NOVELTY - Producing (I) ethanol, corn oil and distillers dried grains with solubles (DDGS) from corn, comprises: (a) introducing corn to corn fractionation unit; (b) introducing obtained starch stream to saccharification unit; (c) introducing obtained glucose to aqueous fermentor; (d) introducing obtained dilute ethanol to distillation unit; (e) introducing obtained ethanol-rich overhead to ethanol drying unit; (f) introducing germ to an extraction unit; (g) drying solids in obtained solids-rich still bottoms to generate DDGS; and (h) recovering e.g. anhydrous ethanol.    USE - The process is useful for producing ethanol, corn oil, distillers dried grains with solubles, power (all claimed), steam, solvent extracted meal, carbon dioxide and co-products that are used in e.g. food, feed, fuel, and chemical/material applications, textiles, soaps and inks.    ADVANTAGE - The process: produces DDGS that has lower residual ethanol content compared to an otherwise-identical process without the vertically stacked counter-current dryer, and does not allows volatile organic compounds to escape (all claimed); does not requires regenerative thermal oxidizer; improves corn dry milling by avoiding hazardous hydrocarbon-based solvents and reducing energy usage and carbon footprint associated with the process; produces high-quality DDGS product with high protein content, low mycotoxin content and low fiber levels; reduces grams of carbon dioxide equivalent per mega joule of energy content for the production of ethanol, thus generating renewable-energy certificates or renewable identification numbers; enables distributed power production to reduce the electricity load on the current and stressed national-power grid, while avoiding the need to build new centralized less-energy-efficient power-generating capacity; reduces the amount of ethanol lost during drying of DDGS; produces more edible corn oil; and produces high protein solvent extracted meal that is utilized in monogastric animal feed diets (poultry and hogs).    DETAILED DESCRIPTION - Producing (I) ethanol, corn oil and distillers dried grains with solubles (DDGS) from corn, comprises: (a) introducing corn to a corn fractionation unit configured to separate the germ and the bran from the endosperm, to generate a starch stream containing up to 98% of the starch contained in the corn; (b) introducing at least a portion of the starch stream, in the form of an aqueous slurry, to a saccharification unit configured to hydrolyze the starch into glucose; (c) introducing at least a portion of the glucose to an aqueous fermentor containing a microorganism to ferment glucose into dilute ethanol and carbon dioxide; (d) introducing the dilute ethanol to a distillation unit configured to generate an ethanol-rich distillate (overhead) and a solids-rich still residue (still bottoms); (e) introducing the ethanol-rich overhead to an ethanol drying unit configured to generate anhydrous ethanol; (f) introducing at least a portion of the germ, or its conditioned form to an extraction unit configured to extract edible crude corn oil using a solvent; (g) drying the solids in the solids-rich still bottoms using a vertically stacked counter-current dryer to generate DDGS; and (h) recovering the anhydrous ethanol, the edible crude corn oil, and the DDGS. INDEPENDENT CLAIMS are also included for:    (1) producing (II) DDGS from still bottoms obtained from corn dry milling, comprising: (a1) providing or receiving the solids-rich still bottoms obtained from the distillation unit configured for purifying a fermentation product from fermentation of corn starch-derived glucose; (b1) optionally removing some liquid from the still bottoms, prior to drying; (c1) drying the still bottoms using a drying gas comprising air in the dryer, to generate a dried solids stream; (d1) cooling the dried solids stream using a cooling gas comprising air to generate a cooled solids stream comprising DDGS; and (e1) recovering the DDGS; and;    (2) producing (III) DDGS and power from still bottoms solids, comprising: (a2) providing or receiving still bottoms solids obtained from separation of a solids-rich still bottoms from the distillation unit; (b2) step (c1) as above pre se; (c2) optionally drying evaporated thin stillage using the drying gas in the dryer, to contribute to the dried solids stream; (d2) step (d1) as above per se; (e2) introducing non-condensable exhaust gases from the dryer to a gas turbine; (f2) introducing a first fuel to the gas turbine under effective combustion conditions in the presence of oxygen derived at least in part from the drying gas and/or cooling gas to generate power and heat; (g2) conveying hot exhaust gases from the gas turbine to a heat-recovery boiler for generating steam; (h2) optionally introducing a second fuel to the heat-recovery boiler; and (i2) recovering the DDGS and the power.