2-Ethylhexanol Production from Butyraldehyde
Ethylhexanol Production Costs Report | Issue B | Q2 2024
Report Details |
160 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
This report presents a cost analysis of a 160 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 presents the economics of 2-Ethylhexanol (2-EH) production from n-butyraldehyde. The process under analysis dehydrates n-butyraldehyde to obtain 2-ethylpropylacrolein, which is then hydrogenated to form the 2-Ethylhexanol. The economic assessment assumes a plant located in the United States.
The report provides a comprehensive study of Ethylhexanol production and related Ethylhexanol production cost, covering three key aspects: a complete description of the Ethylhexanol production process examined; an in-depth analysis of the related Ethylhexanol plant capital cost (Capex); and an evaluation of the respective Ethylhexanol plant operating costs (Opex).
The Ethylhexanol 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 Ethylhexanol 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 Ethylhexanol 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 Overview
Product
2-Ethylhexanol. 2-Ethylhexanol (also known as 2-EH) is an eight-carbon branched chain alcohol. It is one of the most important oxo alcohols sold in commerce, widely used in the production of emollients and plasticizers. The production on commercial scale of this alcohol is based on the aldol condensation of n-butyraldehyde (n-butanal) and the hydrogenation of the hydroxyaldehyde formed. In fact, 2-EH is commonly produced in integrated complexes based on OXO processes, where n-butanal is first obtained by hydroformylation of propylene, and then converted into the aldol, dehydrated and hydrogenated to 2-ethylhexanol; n-butanol and isobutanol can also be produced.
Raw Materials
Hydrogen. The hydrogen molecule, H2, is the normal state of pure hydrogen, even though hydrogen can be found in its atomic form under specific conditions. It is a very stable molecule, not usually reactive under normal conditions. Essentially, molecular hydrogen is produced industrially by three different methods: hydrocarbons steam reforming, hydrocarbons partial oxidation and water electrolysis. Hydrogen can also be obtained as a by-product recovered in processes such as the manufacture of styrene from ethylbenzene.
n-Butyraldehyde. n-Butyraldehyde is an organic compound used as an intermediate in the production of plasticizers, solvents, and rubber accelerators. It is prized for its ability to undergo further reactions in chemical synthesis. n-Butyraldehyde is produced via the hydroformylation of propylene and stored as a liquid. Its reactivity and use in producing chemicals for plastics and rubber make it valuable to the chemical industry.
Up-to-date PDF Report
Professional report based on Q2 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 Q2 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 Q2 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 Q2 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 Ethylhexanol 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 Ethylhexanol 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 Ethylhexanol 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 Ethylhexanol 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 Ethylhexanol Production Cost Reports
2-Ethylhexanol Production from Propylene and Syngas
This report presents the economics of 2-Ethylhexanol (2-EH) production from propylene and syngas located in the United States. Initially, propylene reacts with syngas in a hydroformylation reaction, yielding n-butyraldehyde. This step uses a conventional OXO-alcohol technology. Then, the n-butyraldehyde is submitted to an aldolization, and is subsequently dehydrated to 2-ethylpropylacrolein (EPA). Finally, the EPA is hydrogenated, yielding 2-EH.
Details: 160 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $1,199 USD
The cost analyses presented in this report target a 160 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.
2-Ethylhexanol Production from Butyraldehyde
This report presents the economics of 2-Ethylhexanol (2-EH) production from n-butyraldehyde. The process under analysis dehydrates n-butyraldehyde to obtain 2-ethylpropylacrolein, which is then hydrogenated to form the 2-Ethylhexanol. The economic assessment assumes a plant located in the United States.
Details: 160 kta United States-based plant | Q2 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 160 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
Methyl Methacrylate Production from Acetone, NH3 and Natural Gas
This report presents the economics of a process similar to Evonik Aveneer for Methyl Methacrylate (MMA) production from acetone and hydrogen cyanide (HCN) in the United States. Initially, HCN is produced from ammonia (NH3) and natural gas in an on-site unit. Then, acetone and methanol are used as raw materials for the production of MMA in six main steps, which are described in the report.
Details: 120 kta United States-based plant | Q2 2024 | 107 pages | Issue C From $1,499 USD
The cost analyses presented in this report target a 120 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.
2-Ethylhexyl Acrylate Production
This report approaches the production of 2-Ethylhexyl Acrylate (2-EHA) from acrylic acid and 2-ethylhexanol. The process examined is similar to the Synthomer's 2-EHA Process. In this process acrylic acid and n-butanol are directly converted to 2-EHA via an esterification reaction catalyzed by p-Toluene Sulfonic Acid. The economic analysis performed assumes a plant located in the United States.
Details: 40 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 40 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.
Hydrogen Production from Natural Gas (Steam Reforming)
This report provides an economic analysis of Hydrogen production from natural gas in the United States using a steam reforming process. Initially, methane present in natural gas is cracked with steam generating syngas. Then, the carbon monoxide from syngas is reacted with steam, producing carbon dioxide and additional hydrogen.
Details: 1,000 MM Nm3/y United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 1,000 MM Nm3/y (MM Nm3 per year 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.
Hydrogen Production from Natural Gas (Partial Oxidation Process)
This study provides a techno-economic study of Hydrogen production from natural gas in the United States. In this analysis, natural gas is submitted to a thermal partial oxidation process, producing syngas, which is passed through a shift converter to enrich the Hydrogen output.
Details: 25 MM Nm3/y United States-based plant | Q2 2024 | 107 pages | Issue C From $799 USD
The cost analyses presented in this report target a 25 MM Nm3/y (MM Nm3 per year 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.
Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 30:1)
This report presents an economic analysis of n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. The production ratio of n- to iso-butyraldehyde is about 30.
Details: 160 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 160 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