Process for making a powder or granule containing at least one chelating agent selected from alkali metal salts of methyl glycine diacetic acid (MGDA) and glutamic acid diacetate (GLDA) and iminodisuccinic acid, wherein said alkali metal salts are selected from compounds according general formuIa (Ia), (Ib) and (Ic) [CH 3 -CH -N(CH 2 -COO) 2]M 3-x H x (Ia) wherein M is selected from alkali metal cations, same or different, and x is from zero to 1.0, [OOC-CH 2 CH 2 C-CH -N(CH 2 -COO) 2]M 4-x Hx (Ib) wherein M is selected from alkali metal cations, same or different, and x is from zero to 2.0, [H-N-(CH -CH 2 COO) 2]M 4-x H x (Ic) wherein M is selected from alkali metal cations, same or different, and x is from zero to 2.0, said process comprising the steps of (a) introducing an aqueous solution or aqueous slurry of the respective chelating agent into a spray-dryer or spray-granulator, and removing most of said water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250°C, (b) withdrawing powder or granules, respectively, from the spray-dryer or spray-granulator, respectively, (c) separating off fines from said powder or granules, wherein said fines have a maximum particle diameter of 30 μm in the case of powders and a maximum particle diameter of 350 μm in the case of granules, (d) separating off lumps from said powder or granules, wherein said lumps have a particle diameter of 250 μm or more in the case of powders and 1,000 μm or more in the case of granules, respectively, (e) milling said lumps to a maximum particle diameter of 500 μm in the case of granules or to 40 μm in the case of powders, respectively, (f) re-introducing said fines from step (c) and milled lumps from step (e) into the spray-dryer or spray-granulator, wherein the share of fines is in the range of from 4 to 18 % by weight of the total chelating agent withdrawn in step (b) and the share of milled lumps from step (e) is in the range of from 20 to 40% by weight of the total chelating agent withdrawn in step (b). at least one chelating agent selected from alkali metal salts of methyl glycine diacetic acid (MGDA) and glutamic acid diacetate (GLDA) and iminodisuccinic acid, wherein said alkali metal salts are selected from compounds according general formuIa (Ia), (Ib) and (Ic) [CH 3 -CH -N(CH 2 -COO) 2]M 3-x H x (Ia) wherein M is selected from alkali metal cations, same or different, and x is from zero to 1.0, [OOC-CH 2 CH 2 C-CH -N(CH 2 -COO) 2]M 4-x Hx (Ib) wherein M is selected from alkali metal cations, same or different, and x is from zero to 2.0, [H-N-(CH -CH 2 COO) 2]M 4-x H x (Ic) wherein M is selected from alkali metal cations, same or different, and x is from zero to 2.0, said process comprising the steps of (a) introducing an aqueous solution or aqueous slurry of the respective chelating agent into a spray-dryer or spray-granulator, and removing most of said water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250°C, (b) withdrawing powder or granules, respectively, from the spray-dryer or spray-granulator, respectively, (c) separating off fines from said powder or granules, wherein said fines have a maximum particle diameter of 30 μm in the case of powders and a maximum particle diameter of 350 μm in the case of granules, (d) separating off lumps from said powder or granules, wherein said lumps have a particle diameter of 250 μm or more in the case of powders and 1,000 μm or more in the case of granules, respectively, (e) milling said lumps to a maximum particle diameter of 500 μm in the case of granules or to 40 μm in the case of powders, respectively, (f) re-introducing said fines from step (c) and milled lumps from step (e) into the spray-dryer or spray-granulator, wherein the share of fines is in the range of from 4 to 18 % by weight of the total chelating agent withdrawn in step (b) and the share of milled lumps from step (e) is in the range of from 20 to 40% by weight of the total chelating agent withdrawn in step (b). (a) introducing an aqueous solution or aqueous slurry of the respective chelating agent into a spray-dryer or spray-granulator, and removing most of said water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250°C, (b) withdrawing powder or granules, respectively, from the spray-dryer or spray-granulator, respectively, (c) separating off fines from said powder or granules, wherein said fines have a maximum particle diameter of 30 μm in the case of powders and a maximum particle diameter of 350 μm in the case of granules, (d) separating off lumps from said powder or granules, wherein said lumps have a particle diameter of 250 μm or more in the case of powders and 1,000 μm or more in the case of granules, respectively, (e) milling said lumps to a maximum particle diameter of 500 μm in the case of granules or to 40 μm in the case of powders, respectively, (f) re-introducing said fines from step (c) and milled lumps from step (e) into the spray-dryer or spray-granulator,