2015•Industrial & Engineering Chemistry ResearchRequires access

Technoeconomic Analysis of the Production of Epichlorohydrin from Glycerol

Alberto Almena, Mariano Martı́n

Open publisher page 165 citations

Abstract

In this work we evaluate the production of epichlorohydrin from glycerol, the main byproduct in the biodiesel industry. A process flowsheet is synthesized consisting of glycerol purification, reaction with HCl, and final reaction with NaOH to produce epichlorohydrin. Both reactions are complex equilibriums, and recovery of the reaction medium, hexanoic acid, and purification of the products are required. The process is selected based on the use of cheap and available secondary raw materials, namely HCl and NaOH, compared to other technical alternatives. We couple MATLAB with CHEMCAD to simulate the mass and energy balances. Finally, the economic analysis of the process shows that the process is profitable due to the high selling cost of the epichlorohydrin. For the production of 26.5 kt/yr of epichlorohydrin 99.9%, 41.5 kt/yr of glycerol, 29 t/y of HCl, and 15.9 kt/yr of NaOH are needed. The investment adds up to 63.7 M€ with a production cost of 1.28 €/kg.

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What this paper is about

In this work we evaluate the production of epichlorohydrin from glycerol, the main byproduct in the biodiesel industry. A process flowsheet is synthesized consisting of glycerol purification, reaction with HCl, and final reaction with NaOH to produce epichlorohydrin. Both reactions are complex equilibriums, and recovery of the reaction medium, hexanoic acid, and purification of the products are required. The process is selected based on the use of cheap and available secondary raw materials, namely HCl and NaOH, compared to other technical alternatives. We couple MATLAB with CHEMCAD to simulate the mass and energy balances. Finally, the economic analysis of the process shows that the process is profitable due to the high selling cost of the epichlorohydrin. For the production of 26.5 kt/yr of epichlorohydrin 99.9%, 41.5 kt/yr of glycerol, 29 t/y of HCl, and 15.9 kt/yr of NaOH are needed. The investment adds up to 63.7 M€ with a production cost of 1.28 €/kg.

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Available abstract

In this work we evaluate the production of epichlorohydrin from glycerol, the main byproduct in the biodiesel industry. A process flowsheet is synthesized consisting of glycerol purification, reaction with HCl, and final reaction with NaOH to produce epichlorohydrin. Both reactions are complex equilibriums, and recovery of the reaction medium, hexanoic acid, and purification of the products are required. The process is selected based on the use of cheap and available secondary raw materials, namely HCl and NaOH, compared to other technical alternatives. We couple MATLAB with CHEMCAD to simulate the mass and energy balances. Finally, the economic analysis of the process shows that the process is profitable due to the high selling cost of the epichlorohydrin. For the production of 26.5 kt/yr of epichlorohydrin 99.9%, 41.5 kt/yr of glycerol, 29 t/y of HCl, and 15.9 kt/yr of NaOH are needed. The investment adds up to 63.7 M€ with a production cost of 1.28 €/kg.

Key concepts: Epichlorohydrin, Glycerol, Raw material, Chemistry, Biodiesel production, Production (economics), Pulp and paper industry, Petrochemical

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