LITHIUM ADSORBENT, AND PREPARATION METHOD AND APPLICATION THEREOF

    公开(公告)号:US20250153141A1

    公开(公告)日:2025-05-15

    申请号:US18936689

    申请日:2024-11-04

    Abstract: Disclosed are a lithium adsorbent, and a preparation method and an application thereof, which relate to the technical of extraction of lithium. The method of the disclosure includes obtaining a lithium adsorbent intermediate by mixing an oil phase with an aqueous phase; and obtaining the lithium adsorbent by mixing the lithium adsorbent intermediate with an organic auxiliary agent; where the oil phase includes a lithium source, an aluminum source, an oil-phase matrix, and an oil-phase auxiliary agent, and the oil-phase matrix includes a high-molecular polymer and vinylidene fluoride; the mixing an oil phase with an aqueous phase includes performing gradient stirring on a mixture of the oil phase and the aqueous phase. According to the disclosure, the high-stability lithium adsorbent can be prepared by optimizing and screening the high-temperature resistant oil-phase matrix and a specific preparation process. Compared with an existing lithium adsorbent, the lithium adsorbent prepared through the disclosure has less degradation, better mechanical strength, and stronger corrosion resistance in a high-temperature environment, and therefore a way of effectively extracting lithium resources from high-temperature and high-salt brine is provided.

    METHOD FOR EXTRACTING LITHIUM FROM BRINE, AND APPLICATION

    公开(公告)号:US20250136458A1

    公开(公告)日:2025-05-01

    申请号:US18928921

    申请日:2024-10-28

    Abstract: Disclosed are a method for extracting lithium from brine, and an application. The method includes performing extraction on the brine through a continuous ion exchange process, where according to the continuous ion exchange process, in an adsorption section, adsorption is performed on the brine with an aluminum-based lithium adsorbent; in a water-pushing-material section, a resin column is washed with a solution; in a desorption section, desorption is performed with pure water, and a desorption solution is collected in segments; and in a material-pushing-water section, a solution in a resin column is replaced by spent brine. The solution used in the water-pushing-material section is a front-segment collected liquid in the desorption section, and the front-segment collected liquid satisfies the following parameter: 520 us*cm−1

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