SILVER PLATING SOLUTION AND METHOD OF SILVER PLATING BY CHEMICAL REPLACEMENT
    2.
    发明申请
    SILVER PLATING SOLUTION AND METHOD OF SILVER PLATING BY CHEMICAL REPLACEMENT 审中-公开
    镀银溶液和化学镀替代方法

    公开(公告)号:WO2015027886A1

    公开(公告)日:2015-03-05

    申请号:PCT/CN2014/085127

    申请日:2014-08-25

    CPC classification number: C23C18/54

    Abstract: A silver plating solution is provided. The silver plating solution, including: a silver salt; a complexing agent, comprising ethylenediamine and potassium ferrocyanide; a surfactant, comprising peregal; and an addition agent, comprising benzotriazole; wherein the value of pH of the silver plating solution is 7.8 to 9.6. A method of silver plating by chemical replacement is provided, including: placing the workpiece to be plated into the silver plating solution, wherein the silver plating solution is the silver plating solution of the present disclosure.

    Abstract translation: 提供镀银溶液。 镀银溶液,包括:银盐; 一种络合剂,包括乙二胺和亚铁氰化钾; 表面活性剂,其包含: 和包含苯并三唑的添加剂; 其中所述镀银溶液的pH值为7.8至9.6。 提供了通过化学更换进行镀银的方法,包括:将待镀的工件放置在镀银溶液中,其中镀银溶液是本公开的镀银溶液。

    HEAT-DISSIPATING SUBSTRATE, PREPARATION METHOD AND APPLICATION THEREOF, AND ELECTRONIC COMPONENT

    公开(公告)号:EP3564988A1

    公开(公告)日:2019-11-06

    申请号:EP17885508.6

    申请日:2017-12-08

    Abstract: This disclosure relates to the field of heat dissipation substrates for encapsulating electronic devices, and discloses a heat dissipation substrate, a method for preparing same, an application of same, and an electronic device. The heat dissipation substrate includes: a metal-ceramic composite board, where the metal-ceramic composite board is a metal layer wrapping a ceramic body; a metal oxide layer integrated with the metal layer and formed on an outer surface of the metal layer; and a soldering metal layer formed on at least a part of an outer surface of the metal oxide layer, where the soldering metal layer is used to connect with a copper substrate and bear a chip.

    METHOD FOR SEPARATING IRON ELEMENT FROM BRINE AND USE THEREOF

    公开(公告)号:EP4458995A1

    公开(公告)日:2024-11-06

    申请号:EP22914190.8

    申请日:2022-12-12

    Abstract: The present disclosure provides a method for separating iron element in brine. A pH adjusting agent is added to brine, to adjust the brine to pH between 6.0 and 7.0, and the temperature of the brine is controlled to between 75°C and 90°C. An oxygen-containing gas is introduced into the brine, to covert the iron element in the brine into magnetic iron oxide. The magnetic iron oxide is separated from the brine by magnetic adsorption, to obtain an iron-removed brine. The brine includes geothermal brine.

    MAGNETIC TITANIUM-BASED LITHIUM ADSORBENT AND PREPARATION METHOD THEREFOR

    公开(公告)号:EP4454750A1

    公开(公告)日:2024-10-30

    申请号:EP22909883.5

    申请日:2022-12-16

    Abstract: A magnetic titanium-based lithium adsorbent includes a magnetic composite and a lithium adsorption layer. The lithium adsorption layer is located on an outer surface of the magnetic composite. The magnetic composite includes a magnetic material and a titanium oxide. The lithium adsorption layer includes a lithium titanium oxide. A method for preparing the magnetic titanium-based lithium adsorbent includes the following steps: a magnetic composite is obtained; a precursor of the magnetic titanium-based lithium adsorbent is prepared; and pre-desorption is carried out.

    METHOD FOR RECOVERING LITHIUM FROM LITHIUM-CONTAINING SOLUTION

    公开(公告)号:EP4410743A1

    公开(公告)日:2024-08-07

    申请号:EP22875109.5

    申请日:2022-09-29

    CPC classification number: C22B3/24 C22B3/44 C22B26/12 Y02P10/20

    Abstract: A method for recovering lithium from a lithium-containing solution is provided. A lithium-containing solution with an adjusted pH value or an unadjusted pH value is mixed with a meta-aluminate solution, and the pH value is adjusted to weak acid/neutral, so that lithium can be separated from the lithium-containing solution in the form of a precipitate of LiaX·2Al(OH)3·nH2O. Then, the precipitate is converted into a lithium adsorbent of (1-m)LiaX·2Al(OH)3·nH2O and a LiaX-containing filtrate through desorption of lithium. High-purity Li2CO3 is obtained by performing lithium precipitation on the LiaX-containing filtrate.

    LITHIUM EXTRACTION APPARATUS AND LITHIUM EXTRACTION METHOD

    公开(公告)号:EP4458443A1

    公开(公告)日:2024-11-06

    申请号:EP22914127.0

    申请日:2022-12-08

    Abstract: A lithium extraction apparatus and a lithium extraction method are provided. The lithium extraction apparatus includes a frame (2) and a transmission mesh belt (1). The transmission mesh belt (1) is installed on the frame (2), the transmission mesh belt (1) has water permeable holes, and the transmission mesh belt (1) is configured to carry an adsorbent. The frame (2) is sequentially provided with an adsorption zone (21) and a desorption zone (22) along a traveling direction of the transmission mesh belt (1). A brine spraying device (211) is arranged above the transmission mesh belt (1) in the adsorption zone (21). A desorbing liquid spraying device (221) is arranged above the transmission mesh belt (1) in the desorption zone (22). A lithium extract collecting device (222) is arranged below the transmission mesh belt (1) in the desorption zone (22). The transmission mesh belt (1) in the adsorption zone (21) is folded into a multi-layer structure in the vertical direction; and/or the transmission mesh belt (1) in the desorption zone (22) is folded into a multi-layer structure in the vertical direction.

    SUPERCRITICAL CARBON DIOXIDE CYCLE BASED POWER GENERATION-BRINE LITHIUM EXTRACTION COUPLING SYSTEM

    公开(公告)号:EP4345068A1

    公开(公告)日:2024-04-03

    申请号:EP22860308.0

    申请日:2022-08-16

    Abstract: A coupling system of supercritical carbon dioxide cycle power generation and lithium extraction from brine is provided. The system includes an absorption heat pump unit (100), a supercritical carbon dioxide cycle power generation unit (200), and a lithium extraction from brine unit (300). A brine inlet (32) of the lithium extraction from brine unit (300) is in communication with a to-be-heated material inlet (30) of the absorption heat pump unit (100). A heated material outlet (31) of the absorption heat pump unit (100) is in communication with a raw material inlet (33) of the lithium extraction from brine unit (300). A carbon dioxide cycle cold end outlet (36) of the supercritical carbon dioxide cycle power generation unit (200) is in communication with a heating medium inlet (34) of the lithium extraction from brine unit (300) and/or a driving heat source inlet (28) of the absorption heat pump unit (100). A carbon dioxide cycle cold end inlet (37) of the supercritical carbon dioxide cycle power generation unit (200) is in communication with a heating medium outlet (35) of the lithium extraction from brine unit (300) and/or a driving heat source outlet (29) of the absorption heat pump unit (100).

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