Commodity Production Costs Report
Acetone Production from Propylene (Single-Step Process)
Acetone Operating Costs & Plant Construction Costs
This report approaches the economics of Acetone production from propylene in the United States. In the process examined, a direct propylene oxidation is carried out in the presence of palladium chloride and copper chloride, yielding Acetone.
The report provides a comprehensive study of Acetone production and related Acetone production cost, covering three key aspects: a complete description of the Acetone production process examined; an in-depth analysis of the related Acetone plant capital cost (Capex); and an evaluation of the respective Acetone plant operating costs (Opex).
The Acetone 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 Acetone 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 Acetone plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Key reference(s): ?
Product
Acetone. Acetone, also known as 2-propanone, is the simplest ketone. It is used as solvent for a wide range of organic compounds (e.g. oils, fats, resins, waxes and gums). It is also used as feedstock for the production of several chemicals, such as methyl methacrylate, bisphenol A, and methyl isobutyl ketone. The main source of acetone is the process for phenol production from cumene, which generates acetone as by-product at an approximate ratio for 0.6 kg of acetone per kg of phenol. Industrial consumers of acetone usually receive shipments in large containers made of carbon steel, tank trucks made of stainless steel or aluminum, or rail tank cars made of carbon steel or aluminum. International shipments by sea are usually made in steel barges and amount at least 2,000 metric tons.
Raw Material
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.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Acetone 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 Acetone 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 Acetone 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 Acetone 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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Other Acetone Production Cost Reports
Acetone Production from Isopropanol
This feasibility study presents the economics of Acetone production from isopropanol using a liquid phase dehydrogenation process. The economic analysis presented in the study assumes a plant located in the United States.
Details: 30 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $999 USD
Acetone Production from Propylene (Two-Step Process)
This report presents the economics of a two-step process for Acetone production from propylene in the United States. In the process examined, propylene is hydrated in a catalytic reactor, producing isopropanol. Then, isopropanol is dehydrogenated in a fixed bed catalyst reactor to produce Acetone.
Details: 200 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $1,199 USD
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Other Related Production Cost Reports
Propylene Production from Propane (Moving-Bed Reactor)
This study presents the economics of Polymer Grade (PG) Propylene production from propane. The process consists in the dehydrogenation of propane, carried out in a moving-bed reactor, similar to UOP Oleflex. The economic analysis performed assumes a plant located in the United States.
Details: 550 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD
Isopropyl Alcohol Production from Acetone
In this report, it is approached the economics of Isopropyl Alcohol production from acetone in a typical acetone hydrogenation process, also assuming an industrial plant located in the United States. The reaction is carried out in liquid phase, in two fixed bed reactors in series, catalyzed by a Raney nickel catalyst.
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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.
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This report presents the economics of Polymer Grade (PG) Propylene production from ethylene and raffinate-2. The process under analysis consists in a metathesis process similar to Lummus Technology's Olefins Conversion Technology (OCT). The economic analysis performed assumes a plant located in the United States.
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