This study is aimed at developing an anaerobic digestion system that can produce biogas for cooking purposes at the household level. A lab-scale batch digester was designed and constructed using polypropylene material with a capacity of 20 litres, and with the biogas captured in a floating-top gas reservoir. This initial small-scale construction was mainly to study some important parameters of the anaerobic fermentation process. The parameters studied were: biogas production from various types of organic material, the levels of acidity and dry matter of the organic material, the affect of temperature within the container, along with an evaluation of the time scale and rate of gas production. Four types of organic material were used, including fresh and dry cow dung with dry matter content of 20% and 90% respectively, dry chicken manure with dry matter content of 90%, and food waste with dry matter content of 10%. The test conducted with fresh cow dung was at a time of low ambient temperature in the Sudanese winter, while the tests for the other three feedstock materials were conducted in the higher ambient temperature of the Sudanese summer. The results from the lab scale revealed that the gas production rate was directly proportional to the reactor temperature, while the dry matter contents in the organic material dictated the required mixing ratio with water. Using results from the lab-scale reactor, the digester design was improved and scaled up using a cylindrical water tank with a capacity of 225 litres. Using feedstock of 84.3 kg of fresh cow dung with dry matter of 20% dilutd with water to 10% dry matter, the design was tested at a digestate temperature of 37-38 degrees Celsius. The test covered the calorific value of gas produced, gas consumption rate using a single burner, and the efficiency of the burner. The results were that the calorific value of the biogas was 20.52 MJ/m3, the burner had a gas consumption of 342 liters per hour during a simulation of normal operation for household cooking use, and use of a standardized process indicated a burner efficiency of 51.7%.