Recuperatio processus de sodium sulfate in Lithium altilium productio

In redivivus processus de vastum ternary Lithium gravida et Calcium ferrum phosphate batteries, sulphuric acid et causticum nitri sunt inevitabiliter conversus in sodium sulfate sales propter technological requisita. The raw solution containing sodium sulfate mainly includes the return solution of lithium salt system, the solution after synthesis of ternary nickel-cobalt, the ternary pre-treatment discharge brine, the solution after precipitation of lithium iron phosphate, the discharge brine of lithium iron phosphate, the solution after precipitation of lithium lithium by lithium lithium salt, the residual solution of Nickel, Cobalt, manganese sal, solutio post synthesim de Nickel, Cobalt, Manganese, etc His solutiones sunt directe vel purificatus in MVR ad producendum anhydrous sodium sulfate products. Pelagus productio processus est ut sequitur:

I. Misce liquorem
Termary Nickel, Cobalt synthesis Liquid, ternary pre-tractata missionem murmur, Lithium ferrum phosphate post sedes Lithium, Lithium Ferrum PHOSPHATE Manganese Ferrum Ferrum Nickel Cobalt Manganese SALNTHESIs LIQUIDUS et alias liquida Manganese.

II. Impurities et conflans
Post parasceve Sodium sulfate solutio per liquid alkali + sodium sulfide profundum ad removere gravibus metalla (torcular filter de parva moles Nickel et Cobalt Slag, Redi ad Pasce pro reuse), adjust ad V ~ VII; Post analysis est qualified, rudis liquida cisternina est ingressus, et rudis liquida piscinam plays partes in thesaurizantes et regulanting ad rudis liquida in occursum continua et firmum operationem MVR Wastewater in occursum continua et firmum operationem in MVR Wastewater evaporator. Et rudis liquida cisternina est instructa cum rudis liquida sentinam. Rudis liquidum sentinam aequaliter de sodium sulfate aqueum solutio ad evaporatio curatio ratio. Et imperium valvae post rudis liquida sentinam est adaequatum ponere statera inter elevatio moles rudis liquidum et evaporatio moles.

III. Redi solution
Sodium sulfate decahydrate crystallum produci a lithium salis systematis additur ad condensatum aqua et demersa lithium lava aqua ad formare paene sodium sodium sulfate solution, quae est in separato stock liquida et concentration ratio.

IV. MVR evaporatio et crystallization sodium sulfate solutio
Aqueous solution continet sodium sulfate est preheated a condensate preheater et tunc intrat evaporatio camera MVR evaporatio crystallization ratio. MVR evaporatio system instructum cum verticali calor exchanger post coactus circulation sentinam. Under the action of the forced circulation pump, the material liquid flows in such a circulation along the evaporation chamber – heat exchanger – forced circulation pump – heat exchanger – evaporation chamber, the material liquid is heated in the heat exchanger, and the gas-liquid-solid separation is realized in the evaporation chamber. Convenitur sal slurry mittitur ad sale ex fluxum laoreet ad concentration et separationem, et tunc dimitti in sale subsiderit ad collectionem et concentration et separationem, et tandem dimitti in centrifuge et centrifuga separationem. Centrifuga filtrate et sal Serena supernatant colliguntur in filtrate tristique misit ad MVR evaporator pro evaporatio et crystallization. Sodium sulfate separata a centrifuge intrat in siccatio ratio.

V. ACTILIO - Packaging
Sodium sulfate adeptus a crystallization continet parva aqua et fretus in reuse statu, determinatur utrum uti siccatio apparatu ad redigendum aqua. Et siccatio apparatu potest esse fluidized lectum siccatio (potestate siccatio temperatus ~ CL ℃), aperire pulveris et pulvis collection fulling lectum et in sulfate et in sulfate ad obtinendam anhydrous sodium et ad tremendum est enshydrous sodium sulfate et ad obtinendam anhydrous sodium sulfate products (aquarum contentus <0.5%), packaging ad export) 0.5%), packaging ad export <0.5%), packaging ad export <0.5% ad export.