Ethylene Vinyl Acetate from Ethylene & VAM (Autoclave Process)
Ethylene Vinyl Acetate Production Costs Report | Issue B | Q4 2024
| Report Details |
| 180 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 180 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 report provides the economics of a typical Ethylene Vinyl Acetate production process from ethylene and vinyl acetate (VAM) in the United States. The process examined in this report employs a high-pressure autoclave polymerization.
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 ethylene is fed to a primary compressor to be pressurized to 210 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 1500 bar in a secondary compressor, and then fed to a tubular reactor at different injection points, where polymerization takes place. The reactor outlet is expanded to 250 bar and sent to the separation section.
Separation. Firstly, a High-Pressure (HP) Separation divides the molten copolymer from unreacted monomers, which are recycled to the 2nd compressor and directed 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 (LP) 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 wasted.
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 Blending Silos & Packaging, where it is packaged and sent to storage.
Up-to-date PDF Report
Professional report based on Q4 2024 economic data, ensuring timely evaluations.
Multiple Use Cases
Ideal for investment screening, feasibility studies, cost estimates, and research planning.
Proven Methodology
Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Compact
$799 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Pages | Tables | Images
Read-only Online PDF Format
Updated with Q4 2024 Data
DETAILED
$1,599 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Pages | Tables | Images
Downloadable PDF Format
Updated with Q4 2024 Data
PREMIUM
MOST POPULAR
$2,699 USD
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
Pages | Tables | Images
Print-enabled PDF Format Add-on
Updated with Q4 2024 Data
Share with Co-workers
Technical Support via Email
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
Other Ethylene Vinyl Acetate Production Cost Reports
Ethylene Vinyl Acetate from Ethylene & VAM (Tubular Process)
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.
Details: 220 kta United States-based plant | Q4 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 220 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.
Could Not Find the Report You Need?
Obtain a Bespoke Report
Get a report targeting the process in which you are interested
See Offer Details
Understand Bespoke Reports and how you can easily order them
Check Editions & Pricing
Complete a brief form and see a quotation for your Bespoke Report
Other Related Production Cost Reports
Ethylene Production from Naphtha (Low Severity Steam Cracking)
This report presents the economics of a naphtha-based steam cracker, equipped with an electricity cogeneration unit. In this process, naphtha is thermally cracked at low severity conditions, maximizing propylene to Ethylene ratio. The analysis is based on a plant located in Germany.
Details: 800 kta Germany-based plant | Q4 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 800 kta (kilo metric ton per annum per annum) Germany-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Ethylene Production from Ethane
This report presents the economics of Polymer Grade (PG) Ethylene production from ethane in the United States. In the process under analysis, ethane is thermally cracked in pyrolysis furnaces through the use of steam, yielding Ethylene. A hydrogen-rich gas is generated as by-product.
Details: 1,200 kta United States-based plant | Q4 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 1,200 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.
Vinyl Acetate Production from Acetic Acid and Ethylene
This study presents the economics of Vinyl Acetate production from acetic acid and ethylene in the United States, via a typical vapor-phase oxidation process. In this process, vapor acetic acid, ethylene and oxygen react in a catalytic multi-tube reactor, producing Vinyl Acetate, which is further purified.
Details: 350 kta United States-based plant | Q4 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.
Vinyl Acetate Production from Acetic Acid and Acetylene
This feasibility study examines the economics of a process producing Vinyl Acetate from acetic acid and acetylene. In the process examined, acetic acid and acetylene react in the vapor phase in the presence of a supported metal catalyst to produce vinyl acetate. The economic analysis performed is based on a plant constructed in the United States.
Details: 180 kta United States-based plant | Q4 2024 | 107 pages | Issue B From $799 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.
+800 Reports Developed, Targeting +250 Commodities
Best-in-Class Reports
Analysis of capital and operating costs of commodity production processes. Prices starting at $799 USD
Vast Report Library
858 independent and up-to-date reports examining embryonic and established production processes
Free Sample Reports
Quickly understand the structure and depth of content of our professional reports