The invention discloses a
creatine phosphate sodium continuous flow synthesis process, which comprises the following steps: adding a proper amount of
dichloromethane and a proper amount of
creatinine into a
storage tank A, and stirring until the solution is clear to obtain a
storage tank A material; adding a proper amount of
phosphorus oxychloride into a
storage tank B to obtain a storage tank B material; conveying the materials in the storage tank A and the storage tank B into a micro-channel reactor, reacting to obtain a dichlorophosphoric acid
creatinine reaction solution, then concentrating in a concentration kettle, adding methylbenzene, stirring, crystallizing, and filtering to remove
residual phosphorus oxychloride; adding a proper amount of
purified water and
sodium hydroxide into a tank D, stirring until the solution is clear to obtain a storage tank D material, adding the materials in the tank C and the tank D into a micro-channel reactor, reacting to obtain a
creatine phosphate sodium solution, transferring the solution into an extraction layering kettle, standing and layering to obtain an upper
water layer, and filtering the upper
water layer to obtain the
creatine phosphate sodium. And adding activated cationic resin, stirring, filtering by using a
microfiltration membrane when the pH value of the feed liquid is reduced to 9-10, and crystallizing by adding 95%
ethanol into the filtrate to obtain the creatine phosphate sodium finished product. Through a
continuous flow synthesis process, the use and residue of
phosphorus oxychloride are reduced, and the product safety is improved; reaction impurities and phosphate residues are reduced, the reaction efficiency is improved, and the cost is reduced.