The invention belongs to the technical field of
food additive preparation, and particularly relates to an
acesulfame potassium hydrolysis process and application. The process adopts a secondary
hydrolysis process, and comprises the following steps: introducing sulfonation liquid in a front section and washing
acid water (2-4%) in a rear section into a first
hydrolysis reactor, and accurately controlling the
specific gravity of hydrolysis acid and temperature parameters (for example, the
specific gravity is 1.2-1.3, and the temperature is-5 DEG C to 15 DEG C); materials in the middle of the first hydrolysis reactor continuously overflow into a second hydrolysis reactor (hydrolysis transfer kettle) containing a stirring pump and an external circulation pump, the reaction time is prolonged,
mass transfer is enhanced through external circulation, and the material
retention time is prolonged; and feeding the material in the second hydrolysis reactor into a hydrolysis layering tank, standing, separating an upper-layer acid phase, washing a lower-layer organic phase with water, and finally neutralizing with
potassium hydroxide to obtain an
acesulfame potassium crude product
sugar water solution. The reaction sufficiency is improved through secondary hydrolysis, the temperature is stabilized, the ice maker load and the labor intensity are reduced, the process adaptability is enhanced, and the
acesulfame potassium production stability and yield are effectively improved.