Abstract
γ-aminobutyric acid, a critical neurotransmitter, is experiencing an increasing demand in the medical and health fields. Conventional processes for γ-aminobutyric acid purification from fermentation broth encounter significant challenges, such as high ethanol usage, low yield, complex process flow, and environmental pollution. Therefore, a purification process based on crystallization techniques was developed to address the above issues. The process was implemented in two stages: desalination and γ-aminobutyric acid treatment. Na(2)SO(4) was effectively removed through a cooling crystallization technique. γ-aminobutyric acid with a purity of 98.66% and a yield of 67.32% was further obtained through a designed "antisolvent-cooling" crystallization process in a 3.2 L system. Moreover, the new process reduced ethanol usage compared to conventional processes, streamlined the purification process flow, and was more environmentally sustainable. Furthermore, we established an industrial-scale model for γ-aminobutyric acid production. Techno-economic analysis indicates that an investment in a plant with an annual capacity of 74.16 tons of γ-aminobutyric acid is projected to achieve payback in 1.98 years. In conclusion, the crystallization-based purification process is poised for industrial-scale γ-aminobutyric acid production due to its high efficiency, economic viability, energy conservation, and environmental compatibility.