The application discloses a parallel type bidirectional liquid feeding
reaction system for producing butyl
octanol, which comprises a reaction kettle supported and placed by an external support, bidirectional liquid feeding pipes, a gas inlet
pipe, a premixing cavity, an emulsification mechanism, a catalyst adding mechanism and a buffer mechanism. Liquid propylene enters the premixing cavity through the liquid feeding
pipe, is premixed with CO gas discharged from the gas inlet
pipe, is refined into micron-level gas-liquid emulsions through the emulsification mechanism, the gas-liquid contact area is significantly increased, the reaction efficiency is improved, the catalyst is accurately metered through a
storage tank and an auxiliary mechanism, the reaction stability is ensured, the buffer mechanism in the liquid feeding pipe effectively slows down the liquid
impact force and filters impurities, the cleaning mechanism can scrape and clean the impurities on the surface of the filter plate, the filtering effect is ensured, the liquid propylene and the CO gas are efficiently premixed through optimization of the
feeding mode and the mixing structure, and the reaction efficiency of butyl
octanol production and the consistency of product quality are significantly improved.