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This report approaches the economics of L-Lysine Sulfate production from glucose syrup. In the process examined, glucose syrup is submitted to fed-batch fermentation to produce L-Lysine. The economic analysis provided assumes a plant located in the United States.

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This feasibility study approaches an economic analysis of L-Lysine Monohydrochloride (or L-Lysine-HCl) production from glucose syrup in the United States using a conventional fermentation process. The L-Lysine-HCl is recovered via ion-exchange absorption and crystallization.

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This report presents the economics of Lysine production from raw sugar (sucrose). Sucrose is initially hydrolyzed into glucose and fructose (invert sugar). The invert sugars are then fermented to produce L-Lysine, which is recovered as L-Lysine-HCl. The economic analysis provided assumes a plant located in Germany.

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