Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 214
ICC - Report ID: 214-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Glycerol-Propoxylated Polyether (0 wt% EO) Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 214-A,214-C,214-D,214-E,214-F,214-G,214-H,214-I,214-J
ICC - Related Reports List: 004-A,183-B,183-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"2":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"3":{"1":{"time":"11","price":0},"2":{"time":"6","price":"599"}}},"unit":"d"}
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ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/214-B.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Polyether</b>. Polyether is a class of organic substances produced by polymerized monomers by ether links which may be structured in chain or network. It is a diverse group of polymers most notably polyethylene glycols, polypropylene glycols, epoxy resins and phenoxy resins.</p> <h6>Raw Materials</h6> <p><b>Glycerol</b>. Glycerol is a versatile, naturally-derived compound widely used in pharmaceuticals, personal care products, and food industries as a humectant, sweetener, and solvent. It also serves as a raw material for the production of resins and polyols used in polyurethane foams. Glycerol is primarily obtained as a byproduct from biodiesel production or through the hydrolysis of fats and oils. It is stored as a viscous liquid at ambient conditions and is highly valued for its non-toxicity and biodegradability.</p> <b>Propylene Oxide</b>. Propylene Oxide (PO) is a major commodity chemical. This highly reactive compound is starting material for several products, from polymers and solvents to industrial fluids. Commercially, Propylene Oxide is produced mainly by the so-called chlorohydrin process, based on the reaction of propylene and chlorine in the presence of water to produce propylene chlorohydrin, which is dehydrochlorinated with a base (caustic or lime). PO may also be produced on commercial scale by the oxidation of propylene by organic hydroperoxides – the so called indirect oxidation routes – yielding alcohols as by-product.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/214-B.jpg
ICC - Short Description: This report presents a techno-economic study of a process for Glycerol-Propoxylated Polyether production from propylene oxide and glycerol starter.  In this process, Polyether is produced from propylene oxide using glycerol as starter in the base-catalyzed alkoxylation reaction. Ethylene oxide (EO) is not used in this process. The analysis considers a plant erected in the United States.
ICC - Main Product: Polyether
ICC - Plant Capacity: 50.00
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Glycerol-Propoxylated Polyether (0 wt% EO) Production

Polyether Production Costs Report | Issue B | Q2 2024

Production Cost Report

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Report Details
50 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 50 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.

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Production Process Information

Process Consumptions

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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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

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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Polyether 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 Polyether 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 Polyether 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 Polyether 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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Glycerol-Propoxylated Polyether (5 wt% EO) Production

This report presents the economics for the production of Glycerol-Propoxylated Polyether in the United States from propylene oxide. Glycerol is used a starter for the polymerization, and ethylene oxide (EO) is used in the end of the reaction to form an end-cap in the Polyether structure (5 wt% of ethylene oxide content).

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Glycerol-Propoxylated Polyether (20 wt% EO) Production

This report provides a feasibility analysis of a process for Glycerol-Propoxylated Polyether production from propylene oxide, ethylene oxide (EO) and glycerol starter via a base-catalyzed alkoxylation. The analysis considers a plant constructed in the United States and a final polyether product containing 20 wt% of ethylene oxide in its structure.

Details: 50 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 50 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.

TMP-Propylene Oxide Polyether Production

This report presents the economics of TMP-Propylene Oxide Polyether production in the United States. In this process, Polyether is produced from propylene oxide using trimethylolpropane (TMP) as starter in the base-catalyzed alkoxylation reaction.

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Phosphoric Acid Polyether Production

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The cost analyses presented in this report target a 25 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.

Sorbitol-Based Polyether Production

This report presents a techno-economic analysis of Sorbitol-Based Polyether production. The process examined in this report uses sorbitol as reaction starter. The economic analysis presented assumes a plant located in the USA.

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The cost analyses presented in this report target a 25 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.

Sucrose-Based Polyether Production

This report presents an economic analysis for Sucrose-Based Polyether production. In this process, Polyether is produced from propylene oxide using sucrose as reaction starter. The economic analysis presented is based on a plant constructed in the United States.

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The cost analyses presented in this report target a 25 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.

TDA-Based Polyether Production

This study analyses the economics of TDA-Based Polyether production in the United States. In this process, Polyether is produced from propylene oxide using toluenediamine (TDA) as starter in the base-catalyzed alkoxylation reaction.

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Acrylonitrile Graft Polyether Production

This report presents an economic analysis of Acrylonitrile Graft Polyether production from acrylonitrile and glycerol-propoxylated polyether in the United States. In this case, acrylonitrile is grafted into the polyether, forming a copolymer polyol.

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The cost analyses presented in this report target a 25 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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This report presents the economics of a process for Technical Grade Glycerol production from crude glycerol in the United States. This treatment consists of pretreatment and vacuum distillation steps.

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Propylene Oxide Production from Propylene and Chlorine

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