The invention relates to the technical field of chemical production, in particular to a crude benzene hydrofining process, which comprises the following steps: pretreating crude benzene, performing pressurizing by a pump, exchanging heat by a heat exchanger, and pumping the product into a hydrogen mixing tank; fully mixing a crude benzene full-fraction raw material, hydrogen and part of a recycledhydrogenation product in the hydrogen mixing tank, and fully dissolving the hydrogen in the raw material; sending a gas-liquid mixture discharged from the hydrogen mixing tank into a heating furnaceto be heated to 330-340DEG C, and then sending the product into an excessive hydrogen separation tank, and enabling the excessive hydrogen separated from the top of the excessive hydrogen separation tank to enter a tail gas treatment system; feeding the full-liquid-phase crude benzene raw material rich in dissolved hydrogen from the bottom of the excess hydrogen separation tank into a first-stagehydrogenation reactor, and carrying out a full-liquid-phase hydrogenation reaction under the catalytic action of a hydrogenation catalyst under the conditions of a pressure of 6-6.5MPa and a temperature of 340-345DEG C; flowing back one part of a hydrogenation product from the hydrogenation reactor to the hydrogen mixing tank, keeping the reflux quantity at 80% of the hydrogenation product, and subjecting the rest part to heat exchange with the raw material crude benzene, and then letting the rest part enter the gas-liquid separation tank. Therefore, the energy consumption is low, and the benefit is greatly improved.