Allyl Polyethylene Glycol Production
Allyl PEG Production Costs Report | Issue A | Q3 2024
Report Details |
11 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 11 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 Allyl Polyethylene Glycol (PEG) production in the United States. The analysis assumes an industrial plant that generates Allyl PEG starting from PEG and allyl chloride. In this batchwise process, methoxy polyethylene glycol ether (MPEG) reacts with allyl chloride to generate an allyl-terminated polyethylene glycol methyl ether (Allyl PEG).
The report provides a comprehensive study of Allyl PEG production and related Allyl PEG production cost, covering three key aspects: a complete description of the Allyl PEG production process examined; an in-depth analysis of the related Allyl PEG plant capital cost (Capex); and an evaluation of the respective Allyl PEG plant operating costs (Opex).
The Allyl PEG 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 Allyl PEG 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 Allyl PEG 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 two major sections: (1) Reaction; and (2) Purification.
Reaction. At first, the reactor is purged with nitrogen to guarantee an inert atmosphere during reaction and prevent side oxidative attack to MPEG. The reactor is then charged with MPEG, allyl chloride and catalyst (tetrabutylammonium bromide) at a molar ratio of 1:1.2:0.05 (MPEG:allyl chloride:catalyst). Once reactor is fully charged, its content is gradually heated to 60 °C. The reaction takes approximately 5 hours. During this period, a condenser at the top of the reactor guarantees that any allyl chloride vapors formed are returned to the reactor.
Purification. Once reaction is completed, the reactor mixture is sent to a mixing vessel. In that vessel, the reactor effluent is dissolved in ethyl acetate and washed multiple times with a saturated sodium chloride solution. The washed mixture is routed to a decanter, where an aqueous layer is separated from an organic phase comprising the reactor product. The remaining organic layer is than subjected to a vacuum evaporation step, in which ethyl acetate and remaining impurities are removed and a purified stream of Allyl PEG 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 Allyl PEG 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 Allyl PEG 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 Allyl PEG 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 Allyl PEG 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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Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 100 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.
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