NOVELTY - Cultivating and harvesting legumes harvested fresh, whole with stems, e.g. for storage of silage in bales, in silos, as loaf on ground, comprises: rolling, folding, laying or otherwise placing material on conveyor; refining various materials in various ways; filtering and purifying protein, hydrolyzing starch into sugars and fermenting and distilling it; and drying fibers.    USE - The method is useful for cultivating and harvesting the legumes harvested fresh, whole with stems, for the storage of silage in bales, in silos, as loaf on the ground or similar for processing and ennobling of protein for animal feed and meat substitute for human consumption, glucose and ethanol, and long fibers into fuel pellets and briquettes, or to the industry as the content in board.    ADVANTAGE - The method: stores the crop and shortens the time in the field to secure the harvest-yield; and provides nitrogen that fixed by the pod-crop and carbon that left in the soil as humus which decreases the level of carbon dioxide in the atmosphere.    DETAILED DESCRIPTION - Cultivating and harvesting legumes harvested fresh, whole with stems, for the storage of silage in bales, in silos, as loaf on the ground or similar for processing and ennobling of protein for animal feed and meat substitute for human consumption, glucose and ethanol, and long fibers into fuel pellets and briquettes, or to the industry as the content in board, comprises: rolling, folding, laying or otherwise placing the material on a conveyor as in figure 1 of the specification to separate stems from the seeds and pods, stems spread using threaded rollers, and then using a mangle press out the proteinaceous liquid the material; refining the various materials in various ways; filtering and purifying the protein, hydrolyzing the starch into sugars and fermenting and distilling further, if necessary, to ethanol; and drying the fibers to become raw material for board skivor fuel pellets or briquettes. An INDEPENDENT CLAIM is also included for an apparatus for processing the ensiled material, which rolls out a bale of ensiled legumes or leguminous crops ensiled by another storage form, using a conveyor belt that is described as in figure 1 of the specification with a number of rollers that clean fibers from other materials by scratching the seeds and pods which fall into a trough, a repo in the form of a rotating pipe with strong pegs standing in rows out of a tube, and the tube that rotates at a speed higher than the conveyor so that the crop spread lengthwise, where: the stems lands on the next conveyor belt which has a higher speed than the first conveyor belt, and one fiber is separated from another through pairs of radially corrugated rolls, in which grooves are in form of thread that rotate in opposite directions so that unrolled fibers distributed uniformly over the substrate; with a preferably soft and a hard roll perforated mechanically separate the liquid present in the crop, with two against each other angled rollers get fiber to roll back and forth on a hard surface heated and thus purged completely from the fiber-free materials (proteins and starch), this material is collected in a trough and is screwed on to a grinder, and the fibers are not cut but preferably collected in length coiled on a spool, or rolled or folded as mat; from trough screwed material between two soft rolls peeling bean which has come off by ensiling and on to a mill to grind the seeds into powder, after milling, the powder is mixed with a sugar solution with a specific gravity of between (protein) 1.05 kg/l and (starch) 1.35 kg/l which is used to distinguish them in a tank so that the protein floats up and starch will sink to the bottom, the tank is equipped with a screw in the bottom for the transport of the starch and a sieve gauze with a screw top for transport and dewatering of protein, the screw presses since protein by a cone of the filter cloth for optimum dewatering, and part of this can be seen as in figure 6 of the specification; the sedimented starch is mixed with part of the sugar solution and diluted with water and purified dregs to the appropriate concentration and fed into a trapezoidal screw as in figure 2 of the specification, which function as heat exchanger, within the screw in a tube with a preferably good conductor has a hot liquid to be cooled and the screw, as described feeding a cold liquid to be heated which also holds both the inner and the outer tube clear of protein and starch accumulation and can transport liquids of different density and fluidity, and the screw is formed with inclined guide rails which causes the liquid to move between the inner and outer tubes for optimum heat transfer; the screw is driven by a simple angle gear, this heat exchanger can be bent and further directed to a device using heating and expansion of a liquid using an inclined steel can skim proteins from a material, and this protein is then removed using a conveyor belt with carriers and then with a screw from the process; the remaining liquid is pumped into a ferment-tower as in figure 4 of the specification including a helical path that keeps track of the fluid being pumped in from the bottom of the screw heat exchanger and is sucked up from the top of the distillation, and this is also equipped with an inner water-filled tube with valves against which the web is inclined upwards so that the carbonic acid formed may be evacuated from the process by the overpressure produced by fermentation; the web is also if necessary a trapezoidal screw which drives the liquid forward and mixes the active, when the liquid reaches the top of the alcohol formed being sucked into a distiller, in which the fermented liquid after preheating from the previous step in the process is poured over a stepped medium of figure 5 of the specification of hot liquid filled element with good conductivity and subjected to pressure by a piston in a cylinder in parallel with a similar piston cylinder application and as may the cylinder volume to increase with pressure drop as a result causing the liquid boiling point to fall and vaporates, as the piston turns the valve through which the alcohol gas is sucked into the pump and another valve opens outside which a nozzle is disposed and is pressed against the nozzle alcohol gas in which the heat emitted and collected by a heat exchanger and is removed from the cylinder and this means that the gas is cooled and condensed at the rear of the nozzle, and simultaneously opposite sequence in the second cylinder; and the heat produced by the compression of the gas is used as additional energy in the reactor process, in order to drive the process that is self-sufficient in energy, a generator driven by an internal combustion engine, the fuel for the internal combustion engine is so called gas produced by pyrolysis of the fiber materials produced in ecoreactor, and as a supplement to the heat, the ecoreactor need used engine cooling water.