NOVELTY - A seed sludge is added to the internal circulation anaerobic tank, and desizing wastewater is discharged into the internal circulation anaerobic tank. An industrial glucose is added into internal circulation anaerobic tank, sludge hydrolysis acidification bacteria is inoculated, desizing wastewater methane bacteria and 70-85% soluble contaminants are hydrolyzed and methanation reaction is performed, to obtain methane and carbon dioxide. The continuously stirred tank reactor anaerobic digestion pool is discharged to filter press dehydration.    USE - Method for treating high-concentration printing-dyeing desizing waste water and aerobic (claimed).    ADVANTAGE - The method efficiently and economically treats high-concentration printing-dyeing desizing waste water and aerobic with improved removal rate of chemical oxygen demand in the printing-dyeing desizing wastewater, and high decrement treatment efficiency of residue sludge.    DETAILED DESCRIPTION - A seed sludge is added to the internal circulation anaerobic tank, and desizing wastewater is discharged into the internal circulation anaerobic tank. An industrial glucose is added into internal circulation anaerobic tank, sludge hydrolysis acidification bacteria is inoculated, desizing wastewater methane bacteria and 70-85% soluble contaminants are hydrolyzed and methanation reaction is performed, to obtain methane and carbon dioxide. The desizing wastewater as raw water is printed and dyed, and primary deposited to remove suspended impurities into aerobic pool. An aerobic nitrification tank reflux liquid is reflowed to the anoxic pool. The internal circulation anaerobic tank are discharged intermittently with water outlet of aerobic tank reflowing nitrifying liquid, and the clear liquid is provided in the anoxic tank into aerobic pool. The supernatant liquid of remainder sludge is provided in the anaerobic tank continuously stirred tank reactor anaerobic digestion tank. The continuously stirred tank reactor anaerobic digestion pool of residual sludge is discharged to the intermittent hypoxia pool, and continuously stirred tank reactor anaerobic digestion pool is discharged to filter press dehydration. The water chemical oxygen demand of aerobic pool is less than 500 mg/l.