NOVELTY - The device comprises a reactor with an organic material inlet and a flue gas inlet adapted to introduce flue gas into the reactor, an input driver (80) adapted to continuously transfer the solid organic material to the organic material inlet, an output driver adapted to continuously transfers the solid organic material out of the reactor, a gas flow element operatively connected to the flue gas inlet permitting flue gas to mix with the solid organic material and to restrict flow of the solid organic material away from the flue gas inlet, and a rapid cooling device.    USE - The device is useful for upgrading a solid organic material into a resulting product (claimed), where the solid organic material such as peat, biomass, garbage and low rank coals is useful as fuel and a source of energy and for high volume applications.    ADVANTAGE - The device economically and rapidly reduces the amount of water content and increases the calorific value of the organic material.    DETAILED DESCRIPTION - The device comprises a reactor with an organic material inlet and a flue gas inlet adapted to introduce flue gas into the reactor, an input driver (80) adapted to continuously transfer the solid organic material to the organic material inlet, an output driver adapted to continuously transfers the solid organic material out of the reactor, a gas flow element operatively connected to the flue gas inlet permitting flue gas to mix with the solid organic material and to restrict flow of the solid organic material away from the flue gas inlet, and a rapid cooling device operatively connected to the output driver and adapted to apply a heat transfer liquid directly onto the solid organic material and to form a resulting product. The reactor defines a dryer that contains the gas flow element, a first setter operatively connected to the dryer and adapted to receive both solid organic material from the dryer and flue gas, and a second setter operatively connected to the dryer and adapted to receive both solid organic material from the dryer and flue gas. The first setter and the second setter are connected to the dryer in series. The device further comprises a pair of flue gas generators operatively connected to the second setter, a flue gas generator (40) operatively connected to the first setter, t-air flows, a cyclone adapted to receive flue gas in a flue gas outlet extending from the reactor, a scrubber adapted to receive flue gas from the flue gas outlet, and a controller operatively connected to the input driver, the output driver, and the flue gas generator. The first and second setters have flue gas outlets that are operatively connected to the flue gas inlet of the dryer. The flue gas outlet of each dryer and each setter is located above a corresponding solid organic material outlet of each dryer and each setter. The dryer further comprises a reactor wall and a hopper positioned with the dryer. A hopper wall is separated from the reactor wall by a gap. The t-air flows extend through the hopper wall to the gap in one direction and in another direction through the hopper wall to the gap. The hopper forms a constriction beneath the t-air flows. The constriction is formed above the output driver at a solid organic material outlet of the dryer. The flue gas has a temperature at the flue gas inlet of greater than of 600 degrees C. The cyclone is adapted to remove fine particles of the solid organic material present in the flue gas. The controller controls flow of the solid organic material and the flue gas into the reactor. An INDEPENDENT CLAIM is included for a method for upgrading a solid organic material into a resulting product.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for upgrading solid organic materials.    First reactor (30)    Second reactors (35)    Flue gas generator (40)    Conveyor belts (70)    Input driver. (80)