PACKAGING BODY OF MEDICAL ADHESIVE SHEET
    1.
    发明申请
    PACKAGING BODY OF MEDICAL ADHESIVE SHEET 审中-公开
    医用胶粘剂包装体

    公开(公告)号:US20140308472A1

    公开(公告)日:2014-10-16

    申请号:US14354439

    申请日:2012-10-26

    IPC分类号: C09J7/02

    摘要: Provided is a packaging that is for a medical adhesive sheet, results from housing a medical adhesive sheet resulting from a peelable liner being pasted to the surface to which an adhesive agent layer has been formed of a resin film having the adhesive agent layer, and is characterized by: the medical adhesive sheet being folded in a manner so that the surface to which the peelable liner is provided is the inner surface and the surface to which the resin film is provided is the outer surface; the folded medical adhesive sheet being sandwiched between packaging sheets; and the packaging sheets being sealed at the ends thereof.

    摘要翻译: 本发明提供一种用于医用粘合片的包装,其特征在于,将由可剥离衬垫制成的医用粘合片从由粘合剂层形成的树脂膜粘贴到形成有粘合剂层的表面上, 其特征在于,所述医用粘合片以使得设置有可剥离衬垫的表面为内表面而设置树脂膜的表面为外表面的方式折叠; 折叠的医用粘合片夹在包装片之间; 并且包装片在其端部被密封。

    PURIFICATION APPARATUS
    4.
    发明公开

    公开(公告)号:US20240252951A1

    公开(公告)日:2024-08-01

    申请号:US18566207

    申请日:2022-05-31

    IPC分类号: B01D9/02 C07C51/43

    CPC分类号: B01D9/02 C07C51/43

    摘要: Provided is a method for stably obtaining a product. The present invention relates to a purification apparatus for purifying a compound, the purification apparatus including: a tank for use in the purification apparatus; and a hydraulic wash column, the tank being at least one of a crystallization tank that forms a slurry containing crystals of a compound or a ripening tank that is capable of keeping crystals of a compound suspended in the ripening tank, the tank including an agitator having an agitator shaft and a bearing, the purification apparatus further including:



    a line for discharging the slurry containing crystals of a compound from the tank and feeding the slurry to the hydraulic wash column; and a line for flowing between the agitator shaft and the bearing in the tank at least one of a mother liquor derived from the slurry fed to the hydraulic wash column, the slurry containing crystals of a compound, or a melt obtained by melting the crystals.

    NON-AQUEOUS ELECTROLYTE AND SECONDARY BATTERY

    公开(公告)号:US20240213539A1

    公开(公告)日:2024-06-27

    申请号:US18287359

    申请日:2022-03-14

    IPC分类号: H01M10/0568

    CPC分类号: H01M10/0568 H01M2300/0025

    摘要: A non-aqueous electrolyte solution, containing: compounds represented by the general formulae (1) to (3):
    LiN(R1SO2)(R2SO2) (where R1 and R2 are identical to or different from each other and each represent a fluorine atom, an alkyl group having 1 to 6 carbon atoms, or a fluoroalkyl group with 1 to 6 carbon atoms) (1)


    LiPFa(CmF2m+1)6−a (where 0≤a≤6 and 1≤m≤4)  (2)



    (Li)m(A)n(UFx)y (where A represents an oxygen atom, a sulfur atom, a phosphorus atom, or a nitrogen atom, U represents a boron atom or a phosphorus atom, 1≤m≤6, 1≤n≤6, x is 3 or 5, and 1≤y≤6)  (3).

    METHOD FOR PRODUCING WATER-ABSORBING RESIN
    9.
    发明公开

    公开(公告)号:US20240101766A1

    公开(公告)日:2024-03-28

    申请号:US18263144

    申请日:2022-01-31

    IPC分类号: C08J3/075 C08J3/24

    摘要: Provided is a production method for a water-absorbing resin in which an absorption capacity without pressure of the resulting water-absorbing resin is high and a water-absorbing resin can be efficiently obtained.
    The production method for a water-absorbing resin including a polymerization step of polymerizing a monomer composition containing an internal crosslinking agent and a monomer to obtain a crosslinked hydrogel polymer, and a drying step of drying the crosslinked hydrogel polymer to obtain a dry polymer, in which the crosslinked hydrogel polymer to be subjected to the drying step contains 50 ppm or more of hydrogen peroxide with respect to the solid content mass of the crosslinked hydrogel polymer, and the crosslinked hydrogel polymer is heated during the drying step so that a maximum reaching temperature of the crosslinked hydrogel polymer exceeds 160° C., and/or the dry polymer is heated after the drying step so that a maximum reaching temperature of the dry polymer exceeds 160° C.