed, it precipitates out of the reaction medium. </p><p>Purification. The slurry is pumped into a vessel, where reaction is terminated and the slurry is mixed with small amounts of toluene and water. The toluene allows that the water extracts the catalyst entrained in the polymer. Subsequently, unreacted monomers and solvent are removed from the catalyst-free polymer slurry in steam strippers containing water as dispersing medium, and are recyled to polymerization reactor. </p><p>Finishing. The rubber polymer, present in the form of wet crumbs in water, is fed to a drum with auxiliary agents like anti-agglomerant , so as to ensure that copolymer particles stay suspended and show a reduced tendency to agglomerate. The crumb slurry, with moisture content as high as 90 wt%, is then pumped to a rotary screen where most of the free water is removed. The wet polymer is conveyed through a single screw extruder. While being conveyed through the extruder, water is expelled from the polymer. The extruded dried crumb, containing less than 0.5 wt% of water, is cooled down, baled and packed </p><p></p>
ICC - Short Description: This report analyses the economics of Ethylene Propylene Diene Rubber (EPDM rubber) production from ethylene and propylene in the United States, via a suspension polymerization process using Ziegler-Natta catalyst. Ethylidene norbornene is also used as termonomer to allow vulcanization of the polymer.
ICC - Main Product: EPDM Rubber
ICC - Plant Capacity: 100.00
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Ethylene Propylene Rubber Production

EPDM Rubber Production Costs Report | Issue A | Q2 2024

Production Cost Report

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100 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 100 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.

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Production Process Information

Process Consumptions

Labor Requirements

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Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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Production Process Information

Process Consumptions

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

Plant Cost Breakdowns

Plant Capacity Assessment

Process Flow Diagrams

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the EPDM Rubber 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 EPDM Rubber 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 EPDM Rubber 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 EPDM Rubber 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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