Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 234
ICC - Report ID: 234-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Solution Styrene Butadiene Rubber Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 234-C,234-D,234-A,234-E,234-F
ICC - Related Reports List: 173-A,047-B,047-A,034-C,034-B,173-B
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"2":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"3":{"1":{"time":"7","price":0},"2":{"time":"3","price":"299"}}},"unit":"d"}
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/234-B.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>sSBR</b></p></b></p> <h6>Raw Materials</h6> <p><b>Butadiene</b></p>, <p><b>Chemicals</b></p>, <p><b>Styrene</b></p>, <p><b>Cyclohexane</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/234-B.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Polymerization; and (2) Purification.</p><p>Polymerization. The butadiene and styrene monomers are initially treated for the removal of impurities and dried since moisture could inhibit the polymerization. This mixture is fed with butyl lithium in cyclohexane solution in reactor. The anionic copolymerization is carried out continuously under a nitrogen atmosphere, in two stirred tank reactors operating in series to avoid inhibition effects of air. Potassium tert-butoxide is also fed to promote random copolymerization. The effluent from the polymerization train, a polymer slurry, is routed to purification.</p><p>Purification. The reaction termination is accomplished by mixing stopping agents with the polymer solution from the reactors train, which destroy the catalyst. The mixture is fed to a vessel where part of cyclohexane is flashed off from the slurry. The solvent is condensed and is passed through a couple of columns for the removal of residual impurities, before being recycled to the beginning of the process. The polymer solution is mixed with antioxidants, homogenized and then steam-stripped, for the removal of residual solvent, which is also purified and recycled. The crumb slurry is then pumped to the finishing steps: it is dried, pressed into bales, weighted, film-wrapped, and boxed.</p>
ICC - Short Description: This report presents the economics of SBR production starting from butadiene and styrene in the United States. It approaches a continuous process for producing a solution SBR grade. In this process, the anionic copolymerization of styrene and butadiene is carried out in the presence of cyclohexane solvent.
ICC - Main Product: Styrene Butadiene Rubber
ICC - Plant Capacity: 120.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Solution Styrene Butadiene Rubber Production

Styrene Butadiene Rubber Production Costs Report | Issue B | Q2 2024

Production Cost Report

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120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 120 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

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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Production Process Information

Process Consumptions

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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 Styrene Butadiene 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 Styrene Butadiene 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 Styrene Butadiene 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 Styrene Butadiene 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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This report presents the economics of SBR production starting from butadiene and styrene. The analysis encompasses a plant located in the United States, employing a typical cold emulsion process for generating a non-oil extended, non-staining grade of emulsion SBR (similar to 1502). In this process, an emulsion comprising water, styrene and butadiene is polymerized into a latex, which is then coagulated to form the SBR.

Details: 140 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

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High Solids Styrene Butadiene Latex Production

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Details: 160 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

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Low Solids Styrene Butadiene Latex Production

This report targets SBR Latex production in the United States via a typical cold emulsion polymerization process. The main product generated is a low solids content SBR Latex with high styrene content.

Details: 160 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 160 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

Emulsion Styrene Butadiene Rubber from Styrene and Butane

This report presents the economics of SBR production from n-butane and styrene. In this process, 1,3-Butadiene is initially produced from n-butane via a dehydrogenation process that is similar to Lummus Catadiene. Then, styrene and butadiene are polymerized via a typical cold emulsion process for generating a non-oil extended, non-staining grade of emulsion SBR (similar to 1502).

Details: 140 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   From $1,499 USD

The cost analyses presented in this report target a 140 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

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This report presents the economics of SBR production from n-butane and styrene. In this process, 1,3-Butadiene is initially produced from n-butane via a dehydrogenation process that is similar to Lummus Catadiene. Then, styrene and butadiene are polymerized via a typical continuous solution process for producing a solution SBR grade.

Details: 120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue F   From $1,499 USD

The cost analyses presented in this report target a 120 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

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Other Related Production Cost Reports

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This study presents the economics of Styrene production from chemical grade (CG) propylene and ethylbenzene in the United States. The process examined is a Propylene Oxide/Styrene Monomer (POSM) technology similar to the one owned by LyondellBasell. This process involves ethylbenzene oxidation, epoxidation, hydrogenation and dehydration steps.

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This report presents the economics of 1,3-Butadiene (BD) production from n-butane. In the process, n-butane undergoes a dehydrogenation reaction process similar to Lummus Catadiene, generating a C4s stream which is purified to obtain 1,3-Butadiene. The economic analysis is based on a plant located in the United States.

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