Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: R
ICC - Volume: 172
ICC - Report ID: 172-R
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: PG Ethylene Production from Ethylene-Rich Gas
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 172-A,172-B,172-C,172-D,172-E,172-F,172-G,172-H,172-I,172-J,172-K,172-L,172-M,172-N,172-O,172-P,172-Q,172-S,172-T,172-U,172-V
ICC - Related Reports List: 230-A,198-F
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":"1499","2":"1499","3":"1499"},"2":{"1":"2399","2":"2399","3":"2399"},"3":{"1":"3999","2":"3999","3":"3999"}},"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/172-R.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Ethylene</b></p>, <p><b>Fuel</b></p>, <p><b>Ethane</b></p>, <p><b>Hydrogen</b></p> <h6>Raw Material</h6> <p><b>Ethylene/Ethane mix</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/172-R.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) C3+ Hydrocarbons Removal; (2) Acetylene Hydrogenation; (3) Light Ends Separation; and (4) Ethylene Fractionation.</p><p>C3+ Hydrocarbons Removal. Cracked gas, rich in ethylene, is fed to the deethanizer column. The column overhead vapor, consisting of C2 and lighter components, is sent to hydrogenation reactors. The stream composed of C3+ components obtained bottom is sold as fuel.</p><p>Acetylene Hydrogenation. The deethanizer overhead stream is compressed and fed to two hydrogenation reactors in series, for removing acetylene impurities, which are converted to ethylene and ethane. The hydrogenated stream, composed mainly of ethylene, ethane, methane and hydrogen, is cooled and partially condensed. The resulting liquid, comprising mainly impurities, stream is returned to the deethanizer, while the vapor is routed to the cold box downstream.</p><p>Light Ends Separation. The hydrogenation product stream is sent to a cold box, to separate light ends and hydrogen from ethylene and ethane. The hydrogen-rich gas is split: a portion is routed to a PSA unit for further purification and is returned to the hydrogenation reactors; the remainder is sold as by-product. The condensates from the chilling train are fed to the demethanizer column downstream, while light ends are used as fuel. The demethanizer strips off light ends and hydrogen from the ethylene/ethane stream and returns these components to the cold box.</p><p>Ethylene Fractionation. The C2 stream obtained as the demethanizer bottom is directed to the C2 splitter. In this column, while high purity ethylene is drawn from the column as a side stream. Ethane, from C2-splitter bottoms, is sent to the integrated unit.</p><p></p>
ICC - Short Description: This report examines the costs related to Polymer Grade (PG) Ethylene production via purification of an ethylene-rich stream obtained from a typical ethane steam cracking plant. The economic analysis performed is based on a plant constructed in the United States.
ICC - Main Product: Ethylene
ICC - Plant Capacity: 400.00
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PG Ethylene Production from Ethylene-Rich Gas

Ethylene Production Costs Report | Issue R | Q3 2024

Production Cost Report

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400 kta United States-based plant   |   Q3 2024   |   107 pages

This report presents a cost analysis of a 400 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

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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Ethylene 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 Ethylene 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 Ethylene 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 Ethylene 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

Other Ethylene Production Cost Reports

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This study presents the costs associated with Green Polymer Grade (PG) Ethylene production from ethanol in the United States using a process similar to the processes developed by Braskem and Petrobras. In this process, the reaction system is composed of multiple reactors and multiple furnaces.

Details: 250 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue N   From $799 USD

The cost analyses presented in this report target a 250 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.

PG Ethylene from Ethanol (Similar to Dow Chemical Process)

This study concerns Green Polymer Grade (PG) Ethylene production in the United States. The technology examined in this report is similar to the one developed by Dow Chemical. In this process, a selective oxidation reactor is used in the purification step to remove CO and hydrogen from the process.

Details: 250 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue P   From $799 USD

The cost analyses presented in this report target a 250 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

Homopolymer HDPE from Ethylene (Similar to MarTECH Loop Slurry)

This report presents the economics of High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene in the United States, using a slurry loop process similar to Chevron Phillips MarTECH and INEOS INNOVENE S. In this process, the monomers are polymerized in a single loop reactor.

Details: 450 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue F   From $799 USD

The cost analyses presented in this report target a 450 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 Polymer Grade (PG) Propylene production from ethylene and raffinate-2. The process under analysis consists in a metathesis process similar to Lummus Technology's Olefins Conversion Technology (OCT). The economic analysis performed assumes a plant located in the United States.

Details: 350 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 350 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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