TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The wetting agent comprises expansive clay, metal compound, expandable or softened fiber compound, fatty acid lipid and/or nonionic surface active agent, preferably bentonite, aluminum sulfate, sodium carbonate, diglycol and/or nonionic surface active agent. The oxidant comprises ozone, chlorine, hypochlorite, potassium permanganate, peroxide, oxygen and/or preferably air. The softening agent comprises aluminum sulfate added with nonionic paraffin, quat. ammonium compound added with fatty acid lipid, dialdehyde added with glycols and mixture of phospholipids, nonionic surface active agent and plant oil, and optionally added with antioxidant, hydrophilizing agent including sodium sulfite, potassium sulfite, magnesium sulfite and ammonia sulfite, and inorganic soft agent including magnesium chloride, sodium carbonate, potassium carbonate, sodium bicarbonate, ammonium carbonate, magnesium carbonate and/or ammonium bicarbonate, preferably mixture of phospholipids, nonionic surface active agent and plant oil, potassium sulfite and/or ammonium bicarbonate. The activating agent comprises bentonite, kaolin, vermiculite, nacrite, zeolite, activated carbon, lignite and peat, preferably bentonite and/or lignite.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: The step (A) further comprises selecting and purifying selected organic waste or organic waste containing little inorganic materials. The step (B) comprises cutting or milling organic waste into 0.05-5 cm granules, completely purifying and treating lignocellulose to release cellulose. The step (C) comprises feeding organic waste into physicochemical pretreatment tank, adding water until material is saturated, adding materials comprising (wt.% with respect to total volume of saturated material) water (10-20), wetting agent (0.5-5) and dissociating agent (0.5-5) to decompose cellulose in solid waste, uniformly stirring and directly or indirectly heating using steam. The step (D) comprises maintaining material in liquid or solid state at 140-300 (preferably 180-230) degrees C and 7-77 atm, adding oxidant with dissolved oxygen equivalent weight of 1-6 (preferably 2-4) ppm and 0.5-10 (preferably 0.5-5)% heavy metal remover, oxidizing for 5-30 (preferably 10-20) minutes under 13-31 atm, reducing 3-4 atm pressure, introducing hot steam, filtering, feeding filtered material into high speed active reaction kettle and feeding filtered water into physicochemical pretreatment tank and recovering. The step (E) comprises adding 0.5-15 (preferably 1-5)% softening agent and 1-50 (preferably 5-10)% activating agent into material, reacting at 140-300 (preferably 180-230) degrees C for 5-30 (preferably 10-15) minutes under steam pressure of 3-74 (preferably 10-28) atm, opening decompression valve to enable the steam to explode into decompression tank, respectively introducing decompressed steam into physicochemical pretreatment tank, high speed stable reaction kettle and refinement furnace, and introducing material into product refining furnace. The step (F) comprises regulating humidity of material at 25-35%, milling into 200 meshes to 15 mm, and adding composite fertilizer containing nitrogen, phosphorus and potassium. The wetting agent and dissociating agent can be added into solid material having dry cellulose in mechanical pre-processor before grinding or feeding material having fiber slurry in physicochemical pretreatment tank after adding water. The softening agent is added with antioxidant and/or hydrophilizing agent or inorganic softening agent. The extractant is added into material, and the solid heavy metal is dissolved or changed into metallic compound having lowest solubility. Preferred Components: The solid waste having organic material comprises municipal refuse, agricultural wastes, green wastes, slurry in sewage treatment works, animal wastes, organic waste products, organic wastes slurry of oil refinery and factory of food, paper and medicine, and organic wastes of many hospitals. The dissociating agent is mixture of phospholipids, nonionic surface active agent and plant oil or quat. ammonium compound of formula (I), preferably mixture of phospholipids, nonionic surface active agent and plant oil. The heavy metal extractant comprises ammonium acetate, calcium nitrite, magnesium chloride, mixture of ammonium acetate and ammonium hydroxide with pH of 9, 2% citric acid, 0.2 M ammonium oxalate, EDTA, 1 N ammonium acetate plus 0.2% hydroquinone, 0.04-1 M hydroxyammonium chloride plus 25% acetic acid, sodium hydrosulfite-sodium citrate, diluted acids, strong acids, mixed solution of strong acid, and/or mixture of nitrous acid, hydrogen fluoride and perchloric acid.R1, R2=12-40C hydrocarbon;R3, R4=Me, Et or hydroxyethyl;A=oxyalkylene group;m=valence number;n1, n2=6-30;andX=negative ion.