Commodity Production Costs Report
Ethyl Acetate Production from Ethanol and Acetic Acid
Ethyl Acetate Operating Costs & Plant Construction Costs
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): ?

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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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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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
Other Ethyl Acetate Production Cost Reports

Ethyl Acetate Production from Ethanol
This report presents a techno-economic analysis of Ethyl Acetate production from ethanol via a process similar to the Johnson Matthey's Davy’s Ethyl Acetate technology. In this process, ethanol is dehydrogenated to acetaldehyde, which further reacts with ethanol to form Ethyl Acetate. The economic analysis provided assumes a plant located in the United States.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Ethyl Acetate Production from Ethylene and Acetic Acid
This report examines the economics of Ethyl Acetate production from ethylene and acetic acid in the United States. The process examined is similar to the BP’s AVADA (AdVanced Acetates by Direct Addition of acetic acid to ethylene) technology.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $799 USD

Ethyl Acetate Production from Acetaldehyde
This report examines the economics of Ethyl Acetate production from acetaldehyde in the United States via Tishchenko reaction, which refers to the dimerization of acetaldehyde in the presence of an alkoxide catalyst to form the ester.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue D | From $799 USD
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