Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 39
ICC - Report ID: 039-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Toluene Production from Reformate
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 039-A,039-B
ICC - Related Reports List: 267-A,059-D,201-A,267-B
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"2":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"3":{"1":{"time":"11","price":0},"2":{"time":"6","price":"599"}}},"unit":"d"}
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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/039-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Toluene</b>. Toluene (also known as Methylbenzene) is an aromatic hydrocarbon mainly used as an industrial feedstock and as solvent. A significant part of toluene production is blended directly into gasoline pools. Other major use of this chemical is in the manufacture of the more valuable benzene, through hydrodealkylation. Most of toluene is produced via catalytic reforming of refinery streams (C6–C9 naphthas), along with benzene, xylenes, and C9-aromatics.</p> <p><b>Benzene</b>. Benzene (C6H6) is a flammable and volatile liquid. As the most simple aromatic hydrocarbon, it is used as an intermediate to produce many important chemicals, such as styrene (raw material for polystyrene and synthetic rubber), cyclohexane (used in nylon production), alkylbenzenes (used in detergent industry), aniline (used to produce dyes and polyurethanes), and chlorobenzenes. Also, benzene is used to produce pharmaceuticals, specialty chemicals, plastics, and pesticides. It occurs naturally in crude oil and coal tar. </p> <h6>Raw Material</h6> <p><b>Reformate</b>. Reformate (BTX) is a blend of benzene, toluene, and xylene, used as a feedstock for the petrochemical industry to produce key aromatic chemicals for plastics, fibers, and solvents. Reformate is produced by catalytic reforming of naphtha and is stored as a liquid. Its use in the production of styrene, phenol, and nylon makes it a cornerstone of the chemical industry.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/039-A.jpg
ICC - Short Description: This report presents the economics of Toluene production from reformate. The reformate is submitted to a typical sulfolane liquid-liquid extraction, giving a mixture of aromatics, which is further processed to yield pure Toluene. Benzene and mixed xylenes are produced as by-products. The economic analysis presented is based on a plant constructed in the United States.
ICC - Main Product: Toluene
ICC - Plant Capacity: 350.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Toluene Production from Reformate

Toluene Production Costs Report | Issue A | Q2 2024

Production Cost Report

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Report Details
350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 350 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

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

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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 Toluene 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 Toluene 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 Toluene 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 Toluene 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 Toluene Production Cost Reports

Toluene Production from Reformate

This report presents the economics of Toluene production from reformate. The reformate is submitted to a typical sulfolane liquid-liquid extraction, giving a mixture of aromatics, which is further processed to yield pure Toluene. Benzene and mixed xylenes are produced as by-products. The economic analysis presented is based on a plant constructed 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.

Toluene Production from Pygas

This study presents the economics of Toluene production from pyrolysis gasoline (pygas) in the United States using a typical liquid-liquid extraction process.

Details: 400 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 400 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

Toluene Diisocyanate from Toluene (Liquid-Phase Phosgenation)

This report presents the economics of a typical liquid-phase phosgenation process for Toluene Diisocyanate (TDI) production from toluene and chlorine in the USA. Initially, toluene is submitted to a dinitration to produce dinitrotoluene (DNT), which is then hydrogenated to toluenediamine (TDA). This TDA is reacted with phosgene in liquid phase to yield TDI product. The phosgene used is generated from chlorine in an on-site unit.

Details: 220 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $1,499 USD

The cost analyses presented in this report target a 220 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.

Ethylene Propylene Rubber Production

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.

Details: 100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 100 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.

Reformate from Naphtha (Continuous Catalyst Regeneration)

This feasibility study is about Reformate production from naphtha in the United States. The process evaluated is a continuous catalyst regeneration (CCR) process similar to the UOP CCR Platforming technology. In this process, naphtha is reformed through a series of reactions, in which paraffins are converted to aromatics.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 800 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.

Reformate from Naphtha (Semi-Regeneration)

This study reviews the costs associated with Reformate production from naphtha in the United States. The process under analysis is a semi-regeneration process similar to UOP RZ Platforming technology. In this process, naphtha is reformed through a series of reactions, in which paraffins are converted to aromatics. Hydrogen is generated as by-product.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 800 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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