Coating method for positive electrode material for sulfide solid-state battery
A positive electrode material, solid-state battery technology, applied in battery electrodes, active material electrodes, positive electrodes, etc., can solve the problem that it is difficult to achieve the coating effect of sulfide electrolyte, cannot ensure the uniformity and integrity of the coating layer, and is difficult to be coated with sulfide electrolyte. problems such as uniform coverage
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Embodiment 1
[0028] 5kg LiCoO 2 The positive electrode material is placed in the reaction chamber of the ALD equipment, and when the temperature of the reaction chamber reaches 350 °C, the 2 WO 4 Stoichiometric ratio of each element loading precursor source lithium tert-butoxide C 4 H 9 LiO, tungsten hexacarbonyl W(CO) 6 , H 2 O into the reaction chamber. Among them, the chamber pressure was 0.7 mbar, and the number of pulse cycles of the precursor source was 200 times. Replace the precursor source of the sulfide electrolyte, and continue to load 0.05M Li with inert gas when the temperature of the reaction chamber reaches 200 °C 3 PS 4Vaporize the N-methylformamide solution into the reaction chamber. Among them, the chamber pressure was 0.8 mbar, and the number of pulse cycles of the precursor source was 1000 times. After the sulfide electrolyte coating process is completed, the temperature of the reaction chamber is increased to 400 ° C, so that the coated cathode material is dir...
Embodiment 2
[0030] 5kg LiNi 0.8 Co 0.1 Mn 0.1 O 2 The positive electrode material is placed in the reaction chamber of the ALD equipment, and when the temperature of the reaction chamber reaches 300 °C, the 3 BO 3 Stoichiometric ratio of each element loading precursor source lithium tert-butoxide C 4 H 9 LiO, triethyl borate C 6 H 15 BO 3 , H 2 O into the reaction chamber. Among them, the chamber pressure was 0.7 mbar, and the number of pulse cycles of the precursor source was 200 times. Replace the precursor source of the sulfide electrolyte, and continue to load 0.01M Li with inert gas when the temperature of the reaction chamber reaches 100 °C 6 PS 5 Vaporization mist of Cl in ethanol solution into the reaction chamber. Among them, the chamber pressure was 0.8 mbar, and the number of pulse cycles of the precursor source was 5000 times. After the sulfide electrolyte coating process is completed, the temperature of the reaction chamber is increased to 450 °C, so that the co...
Embodiment 3
[0032] 5kg LiNi 0.6 Co 0.2 Mn 0.2 O 2 The positive electrode material is placed in the reaction chamber of the ALD equipment, and when the temperature of the reaction chamber reaches 300 °C, the 3 PO 4 Stoichiometric ratio of each element loading precursor source lithium tert-butoxide C 4 H 9 LiO, triethyl phosphate C 6 H 15 O 4 P.H 2 O into the reaction chamber. Among them, the chamber pressure was 0.7 mbar, and the number of pulse cycles of the precursor source was 200 times. Replace the precursor source of the sulfide electrolyte, and continue to load 0.01M Li with inert gas when the temperature of the reaction chamber reaches 100 °C 7 P 3 S 11 Vaporize the acetonitrile solution into the reaction chamber. Among them, the chamber pressure was 0.8 mbar, and the number of pulse cycles of the precursor source was 5000 times. After the sulfide electrolyte coating process is completed, the temperature of the reaction chamber is increased to 450 °C, so that the coat...
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