TECHNOLOGY FOCUS - COMPUTING AND CONTROL - Preferred Process: In the process, The ethanol and methane are collected from the fermentation. The process further involves distilling the solution to separate the ethanol from the carbon dioxide and water contaminants; collecting the separated carbon dioxide and ethanol in separate storage containers; reintroducing the water to the anerobic digester; drying and compressing the methane prior to storage; applying a positive suction to the anerobic digester to collect the methane; collecting all solid organic material from the anerobic digester; drying and granulating the solid organic material to form fertilizer; desalinating any waste water produced from the process prior to release. Preferred System: In the system, the outlet is a fluid outlet for collecting ethanol from the anerobic digester, where fluid outlet is in further fluid communication with a distillation column for purifying ethanol from any contaminants. The ethanol is in solution with carbon dioxide and water contaminants. The distillation unit is in fluid communication with at least two storage tanks for collecting purified ethanol and carbon dioxide. The distillation unit further comprises a fluid return for reintroducing water into anerobic digester. The distillation unit provides a source of ethanol that is at least 90% pure. The anerobic digester further comprises at least one gas outlet for collecting methane from the anerobic digester. The gas outlet is in fluid communication with a storage tank for collecting the methane. The dryer and a compressor are in fluid communication between the gas outlet and the storage tank for drying and pressurizing the methane prior to storage. The gas outlet further comprises a vacuum pump for applying positive suction to the anerobic digester. The anerobic digester further comprises a solid material outlet for collecting solid organic material from anerobic digester. The system further comprises a rotary kiln for drying and granulating solid organic material; a desalinization unit in fluid communication with anerobic digester for treating any waste water produced there prior to release. The heater is designed to heat anerobic digester at 85-130 degrees F. Preferred Components: The weak acid is a solution of sulfuric acid (3%). The neutralizer is a buffering agent capable of increasing the pH of the pretreated material to around 7. The starter sugar is in a solution concentration of 0.1%. The microorganism is Saccharomyces cerevisiae. ACTIVITY - Fertilizer. No biological data given.    MECHANISM OF ACTION - None given.    EXAMPLE - No suitable example given.