NOVELTY - The method comprises grinding (a) lithium battery electrodes and lithium batteries, dissolving (b) organic components and/or polymers of the electrodes and/or batteries in an organic solvent to obtain a suspension, separating (c) undissolved metals in the suspension, filtering (d) the suspension through a filter press to obtain a solid mass, recovering (e) the solid mass retained on the filter press, suspending the solid mass in water, recovering sedimented or coagulated material, resuspending the sedimented material in water and then adjusting the pH of the resulting suspension.    USE - The method is useful for recycling lithium battery electrodes and/or lithium batteries, which are useful for hybrid vehicles, electric vehicles, electric appliances and buses, trucks, bicycles and electric scooters.    ADVANTAGE - The method allows economic and high rate recycling of lithium battery electrodes and/or lithium batteries without emission of toxic gases to the environment.    DETAILED DESCRIPTION - The method comprises grinding (a) lithium battery electrodes and lithium batteries, dissolving (b) organic components and/or polymers of the electrodes and/or batteries in an organic solvent to obtain a suspension, separating (c) undissolved metals in the suspension, filtering (d) the suspension through a filter press to obtain a solid mass, recovering (e) the solid mass retained on the filter press, suspending the solid mass in water, recovering sedimented or coagulated material, resuspending the sedimented material in water and then adjusting the pH of the resulting suspension at a pH of less than 3-4, filtering the suspension on the filter press to obtain a filtrate, separating a part of the iron from the electrodes and/or batteries by precipitation of iron phosphate and a part of lithium from the electrodes and/or batteries by precipitation of a lithium salt. The step of separating the iron and lithium from the electrodes and batteries comprises recovering the filtrate and precipitating a lithium salt, recovering the solid fraction retained on the filter press, adjusting the pH to 2-3 at room temperature, where ferric ion (Fe2+ and Fe3+) and phosphate ion pass in solution and titanium, filtering the suspension, recovering solid titanium on the filter, precipitating iron phosphate contained in the filtrate, recovering titanium solid retained on the filtrate, recovering the filtrate, separating iron phosphate by filtration of filtrate, and recovering the filtrate and precipitating lithium salt. The step of precipitating iron phosphate comprises: adjusting pH of the recovered filtrate to 5, filtrating the suspension, recovering the precipitate, washing the precipitate with water and drying the precipitate at a temperature of less than or equal to 30 degrees C; adding 1-30 vol.% of hydrogen peroxide with respect to the total volume of the recovered filtrate; and adjusting the pH of the solution to 5, recovering the formed precipitate, washing the precipitate and drying at a temperature of 50 degrees C. The iron phosphate is calcined at a temperature of 500 degrees C in air to obtain crystalline iron phosphate. The step of precipitating the lithium salt comprises: mixing the filtrate with an aqueous solution with a pH of greater than 12 and containing a quantity of phosphate ions that is one third of the quantity of lithium ion, heating the mixture at a temperature of 50 degrees C to form precipitate and washing the precipitate with water to obtain lithium phosphate; mixing the filtrate with an aqueous solution with a pH of greater than 12 and containing a quantity of carbonate ions that is equal to the quantity of lithium ion, heating the mixture at a temperature of 90-100 degrees C and then filtering the suspension at a temperature of 100 degrees C to obtain a dry extract of lithium carbonate; and passing the filtrate on a cationic ion exchange resin at a mole ratio of lithium ions present in 10-6 to 10-2 solution/g of resin, contacting the resin with an acid solution having a pH of less than 3 at a volume ratio of liquid/resin of less than 1 and recovering the lithium carbonate by filtration the suspension at a temperature of 100 degrees C. The process further comprises: purifying the solvent contained in the filtrate by centrifugation to obtain a colorless liquid; performing evaporation-condensation of colorless liquid at a temperature of 60-80 degrees C; optionally recovering the solvent; extracting carbonaceous materials of the suspension by flotation; washing the materials with acidic aqueous solution having a pH of less than 3; filtering the carbonaceous materials; and separating trimetals from the electrodes and batteries.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for recycling lithium battery electrodes and/or lithium batteries (Drawing includes non-English language text).    Grinding lithium battery electrodes and lithium batteries (a)    Dissolving organic components and/or polymers of the electrodes and/or batteries in an organic solvent to obtain a suspension (b)    Separating undissolved metals in the suspension (c)    Filtering the suspension through a filter press to obtain a solid mass (d)    Recovering the solid mass retained on the filter press and suspending the solid mass in water. (e)