Commodity Production Costs Report

Ethyl Acetate Production from Ethanol and Acetic Acid

Ethyl Acetate Operating Costs & Plant Construction Costs

100 kta United States-based plant | 107 Pages | Issue A | Q3 2024
Starting at $799 USD | See Report Editions Prices

This study approaches the economics of Ethyl Acetate production from ethanol and acetic acid in the United States. In this process, Ethyl Acetate is produced by continuous esterification of acetic acid and ethanol.

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

The Ethyl Acetate 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 Ethyl Acetate 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 Ethyl Acetate 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): ?

Ethyl Acetate Production Cost Report Process Schematic

The process under analysis comprises two major sections: (1) Reaction and (2) Purification.

Reaction. In the process under analysis, the reaction is conducted in two steps. Firstly, the reactants, acetic acid and ethanol, in slight excess, are mixed together in pre-esterification reactors along with sulfuric acid, that is used as a catalyst for the esterification. This first reaction is conducted until equilibrium is reached and then the reactors output is directed to an esterification column. There, two methods are used to shift the reaction equilibrium towards the production of ethyl acetate: water by-product removing and excess ethanol addition. Excess ethanol is added to reaction medium via an upstream recycle stream that is fed to the bottom of the column. Water is continuously removed from the reaction medium through column bottoms while the reactants, and ethyl acetate move upward in the column.

Purification. The top product from the esterification column still containing a large excess of ethanol is directed to a further distillation step. The top product of this column is a ternary azeotrope of Ethyl Acetate, ethanol and water. To further purify Ethyl Acetate in the ternary azeotrope mixture it is first required to break down the azeotrope. The ternary azeotrope mixture is mixed with water and then settled in a decanter in order to break down the azeotrope. The organic phase recovered from the decanter, more concentrated in Ethyl Acetate, can now be directed to a final distillation step to reach product specification.

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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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 80 Pages | 22 Tables | 9 Images

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Table of Contents


Features
  • 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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 90 Pages | 28 Tables | 13 Images

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Updated with Q3 2024 Data

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Table of Contents


Features
  • 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
  • See All Features

  • 107 Pages | 34 Tables | 22 Images
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  • Updated with Q3 2024 Data
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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Ethyl Acetate 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 Ethyl Acetate 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 Ethyl Acetate 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 Ethyl Acetate 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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