NOVELTY - A household refuge, livestock waste and biomass waste are primarily separated in factory. The organic material as raw material is crushed to obtain raw material, and transported to organic material storage silo. The raw material is magnetically separated by second class automation magnetic separation device to remove ferromagnetic material, and is transported to an oxidative reactor via a feeding machine. The raw material particles with grain diameter of 8 mm or less are crushed to obtain intermediate product which is used to produce organic complex fertilizer.    USE - Treatment of household refuge and livestock waste used for producing organic complex fertilizer (claimed).    ADVANTAGE - The method enables efficient treatment of household refuge and livestock waste, without waste discharge.    DETAILED DESCRIPTION - A household refuge, livestock waste and biomass waste are primarily separated in factory. The waste is divided into organic material, inorganic material, light plastic, inflammable material and ferromagnetic material by crushing, machine screening, gravity selection, wind selection, magnetic selection and grain diameter selection of waste. The organic material as raw material is crushed to obtain raw material having grain diameter of 8-68 mm, and transported to organic material storage silo. The raw material is magnetically separated by second class automation magnetic separation device to remove ferromagnetic material, and is transported to an oxidative reactor via a feeding machine. The oxygen-enriched air with oxygen content of 25-35% which is pre-heated to 50-60 degrees C, is charged to the oxidative reactor, and phosphorus oxide with concentration of 5-10 wt.% is added to oxidative reactor, such that the mass ratio of raw material and phosphorus oxide is 100:3-5. When volume of raw material is 75-80% of oxidative reactor capacity, the charging of material is stopped. When pressure in reactor is 0.1-0.2 MPa, the charging of oxygen-enriched air is stopped, and temperature is increased from room temperature to 145 degrees C within 5 minutes. The pressure of oxidative reactor is controlled to 0.2-0.6 MPa, and temperature and pressure of oxidative reactor are maintained for 10-15 minutes, and the starchy material is degraded. After 5 minutes, the temperature of oxidative reactor is increased to 145-205 degrees C, and pressure of oxidative reactor is controlled to 0.6-1 MPa, and temperature and pressure of oxidative reactor are maintained for 10-15 minutes, and sugar, crude fiber and protein are degraded. The temperature of oxidative reactor is increased to 205-230 degrees C, and pressure is controlled to 1-1.25 MPa, and temperature and pressure of oxidative reactor are maintained for 10-15 minutes, and fat fur is degraded. After degradation reaction is completed, pressure of oxidative reactor is decompressed to 0.3-0.4 MPa, and steam in oxidative reactor is discharged. The hot air at 80-100 degrees C is charged to stove the raw material for 30-50 minutes. The moisture content of raw material in oxidative reactor is reduced to 30% or less. The raw material in reactor puffs to puff storehouse, and hydrolyzed. The hydrolyzed product is neutralized, such that pH is adjusted to 6-7.5. The raw material particles with grain diameter of 8 mm or less are crushed to obtain intermediate product. The intermediate product is transported to obtain organic complex fertilizer.