摘要:
Provided is a method for preparing manganese sulfate monohydrate, which comprises the following steps: (1) reacting MnO with (NH 4 ) 2 SO 4 solution under heat, and separating solid from liquid after reaction; 2) determining the concentration of MnSO 4 in the resulting solution of step 1), adding equimolar ammonium sulfide solution thereto to carry out reaction under agitation, separating solid from liquid after reaction, and then washing solid phase; 3) dissolving the solid phase with concentrated sulfuric acid, adding hydrogen peroxide to the obtained solution, heating to boiling, adjusting the pH value of the solution to 5-6, removing the solid phase through precise filtration, evaporating and oven drying the filtrate to obtain MnSO 4 •H 2 O product. The impurities are separated away and the amount of byproducts is reduced by this method, and the yield of manganese sulfate monohydrate is improved.
摘要:
Braunstein-haltige Manganerze werden in wäßriger Suspension mittels Schwefeldioxid und Luft dadurch aufgeschlossen, daß man Schwefeldioxid in reiner Form einspeist und die Luftzufuhr so regelt, daß ein Partialdruckverhältnis pS0 2 : pO 2 von 4 bis 14, vorzugsweise 8 bis 12, und ein pH-Wert von höher als 4, vorzugsweise höher als 4,2, eingehalten wird. Das Verfahren ist allein für die Messung des pH-Wertes steuerbar, sehr umweltfreundlich und mit großer Wirtschaftlichkeit durchführbar.
摘要:
The present invention describes a method of making manganous sulphate solution with low level impurity of potassium from high potassium ores which comprises adding the reduced ore to spent electrolyte containing ferric ions and digesting same at pH 1-2 and temperature of 60-90°C for 1-4 hours, and if desired thereafter again adding reduced ore to the digested product till pH is raised to 4-6.
摘要:
The invention relates to a method for producing manganese sulfate monohydrate. According to the invention, this method comprises: • a stage of electric leaching (S2) of manganese-comprising ore at a temperature from 20°C to 40°C and under constant air purging in a diaphragm-less electrolyzer, • stages of jarosite (S3), hydrolytic (S4), sulfide (S5) and fluoride (S6) purification of the obtained solutions, • a stage of autoclave crystallization (S7) of a salt at a temperature from 160°C to 165°C and at a pressure from 0,60 MPa to 0,65 MPa. In addition, the stage of electric leaching (S2) is performed with a concentration of iron ions from 3,5 g/l to 4,5 g/l using a stainless steel mesh as a cathode with a cathode current density from 200 A/m 2 to 250 A/m 2 . A process control at the electric leaching stage (S2) is carried out by changing a value of a redox potential of a Fe 3+ /Fe 2+ system. The obtained salt is flushed with anhydrous methanol at a temperature from 30°C to 40°C during from 0,5 hour to 1 hour, while a ratio of a salt crystal mass and an anhydrous methanol volume is 1/2,5 kg/I.
摘要:
The invention relates to a method for producing manganese sulfate monohydrate. According to the invention, this method comprises: • a stage of electric leaching (S2) of manganese-comprising ore at a temperature from 20°C to 40°C and under constant air purging in a diaphragm-less electrolyzer, • stages of jarosite (S3), hydrolytic (S4), sulfide (S5) and fluoride (S6) purification of the obtained solutions, • a stage of autoclave crystallization (S7) of a salt at a temperature from 160°C to 165°C and at a pressure from 0,60 MPa to 0,65 MPa. In addition, the stage of electric leaching (S2) is performed with a concentration of iron ions from 3,5 g/l to 4,5 g/l using a stainless steel mesh as a cathode with a cathode current density from 200 A/m 2 to 250 A/m 2 . A process control at the electric leaching stage (S2) is carried out by changing a value of a redox potential of a Fe 3+ /Fe 2+ system. The obtained salt is flushed with anhydrous methanol at a temperature from 30°C to 40°C during from 0,5 hour to 1 hour, while a ratio of a salt crystal mass and an anhydrous methanol volume is 1/2,5 kg/I.
摘要:
In a method of recovering an active metal of a lithium secondary battery, a cathode active material mixture obtained from a used cathode of a lithium secondary battery is prepared. The cathode active material mixture is reacted in a fluidized bed reactor to form a preliminary precursor mixture. A lithium precursor is recovered from the preliminary precursor mixture. Yield and selectivity of a lithium precursor can be improved using the fluidized bed reactor.