Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 379
ICC - Report ID: 379-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Ethylidene Norbornene Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 290-A,201-A,173-B,173-A
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":"1999","2":"1999","3":"1999"},"2":{"1":"2999","2":"2999","3":"2999"},"3":{"1":"4799","2":"4799","3":"4799"}},"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/379-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Ethylidine Norbornene</b></p>, <p><b>Fuel</b></p> <h6>Raw Materials</h6> <p><b>Butadiene</b></p>, <p><b>Chemicals</b></p>, <p><b>Dicyclopentadiene</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/379-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Thermal Cracking; (2) Diels-Alder Reaction; (3) VNB Purification; and (4) Isomerization.</p><p>(1) Thermal Cracking. Fresh and recycled dicyclopentadiene (DCPD) streams are mixed and fed to a stirred tank reactor filled with diphenylether. Upon contact with the reaction medium, the DCPD quickly reaches the high temperature required to trigger the dimer's thermal cracking and produces cyclopentadiene (CPD). The reactor has a reflux condenser coupled to its top exit, which ensures that only the evaporated CPD produced leaves to proceed to the Diels-Alder reaction step, while via a side exit the reactors liquid medium is continuously fed to a distillation column responsible for removing the tetrahydroindene (THI) by-product.</p><p>(2) Diels-Alder Reaction. The CPD produced is then fed to a tubular reactor along with butadiene to react and produce 5-vinyl-2-norbornene (VNB) as well as the by-products 4-vinylcyclohexene (VCH), THI, DCPD, and oligomers. The reactor's outlet stream is fed to a distillation column where the unreacted reactants are recovered as distillate and recycled to the reactor along with the solvent (toluene), while the products come out as the bottom stream and proceed to purification downstream.</p><p>(3) VNB Purification. The reaction products go through three distillation columns. The first one is responsible for removing VCH. In the second column, the main reaction product, VNB, is separated from the heavy impurities and sent to the isomerization reactor downstream. In the third column, the produced DCPD and THI are separated from the oligomers and recycled to the thermal cracking reactor.</p><p>(4) Isomerzation. The purified VNB is then fed to a tubular fixed bed reactor packed with catalyst where it is converted into the target product, 5-Ethylidene-2-Norbornene (ENB).</p>
ICC - Short Description: This report presents the economics of 5-Ethylidene-2-Norbornene (ENB) production from dicyclopentadiene and butadiene based on an industrial plant located in the United States.. Initially, dicyclopentadiene is cracked into cyclopentadiene. The cyclopentadiene obtained is subjected to Diels-Alder reaction with butadiene to produce 5-vinyl-2-nor bornene (VNB); which in then isomerized to 5-Ethylidene-2-Norbornene.
ICC - Main Product: Ethylidene Norbornene
ICC - Plant Capacity: 25.00
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ICC - Images Count: {"versions":{"1":"9","2":"13","3":"22"}}
ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Ethylidene Norbornene Production

Ethylidene Norbornene Production Costs Report | Issue A | Q2 2024

Production Cost Report

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

This report presents a cost analysis of a 25 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

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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 Ethylidene Norbornene 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 Ethylidene Norbornene 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 Ethylidene Norbornene 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 Ethylidene Norbornene 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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