Acrylic Acid Production from 3-Hydroxypropionic Acid
Acrylic Acid Production Costs Report | Issue M | Q3 2024
| Report Details |
| 150 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 150 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 Acrylic Acid production from 3-hydroxypropionic acid (3-HP). 3-HP is submitted to a dehydration reaction to generate Glacial Acrylic Acid. The reaction is carried out in vapor phase in a reactor column. The economic analysis approaches a plant located in the United States.
The report provides a comprehensive study of Acrylic Acid production and related Acrylic Acid production cost, covering three key aspects: a complete description of the Acrylic Acid production process examined; an in-depth analysis of the related Acrylic Acid plant capital cost (Capex); and an evaluation of the respective Acrylic Acid plant operating costs (Opex).
The Acrylic Acid 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 Acrylic Acid 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 Acrylic Acid 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 the following main sections: (1) Dehydration; (2) Separation; and (3) Purification.
Dehydration. The aqueous solution of 3-hydroxypropionic acid is passed through a reactor column, packed with gamma-alumina catalyst where the 3-HP is dehydrated to acrylic acid.
Separation. The product from dehydration is fed to an azeotropic distillation system, comprised of an extractive distillation column and a stripping column, for water removal. Toluene is used as azeotropic agent to facilitate the water removal.
Purification. The acrylic acid from azeotropic distillation is fed to the crude acrylic acid distillation for removal of remaining impurities, and finally submitted to a melt crystallization carried out in multitube exchangers. After operating cycles (alternating crystallizing/melting stages), glacial acrylic acid is obtained.
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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 Acrylic Acid 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 Acrylic Acid 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 Acrylic Acid 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 Acrylic Acid 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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