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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.
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.
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.
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).
This report presents a feasibility study of Phosphoric Acid Polyether production in a United States-based facility. In this case, phosphoric acid is the starter of the acid-catalyzed alkoxylation reaction to oligomerize propylene oxide.
This report presents a techno-economic analysis of Polytetramethylene Ether Glycol (PTMEG) production from tetrahydrofuran (THF) polymerization in the United States. The THF is polymerized by a strongly acidic catalyst, forming PTMEG.
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.
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.
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.
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.