The invention relates to a 2,4-dinitraniline continuous ammonification production technology, which is characterized in that 2, ,4-dinitraniline and ammoniacal liquor are taken as raw materials, the raw materials are reacted at temperature of 160-170 DEG C and pressure of 0.5-1.0 MPa, and then continuously added in an ammonification reactor; when the raw materials exceeds a discharge hatch, and are successively flowed to two auxiliary reactors, wherein the reaction temperature is controlled at 160-170 DEG C, and the reaction pressure is controlled at 0.5-1.0 MPa, reaction time of an ammonification reactor is 42 minutes, and reaction time of each auxiliary reactor is 15 minutes. The production technology has the advantages of high production efficiency, low energy consumption, environmental protection, economy, low labor intensity and safety, waste heat during an ammonification reaction process can be fully used, by-product ammonium chloride can be simultaneously recovered, no waste water is generated, and the production technology has the advantages of green production and good economic benefit.