NOVELTY - Sustainable integrated bio grind refining process (P1) for a feedstock of corn and corn stover, comprising: feeding 15-30% of the feedstock to a wet grind stream; feeding 15-18% of the feedstock to a dry grind stream; feeding 15-30 percent of the feedstock to a lignocellulose stream; and processing the feedstock to form germ, steep liquor, high protein soft starch, pre-liquefaction corn germ, post-distillation corn oil, and by-products of standard DPGS (sic), low oil DPGS, high protein DPGS, and batch feed lignin. The process operates as a batch or continuous process.    USE - The processes are useful: as a sustainable integrated bio grind refining process for a feedstock of corn and corn stover to produce fuel ethanol; for refining a feedstock comprising corn starch containing materials and plant bio-mass containing cellulose that can be converted with a process for food priority, animal feed, and fuel ethanol; and for producing ethanol from corn, cereal grain, adjuncts of cereal grain processing, corn stover, adjuncts of biomass material, starch containing tubers, or starch containing adjuncts of rejects or re-process materials (all claimed).    ADVANTAGE - The process: improves the quality of ethanol without any loss in the nutritional value of corn due to harsh temperature and chemicals; utilizes pervaporation process which significantly reduces the size of the distillation and evaporation steps due to reduced volume and steam for distillation; does not have any solids waste discharges; and is cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a process (P2) for refining a feedstock comprising corn starch containing materials and plant bio-mass containing cellulose that can be converted with a process for food priority, animal feed, and fuel ethanol, comprising: providing corn kernels having a moisture content of 10-30% and comprising a pericarp comprising coarse fiber, an endosperm comprising soft starch, hard starch, protein, and fiber; and a germ; screening the feedstock to remove 20-40% of the corn to remove small grain, broken grain, and elevator dust, and then diverting to a secondary process for conventional dry grind processing; steeping the corn kernels in recycled water from down stream processes, where the water has a temperature of 125-160 degrees F, is essentially free of sulfurous acid and comprises amylase enzymes in a counter-current steeping reactor system for 10-20 hours to produce an aqueous slurry of steeped corn kernels having a moisture content of 40-50%; washing the steeped corn and fractionate the steep liquor to be used as fermentation media, blending protein, and animal feed; coarsely grinding the steeped corn kernels to produce a coarsely ground stream comprising coarse fiber, soft starch, hard starch-protein-fine fiber fragments and germs; reducing the dry substance to 17-18% to hydrofloat fractionate the germ and any other starch product to be used for food and transferring the balance to a Supraton system for blending to 40-42 percent dextran sodium sulfate (DSS) for feedstock; blending the dry grind feedstock to drop the moisture to 15-18% moisture, and replacing the corn used for food in the bio/wet grind stream with the volume planned for the dry milling stream; cleaning the corn and adding the corn cleanings-off-all to the Supraton system for DSS blending; coarse grinding the cleaned dry grind food products required and sending the balance to the Supraton system for blending and controlling the feedstock to raise the typical dry grind fermented dry substance from 34-36 to 40-42 dry substance starch; subjecting the partially gelatinized stream to sufficient shear and cavitation forces in the presence of effective amounts of amylase enzymes to gelatinize substantially all the starch and to produce a liquefied stream at a viscosity typically of the dry grind 34-36 DSS level; exposing the liquefied stream to effective amounts of amylase enzymes to produce a saccharified stream reducing the viscosity for fractionating the remaining insoluble corn grain to produce a clean soluble stream to the fermenter; adding an amount of yeast to the saccharified stream and fermenting it to produce carbon dioxide and a fermented stream containing ethanol; scrubbing the carbon dioxide removed from the fermenter to recover retained ethanol; returning sufficient carbon dioxide for the agitation assist fine bubble system for anaerobic fermentation and head space blanketing; and finishing the refining of the ethanol in the distillation system; and (2) a sustainable process (P3) for producing ethanol from corn, cereal grain, adjuncts of cereal grain processing, corn stover, adjuncts of biomass material, starch containing tubers, or starch containing adjuncts of rejects or re-process materials, comprising: carrying out corn wet grinding with food fractionation with continuous steeping; carrying out corn dry grinding with cereal grin adjunct and counter flow bi-products and wash water blending; carrying out corn bio grinding with Langhauser Associates, Inc. (LAI) Supramyl high solids feed, high speed centrifugal colloid mill, combination fine grind/liquefaction with high shear and low viscosity discharge, where the discharge is separated for addition to the combined fermentation system and the animal feed refining system with the balance to feed the cellulose grind; cellulose grinding by utilizing available fiber, heat, water, catalyst, chemicals, enzyme and yeast recycles from the bio grind, adjunct from the dry grind and additional feedstock material containing cellulose, hemicellulose, lignin, and pectin; combined fermentation process comprising three continuous fermenters comprising the bio grind LAI continuous cascade fermenter process with carbon dioxide fine bubble supplemental mixing and blanketing for anaerobic yeast ethanol production, the invention of a one stage continuous pentose utilizing recycled catalyst and pervaporation filter fractionation of ethanol discharged to the primary fermenter for concentration, and the invention of a one stage fermenter for the discharge of the cellulose/dextrose hydrolysate process, where the evaporation and animal feed products are combined with the bio grind fermentation and animal feed processes; and washing the animal feed fraction in the fermenters, where the fiber, corn steep syrup and protein are blended with a priority to produce the corn value products with the best demand and price.