NOVELTY - Sourced processing method of village sewage without aeration, comprises pouring sewage into anaerobic producing methane reactor and recovering the produced methane; adding phosphorus removal flocculant into the effluent after being treated; adding treated effluent into ammonia nitrogen adsorption pool with addition of natural clinoptilolite; and then finishing the treatment of sewage.    USE - Sourced processing method of village sewage without aeration.    ADVANTAGE - The method resolves and removes the organic matter in the sewage and produces methane at the same time. The method is in small occupation area, small quantity of residual sludge with chemical oxygen demand removal rate of 75-90%, total nitrogen removal rate of 70-80% and total phosphorus removal rate of 71-88%. The discharged water can be used as life-using water or can be used for irrigation.    DETAILED DESCRIPTION - Sourced processing method of village sewage without aeration, comprises:    (A) pouring sewage into an anaerobic producing methane reactor through geogrid, where the sludge concentration of anaerobic particles in anaerobic producing methane reactor is 30-60 g volatile suspended solids (VSS)/L while the temperature inside is controlled at 15-30 degrees C and the hydraulic retention time is 6-12 hours; and recovering the produced methane;    (B) adding phosphorus removal flocculant into the effluent after being treated, where the effluent enters into micro-flocculation-filtering pool after passing through a tubular static mixer, the filter material in the micro-flocculation-filtering pool is homogeneous quartz sand with grain diameter of 0.8-1.5 mm, the thickness of filter material layer is 0.8-1.5 m, and the filtering speed is 6-10 m/hour;    (C) adding treated effluent into ammonia nitrogen adsorption pool with the addition of natural clinoptilolite having grain diameter of 0.5-1.0 mm, where the thickness of packing layer is 0.6-1.0 m, the filtering speed is 6-10 m/hour; and    (D) then finishing the treatment of sewage.    The phosphorus removal flocculant is polyaluminum chloride (PAC) or polyferric aluminum chloride (PFAC). The dosage of PAC is 5-10 mg/l with backwashing time of 20-30 hours while the dosage of PFAC is 5-10 mg/l with backwashing time of 30-50 hours.