Ethylene Vinyl Acetate from Ethylene & VAM (Tubular Process)
Ethylene Vinyl Acetate Production Costs Report | Issue A | Q3 2024
Report Details |
220 kta United States-based plant | Q3 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.
Report Abstract
This study presents a techno-economic analysis of a typical Ethylene Vinyl Acetate production process from ethylene and vinyl acetate (VAM) using a high-pressure tubular polymerization process. The plant is assumed to be located in the United States.
The report provides a comprehensive study of Ethylene Vinyl Acetate production and related Ethylene Vinyl Acetate production cost, covering three key aspects: a complete description of the Ethylene Vinyl Acetate production process examined; an in-depth analysis of the related Ethylene Vinyl Acetate plant capital cost (Capex); and an evaluation of the respective Ethylene Vinyl Acetate plant operating costs (Opex).
The Ethylene Vinyl 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 Ethylene Vinyl 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 Ethylene Vinyl 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.
Process Schematic

The process under analysis comprises three major sections: (1) Polymerization; (2) Separation; and (3) Extrusion and Packaging.
Polymerization. Fresh and recovered ethylene are fed to a primary compressor to be pressurized to 300 bar. The outlet stream is mixed with dried fresh and recycled vinyl acetate monomer (VAM), and an unreacted monomers stream recovered downstream. This mixture is pressurized to 3000 bar in a secondary compressor, and then fed to a tubular reactor at different injection points, so the polymerization takes place. The reactor outlet is expanded to 300 bar and sent to a separation section.
Separation. Firstly, a High-Pressure Separation divides the molten copolymer from unreacted monomers, which are recycled to the 2nd compressor and to a VAM recycle condenser. Waxes formed during the polymerization are condensed and sent to disposal. The bottom stream from the HP Separation is passed through a Low-Pressure Separation, operating at 1.5 bar, to remove remaining unreacted monomers, which are sent to Wax Removal. The copolymer melt is sent to extrusion. A stream from the VAM recycle condenser is fed to a distillation column, were VAM is recovered and recycled to the second compressor, and heavies are disposed as waste.
Extrusion and Packaging. The copolymer melt from the LP Separation is further fed into an extruder, which is used to incorporate the required additives, as well as to pelletize the polymer. The product is then sent to product blending and storage.
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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 Ethylene Vinyl 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 Ethylene Vinyl 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 Ethylene Vinyl 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 Ethylene Vinyl 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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