NOVELTY - The method comprises crushing kitchen waste to a diameter of less than 5 cm, mixing 0.01 wt.% of crushed kitchen waste with a fermented material, performing dry anaerobic treatment of the mixed material into a dry anaerobic fermentation reactor at a temperature of 33-35 degrees C by circulating water, controlling water flow rate using a flow control valve, performing hydrolysis acidification of fermented material using low molecular weight volatile fatty acids, filtering the fermented material from the dry anaerobic reactor through filter layers by circulating water, and leaching fermented material.    USE - The method is useful for dry anaerobic treatment of kitchen waste (claimed).    ADVANTAGE - The method ensures dry anaerobic treatment of kitchen waste with reduced energy consumption and without using stirrer.    DETAILED DESCRIPTION - The method comprises crushing kitchen waste to a diameter of less than 5 cm, mixing 0.01 wt.% of crushed kitchen waste with a fermented material, performing dry anaerobic treatment of the mixed material into a dry anaerobic fermentation reactor at a temperature of 33-35 degrees C by circulating water, controlling water flow rate using a flow control valve, performing hydrolysis acidification of fermented material using low molecular weight volatile fatty acids, filtering the fermented material from the dry anaerobic reactor through filter layers by circulating water, leaching the fermented material, where the content of effluent water of volatile fatty acids is 2-20 g/l, preferably 10 g/l, replacing the circulating water in the anaerobic treatment, supplying fermented feed gas produced during the hydrolysis acidification from a top of the dry anaerobic reactor to a gas-water separator, recycling separated gases, and performing dynamic aerobic composting at a temperature of 55-65 degrees C for 10-15 days. The ratio of circulating water and recycled water is 1:1. An INDEPENDENT CLAIM is included for a device for dry anaerobic treatment of kitchen waste.