NOVELTY - Streptomycin bacteria slag processing device comprises a streptomycin bacteria dreg storage tank (1), an alkali liquid tank (2), a pre-reaction tank (3), a regulating tank (4), a straw fermentation tank (5), an anaerobic sequencing batch reactor (ASBR), a biogas collecting tank, a programmable logic controller (PLC) automatic control system, a computer, a first peristaltic pump, a second peristaltic pump, a third peristaltic pump, a fourth peristaltic pump four, a first online water quality monitoring system, a second online water quality monitoring system and a first electric stirrer.    USE - The device is useful for processing streptomycin bacteria slag (claimed).    ADVANTAGE - The device and method improves the utilization efficiency of organic matter streptomycin bacteria dreg, and thus simultaneously achieving the utilization of harmless streptomycin bacteria dreg and resources.    DETAILED DESCRIPTION - Streptomycin bacteria slag processing device comprises a streptomycin bacteria dreg storage tank (1), an alkali liquid tank (2), a pre-reaction tank (3), a regulating tank (4), a straw fermentation tank (5), an anaerobic sequencing batch reactor (ASBR), a biogas collecting tank, a programmable logic controller (PLC) automatic control system, a computer, a first peristaltic pump, a second peristaltic pump, a third peristaltic pump, a fourth peristaltic pump four, a first online water quality monitoring system, a second online water quality monitoring system, a third online water quality monitoring system, a first electric stirrer, a second electric stirrer, a third electric stirrer, an acid tank, an alkali tank, a first temperature probe, a second temperature probe, a first pH probe, a second pH probe, an oxidation-reduction potential (ORP) probe, a first heating rod, a second heating rod, an airbag, a timer, a first stirring paddle, a second stirring paddle, a third stirring paddle, an online water quality rapid detection system, a sludge discharge pump, a carbon source dosing pump, an acid dosing pump and an alkali adding pump. The streptomycin bacteria dreg storage tank is connected to the alkali liquid tank and left lower part of the pre-reaction tank through a first peristaltic pump and a second peristaltic pump, respectively. The lower part of the reaction pool is connected to the left lower part of the regulating tank by the third peristaltic pump. The lower part of the regulating pool is connected to the ASBR by a fourth peristaltic pump. The lower part of the ASBR is connected to the sludge discharging pump and the biogas collecting tank. The first peristaltic pump, the second peristaltic pump, the third peristaltic pump and the fourth peristaltic pump are connected to the sludge discharge pump and the timer. The pre-reaction tank, regulating tank and the ASBR are set with the first online water quality monitoring system, the second online water quality monitoring system and the third online water quality monitoring system. The first online water quality monitoring system is connected to one end of a first temperature probe, while the other end of the first temperature probe is set in the pre-reaction tank. The first online water quality monitoring system is connected to the computer. The second online water quality monitoring system is connected to the first pH probe. The other end of the first pH probe is connected to the inner side of the regulating tank. An INDEPENDENT CLAIM is also included for processing streptomycin bacteria slag using the device, comprising (i) injecting streptomycin bacteria slag into the streptomycin bacteria dreg storage tank and pre-reaction tank by the second peristaltic pump, feeding into ASBR at a rate of 4.5-5 vol.%, then alkali liquid into the alkali liquid tank of the pre-reaction tank, adding alkali sodium hydroxide into the streptomycin bacteria slag in a mass ratio of 0.08-0.10; (ii) preprocessing by regulating the temperature and the stirring time in the pre-reaction tank by using PLC automatic control system, and heating, and mixing based on the start control signals obtained from the temperature detection value of the first online water quality monitoring system using the PLC automatic control system, and heating the first heating rod, once the reaction temperature in the reaction pool is less than 75 degrees C, setting the mixing time to 2.5 hours, once the heating temperature reached 75 degrees C, and then maintaining the temperature constant; (iii) stirring the resulting mixture injected into the regulating tank by the third peristaltic pump, detecting ammonia nitrogen and chemical oxygen demand (COD) concentration in the regulating tank by using online water quality fast detection system, and then producing signal feedback from the PLC automatic control system, and simultaneously injecting supernatant into the regulating tank from the straw fermenting tank, starting the second electric stirrer to drive the second stirring paddle to stir, and stopping the injection process once the carbon/nitrogen ratio in the regulating tank reaches to 20:1-25:1; (iv) carrying out real-time detection of the pH values of the regulating tank and second online water quality monitoring system by using the first pH probe, and controlling the opening and closing operation of the acid pump and alkali pump online by using the PLC automatic control system, where the pH of the regulating tank inner side is 7-7.2; (v) regulating the water quality in the mixture injected into the ASBR by using the fourth peristaltic pump in a volume set load of not less than 2.5 gVSS/l.d, and setting the reaction temperature to 40 degrees C, increasing the anaerobic reaction stirring time once the oxidation-reduction potential ORP value is higher than the setting range is 70-100 mV, increasing hydraulic retention time (HRT), and conversely reducing HRT, and carrying out anaerobic reaction under continuous stirring mode, collecting the marsh gas obtained in the ASBR into the airbag, and burning the clean fuel; and (vii) feeding the streptomycin bacteria slag mixture into the biogas residue collecting tank by the sludge discharge pump, and controlling the running time of the sludge discharge pump by using the timer, and recycling the biogas residue which can be utilized as an organic fertilizer raw material resource, where the residence time of streptomycin bacteria slag in the ASBR, is 20-25 days, and controlling the running time of the sludge discharge pump by using the timer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the streptomycin bacteria slag processing device (Drawing includes non-English language text).    Streptomycin bacteria dreg storage tank (1)    Alkali liquid tank (2)    Pre-reaction tank (3)    Regulating tank (4)    Straw fermentation tank (5)