Commodity Production Costs Report

Toluene Diisocyanate from Toluene (Liquid-Phase Phosgenation)

Toluene Diisocyanate Operating Costs & Plant Construction Costs

220 kta United States-based plant | 107 Pages | Issue D | Q3 2024
Starting at $1,499 USD | See Report Editions Prices

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.

The report provides a comprehensive study of Toluene Diisocyanate production and related Toluene Diisocyanate production cost, covering three key aspects: a complete description of the Toluene Diisocyanate production process examined; an in-depth analysis of the related Toluene Diisocyanate plant capital cost (Capex); and an evaluation of the respective Toluene Diisocyanate plant operating costs (Opex).

The Toluene Diisocyanate production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Toluene Diisocyanate plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Toluene Diisocyanate plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.

Key reference(s): ?

Toluene Diisocyanate Production Cost Report Process Schematic

The process under analysis comprises three major sections: (1) Toluene Nitration; (2) DNT Reduction; and (3) TDA Phosgenation.

Toluene Nitration. The nitration of toluene occurs in two steps. In the first step Toluene reacts with nitric acid (HNO3), in the presence of sulfuric acid, to form three mononitrotoluene isomers ortho-, meta- and para-mononitrotoluenes. In the second step, nitric acid reacts with mononitrotoluene isomers in the presence of sulfuric acid to form dinitrotoluene (DNT), as indicated below. The acid concentration is controlled to prevent the formation of trinitrotoluenes. A mix of isomers result from the second step nitration, but the mixture essentially contains about 80/20 wt% of 2,4-DNT and 2,6-DNT. The effluent is sent to a caustic wash to neutralize remaining acids.

DNT Reduction. In the reduction stage, DNT is hydrogenated in the presence of hydrogen and a Raney Nickel catalyst. Methanol is used as a solvent to keep the catalyst in suspension in the reaction medium. No isomerization takes places, so the DNT isomers are converted to their corresponding diamines. After a few purification steps 80/20 TDA is directed to next section while catalysts and reagents are recycled.

TDA Phosgenation. The final stage, the phosgenation of TDA, also takes place in two steps. First, TDA reacts with a molecule of phosgene to yield toluene dicarbamyl dichloride (TDD). Then, toluene dicarbamyl dichloride is decomposed into toluene diisocyanate and hydrochloric acid. The outlet stream from the reaction zone is subsequently quenched, and most of the unreacted phosgene, hydrogen chloride and other light by-products are separated as a gaseous phase. After a few purification steps 80/20 TDI is recovered as the final product and hydrogen chloride is absorbed into water to be sold as a 32 wt% HCl solution.

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Table of Contents


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  • Production Process Information
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  • 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 Toluene Diisocyanate 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 Diisocyanate 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 Diisocyanate 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 Diisocyanate 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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