NOVELTY - The reformer combination has a chamber (110) that is provided with an upper outer wall portion (101) and a lower base portion (103). An inner wall (3) is arranged within chamber. An upper portion of inner wall is connected to chamber for forming the inner and outer chambers. A thermal insulator is formed in outer chamber by producing partial vacuum during withdrawal of material from a top opening of inner chamber. A stirring element and cross elements (4) are separately arranged within the inner chamber.    USE - Reformer combination is used in electric arc gas-to-liquid process for producing oil (all claimed), synthetic gas for gas generator and fuel cell, and nitrogen-rich ash fertilizer.    ADVANTAGE - The leakage of gas from inner wall of chamber can be prevented effectively, since cross elements are welded to outside and inside of the inner wall in chamber. The production efficiency of oil, gas and ash can be improved, since stirrers are provided to maintain the feedstock and pyrolysis reaction products. The harmful substances can be removed efficiently from the environment. The ash fertilizer can be stored and transported economically. The manufacturing cost of reformer combination can be reduced, since size of reformer combination is reduced. The reforms basic organic elements found in waste material into high value partially refined petroleum. The operating cost of oil production facility can be reduced. The operating efficiency of oil production facility can be improved.    DETAILED DESCRIPTION - The reformer combination has an ash support element (8) that is arranged within chamber formed below opening of a lower reformer. An evacuation structure is coupled to the upper chamber for withdrawing the material from top opening of the inner chamber. The electrical insulation is formed between ash support element and lower reformer for causing an electric current to-be-induced from the inner wall to a top portion of wetted feedstock in the upper chamber. A gas/liquid separation structure is coupled to the evacuation structure for separating gas products from liquid products withdrawn from the top opening of the inner chamber. The water/oil separation structure is coupled to the gas/liquid separation structure for separating water products from oil products. The stirring element is provided with horizontally-arranged stirring arms rotated about a vertically-arranged axle by driving structure coupled to axle. The cross elements are horizontally arranged with the stirring arms. A burner apparatus (217) is arranged below the ash support element for heating the material within the inner chamber. A scrubber liquid input portion is arranged above upper chamber for supplying scrubber liquid to a top of the material in the upper chamber. A feedstock input portion is provided to supply feedstock material to the upper chamber. An airlock structure is coupled to feedstock input portion for restricting flow of air into upper chamber to maintain portion of the partial vacuum in the upper chamber. The ash evacuation structure is arranged below the ash support element for removing ash from the inner chamber. The ash evacuation structure is provided with an air opening port for permitting air flow upward through the inner chamber. A drive structure is coupled to a top of the reformer for rotating the stirring element within the inner chamber. INDEPENDENT CLAIMS are included for the following:    (1) a non-transitory computer-readable medium storing program for reformer combination, involves inputting feedstock into reaction chamber. The feedstock in reaction chamber is combusted. The electrical current flow is induced between the reaction chamber wall and the feedstock so as to cause arcing in the feedstock within the reaction chamber. The ash reaction byproducts are migrated downwardly to ash support structure which is electrically isolated from the reaction chamber wall. The gas and liquid reaction byproducts are migrated upwardly to the upper chamber. The gas/liquid products are excavated from the upper chamber. The oil and synthetic gas are separated from the evacuated gas/liquid products; and    (2) oil, which comprises 0.2-15 wt.% isoparaffin, 0.1-15 wt.% naphthene, 3-75 wt.% mono aromatics, 0-40 wt.% di-aromatics, 0-15 wt.% polyaromatics, 0.1-3 wt.% acid, 0-15 wt.% alcohol, 0.1-3 wt.% aldehyde, 0.1-7 wt.% amine, 0.1-3 wt.% ester, 0.1-7 wt.% indene, 0.1-7 wt.% ketone, 0.1-30 wt.% olefin, and 0.1-11 wt.% low-level organic compound.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the reformer apparatus.    Inner wall (3)    Cross element (4)    Ash support element (8)    Upper outer wall portion (101)    Lower base portion (103)    Chamber (110)    Burner apparatus (217)