Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 268
ICC - Report ID: 268-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Dinitrotoluene Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 039-A,059-E,088-E,059-C,088-C,039-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/268-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Dinitrotoluene</b>. Dinitrotoluene is an intermediate chemical used in the production of toluene diisocyanate (TDI) and explosives. It is a key component in polyurethane foam production and in making dyes and plasticizers. Dinitrotoluene is produced by nitrating toluene with nitric acid and sulfuric acid, and it is stored as a yellow crystalline solid. Its application in both the explosive and polyurethane industries illustrates its diverse industrial significance.</p> <h6>Raw Materials</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> <b>Nitric Acid</b>. Nitric acid is a strong oxidizing acid used in the production of fertilizers, explosives, and in various chemical syntheses. It also plays a critical role in metal processing and the production of nitrates. Nitric acid is produced by oxidizing ammonia via the Ostwald process and is stored as a liquid. Its ability to act as both an oxidant and a nitrating agent makes it a key component in the production of ammonium nitrate for both agricultural and industrial applications.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/268-A.jpg
ICC - Short Description: This feasibility study provides an economic analysis of Dinitrotoluene (DNT) production from toluene and nitric acid in the United States via a two-step nitration process. Initially, nitric and sulfuric acids are reacted with toluene to form mononitrotoluene, which is further nitrated to produce DNT.
ICC - Main Product: Dinitrotoluene
ICC - Plant Capacity: 220.00
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Dinitrotoluene Production

Dinitrotoluene Production Costs Report | Issue A | Q2 2024

Production Cost Report

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220 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 220 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

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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

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Dinitrotoluene 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 Dinitrotoluene 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 Dinitrotoluene 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 Dinitrotoluene 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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Other Related 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.

Toluene Diisocyanate from DNT and Cl2 (Liquid-Phase Phosgenation)

This study presents the costs associated with Toluene Diisocyanate (TDI) production from dinitrotoluene (DNT) and chlorine in the United States. Initially, DNT is hydrogenated to toluenediamine (TDA), which is reacted with phosgene in liquid phase to produce TDI. The phosgene used in this process is generated from chlorine and carbon monoxide in an on-site unit.

Details: 180 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $1,199 USD

The cost analyses presented in this report target a 180 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 Diisocyanate from DNT and Cl2 (Gas-Phase Phosgenation)

This report shows a techno-economic analysis about Toluene Diisocyanate (TDI) production from dinitrotoluene (DNT) and chlorine in the United States. The process examined in this report is similar to the Bayer gas-phase phosgenation (GPP) technology. DNT is hydrogenated to toluenediamine (TDA), which then reacts with phosgene in gas phase to produce TDI. The phosgene used in generated from chlorine.

Details: 180 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   From $1,199 USD

The cost analyses presented in this report target a 180 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.

Weak Nitric Acid from Ammonia (Dual Pressure Process)

In this report, it is approached the economics of Weak Nitric Acid (65 wt%) production from ammonia in a typical dual pressure process, assuming an industrial plant located in the United States. Initially, ammonia is oxidized to nitric oxide at medium pressure. Then, nitric oxide is oxidized to form nitrogen dioxide, and absorbed at high pressure by water producing nitric acid.

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

Concentrated Nitric Acid Production from Weak Nitric Acid

This study presents a feasibility analysis of Concentrated Nitric Acid (99 wt%) production from weak nitric acid (65 wt%) by extractive distillation using sulfuric acid as dehydrating agent. The economic analysis assumes a plant constructed in the United States.

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