Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: M
ICC - Volume: 172
ICC - Report ID: 172-M
ICC - Report Location: China
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Ethylene Production from Vacuum Gas Oil
ICC - Show Overview: 1
ICC - Report Location ID: 3
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-N,172-O,172-R,172-P,172-Q,172-S,172-T,172-U,172-V
ICC - Related Reports List: 198-F,230-A
ICC - Report Location Code: CHN
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/172-M.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Ethylene</b></p>, <p><b>Propylene</b></p>, <p><b>Pygas</b></p>, <p><b>Butadiene</b></p>, <p><b>Raffinate-1</b></p>, <p><b>Hydrogen</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Vacuum Gas Oil</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/172-M.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Cracking and Quenching; (2) Compression and Drying; and (3) Separation.</p><p>Cracking & Quenching. A vacuum gas oil is fed to furnaces in which it is cracked, forming ethylene, propylene and other by-products. The furnace outlet stream is fed to a quench, to prevent further reactions and formation of undesirable by-products. From a decanter downstream the quench tower, fuel oil and water to waste treatment are removed. Cracked gas from the quench is sent to compression and separation.</p><p>Compression & Drying. The compression of the cracked gas is performed across 5 stages. After the third stage, carbon dioxide and sulfur are removed from cracked gas by caustic soda and water washes in a caustic scrubber. The compressed cracked gas is cooled and then dried in molecular sieves, so that most of the water is removed.</p><p>Separation. The dried cracked gas is fed to a cold box to remove hydrogen and light hydrocarbons, minimizing ethylene losses. Condensates are fed to separation columns. In the demethanizer, methane is separated from the main stream that is fed to the deethanizer. The top of the deethanizer is fed to an acetylene converter and then fractionated in the C2-splitter. Polymer grade (PG) ethylene is obtained as main product. The deethanizer bottom stream is fed to a depropanizer, which distillates C3 components. This stream is catalytically hydrotreated for impurities removal, and then fed to the C3-splitter. PG propylene is drawn from the column as a side stream. The Depropanizer bottom stream is separated into a crude C4 stream, recovered as column overhead product, and pyrolysis gasoline by-product. The crude C4 stream is condensed and fed to extraction columns, in order to separate raffinate-1. The crude butadiene stream is fed to the distillation columns so as to purify butadiene .</p>
ICC - Short Description: This report provides a feasibility study of Ethylene production from vacuum gas oil (VGO) using a steam cracking process in China. In this process, VGO is thermally cracked in pyrolysis furnaces through the use of steam, generating ethylene and other by-products.
ICC - Main Product: Ethylene
ICC - Plant Capacity: 800.00
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Ethylene Production from Vacuum Gas Oil

Ethylene Production Costs Report | Issue M | Q2 2024

Production Cost Report

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Report Details
800 kta China-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 800 kta (kilo metric ton per annum) China-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

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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

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

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This report approaches the economics of Green Polymer Grade (PG) Ethylene production from hydrous ethanol using a dehydration process similar to the process developed by Scientific Design. In this process, the reaction system is composed of only one reactor and one furnace. The study also assumes a plant constructed in the United States.

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue O   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.

CG Ethylene Production from Ethanol

This report approaches the economics of Green Chemical Grade (CG) Ethylene production from hydrous ethanol using a dehydration process similar to the process developed by Scientific Design. In this process, the reaction system is composed of only one reactor and one furnace. The study assumes a plant constructed in the United States.

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue Q   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   |   Q2 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   |   Q2 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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