Butanediol Production from Propylene
Butanediol Production Costs Report | Issue F | Q4 2024
Report Details |
65 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 65 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 feasibility analysis is about 1,4-Butanediol (BDO) production from propylene in the United States using an allyl alcohol process. Initially, propylene is reacted with acetic acid and oxygen, producing allyl acetate. The allyl acetate is then hydrolyzed, yielding allyl alcohol. Finally, the allyl alcohol is converted by hydroformylation and hydrogenation to BDO.
The report provides a comprehensive study of Butanediol production and related Butanediol production cost, covering three key aspects: a complete description of the Butanediol production process examined; an in-depth analysis of the related Butanediol plant capital cost (Capex); and an evaluation of the respective Butanediol plant operating costs (Opex).
The Butanediol 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 Butanediol 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 Butanediol 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
Butanediol. Butanediol is a versatile organic chemical used as an intermediate in the production of a wide range of industrial and consumer products. It plays a crucial role in manufacturing polyurethanes, engineering plastics, and fibers, and is also used in the synthesis of pharmaceuticals, solvents, and coatings. Butanediol is typically produced through the hydrogenation of maleic anhydride or succinic acid. It is handled and stored as a stable liquid at room temperature, and its demand continues to grow in sectors such as automotive, construction, and electronics.
Raw Materials
Propylene. Propylene, the main raw material consumed, is a colorless gas at room temperature. It is a low-boiling, flammable, and highly volatile gas, with molecular formula C3H6. Propylene reacts vigorously with oxidizing materials. It may be mildly irritating to the nose, throat, and respiratory tract; propylene has low acute toxicity from inhalation. PG Propylene has been mainly produced as ethylene manufacturing co-product (via steam cracking of paraffinic hydrocarbons) and by-product of petroleum refining (separation from refinery gas). Most recently, amid a tight propylene market, new and novel lower-cost chemical processes for on-purpose propylene production have emerged.
Acetic Acid. Acetic acid (also known as ethanoic acid, hydrogen acetate) is a carboxylic acid found in dilute solutions in plant and animal systems. This chemical is widely used in organic processes, primarily in the production of polymers derived from vinyl acetate, used in paints and coatings, cellulose used to produce acetate fibers, and as solvent. While 2–12 wt% acetic acid solutions, usually called vinegar, have long been produced by ethanol fermentation, nowadays the commercial production of acetic acid is mainly based on methanol carbonylation and liquid-phase oxidation of n-butane.
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Production Process Information
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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 Butanediol 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 Butanediol 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 Butanediol 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 Butanediol 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 Butanediol Production Cost Reports
Butanediol Production from Butadiene
This assessment examines a technology similar to the process proposed by Mitsubishi Chemical for 1,4-Butanediol (BDO) production from butadiene (BD) in the United States. In this process, BDO is produced from BD via acetoxylation.
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The cost analyses presented in this report target a 65 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.
Butanediol from Raw Sugar (By-Products: THF & Ammonium Sulfate)
This report concerns the bio-based BDO production in the Germany from raw sugar. In this report, BDO is produced using a two-step process similar to Myriant/JM Davy technology. In this process, raw sugar is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are fermented to produce to succinic acid, that is then hydrogenated to BDO. Ammonium sulfate and tetrahydrofuran (THF) are generated as by-products.
Details: 65 kta Germany-based plant | Q4 2024 | 107 pages | Issue J From $1,199 USD
The cost analyses presented in this report target a 65 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.
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