The present application provides an
aldehyde liquid phase hydrogenation reaction system, which is provided with a novel
liquid phase hydrogenation reactor. The reactor is provided with upper and lower column catalyst
bed layers, and the outer wall is provided with baffles; the
bed support structure and the redistributor are arranged between the upper and lower column catalyst
bed layers; the support porcelain ball and the
wire mesh layer are arranged below the lower column catalyst bed layer; the first fresh
hydrogen inlet is arranged at the top of the cylinder, and the
liquid phase inlet is arranged below the first fresh
hydrogen inlet; the second fresh
hydrogen inlet is arranged above the redistributor; the
boiler water inlet and the
water vapor mixed outlet are arranged in the upper and lower column catalyst bed
layers, respectively; the bottom of the cylinder is provided with a liquid phase outlet; the
gas phase outlet is arranged below the lower column catalyst bed layer; the fresh hydrogen is input through the first fresh hydrogen inlet and the second fresh hydrogen inlet; the
water vapor mixed outlet is connected with the
steam drum; the liquid phase outlet and the
gas phase outlet are connected with the separation tank, and the top of the separation tank is connected with the vent
gas cooler. The present application avoids the problem of temperature rising, produces high-grade steam as by-product, and saves energy and reduces consumption.