METHOD FOR RECYCLING LITHIUM BATTERY CATHODE MATERIAL

    公开(公告)号:US20230335817A1

    公开(公告)日:2023-10-19

    申请号:US18212697

    申请日:2023-06-21

    CPC classification number: H01M10/54 C22B7/008 C22B26/12

    Abstract: A method for recycling a lithium battery cathode material. Residual aluminum on the positive electrode sheet is dissolved by a sodium hydroxide solution, and lithium in the cathode material enters the solution during the dissolution of aluminum, such that an ionic potential is vacated on the cathode material; a residue is washed to avoid sodium ion contamination, then dried, and allowed to react with metallic lithium and lithium sulfide under heating, such that crystal lattices of the material change; a product after first-stage lithium supplementation is directly sintered with a lithium source in an oxygen atmosphere to obtain monocrystalline ternary cathode material agglomerates, where a sintering method and a sintering temperature are controlled; and the agglomerates are crushed, then washed to remove residual lithium on the surface, and dried to obtain a monocrystalline ternary cathode material, which has the performance close to that of the initially synthesized monocrystalline cathode material.

    A METHOD OF SEPARATING AND RECOVERING BROMINE FROM PRINTED CIRCUIT BOARD INCINERATION ASH BY TWO-STEP PROCESS

    公开(公告)号:US20230192488A1

    公开(公告)日:2023-06-22

    申请号:US16627721

    申请日:2019-01-15

    Inventor: DEAN PAN YUFENG WU

    Abstract: The invention relates to the field of efficient separation and recovery of bromine by full wet method, especially to a two-step separating method of bromide and recovery of lead and zinc from printed circuit board Incineration ash. It mainly includes first sodium hydroxide alkaline leaching, secondary sodium peroxide alkaline leaching, pH adjustment, separate lead and zinc, bromide evaporation and crystallization to recover crude bromide and other steps. Compared with traditional comprehensive recovery process of ash, the invention uses sodium hydroxide to dissolve bromide, lead and zinc, and uses the strong oxidation of sodium peroxide in alkaline environment, copper bromide and other bromine are oxidized and leached; through two-step method, the efficient leaching of bromine, lead and zinc is realized, silver and other precious metals are enriched at the same time. It is beneficial to subsequent recovery of precious metals and has the characteristics of short tail liquid discharge.

    Process for recovering zinc and/or zinc oxide II
    10.
    发明授权
    Process for recovering zinc and/or zinc oxide II 有权
    回收锌和/或氧化锌的方法II

    公开(公告)号:US09284624B2

    公开(公告)日:2016-03-15

    申请号:US13988911

    申请日:2011-11-23

    Abstract: A process for recovering zinc from a zinc containing material, the process including the steps of: leaching the zinc containing material with an alkaline lixiviant comprising an aqueous mixture of NH3 and NH4Cl, or ionic equivalent, having a NH4Cl concentration of between about 10 g/L and about 150 g/L H2O and a NH3 concentration of between 20 g/l H2O and 250 g/L H2O, to produce a zinc containing leachate; stripping ammonia from the leachate to produce a stripped liquor which includes a zinc containing precipitate, the stripped liquor having a NH3 concentration of between 7 and 30 g/L H2O; and recovering the zinc from the stripped liquor.

    Abstract translation: 一种从含锌材料中回收锌的方法,该方法包括以下步骤:用包含NH 3和NH 4 Cl的水性混合物或离子当量的碱性浸液浸出含锌材料,其NH 4 Cl浓度为约10g / L和约150g / L H 2 O和NH 3浓度在20g / l H 2 O和250g / L H 2 O之间,以产生含锌浸出液; 从渗滤液中除去氨以产生包含含锌沉淀物的汽提液,所述汽提液体的NH 3浓度为7至30g / L H 2 O; 并从汽提液中回收锌。

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