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    • 7. 发明授权
    • Method of estimating the lifetime of thermal barrier coatings
    • 估算热障涂层寿命的方法
    • US06681639B2
    • 2004-01-27
    • US10120416
    • 2002-04-12
    • Otto BernhardiRoland MueckeHans Joachim SchmutzlerChristoph SommerMarianne Sommer
    • Otto BernhardiRoland MueckeHans Joachim SchmutzlerChristoph SommerMarianne Sommer
    • G01N332
    • C23C28/3215C23C4/12C23C28/345C23C28/3455G01N17/00
    • A method of estimating the lifetime of a thermal barrier coating (14), which is applied to the surface of a member subjected to cyclical thermal loads, especially a vane and/or blade of a gas turbine, by means of a bond coat (12) lying in between the coating and the member, leads to more accurate results with simplified calculation by determining, in a first step, the amplitude of the normal stress (&Dgr;&sgr;n) perpendicular to the interface between the bond coat (12) and the thermal barrier coating (14) during cyclical loading, and calculating, in a second step, the number Ni of cycles to failure for every normal stress amplitude (&Dgr;&sgr;n) in accordance with the formula N i ⁢   = C ⁡ ( △σ n σ 0 ) m where &sgr;0 is a stress reference value and C(&dgr;ox) and m(&dgr;ox) are material parameters, which depend on the thickness (&Dgr;ox) of an oxide layer (13), which is located between the thermal barrier layer (14) and the bond coat (12) and grows with the cyclical loading.
    • 一种估计热障涂层(14)的寿命的方法,其通过粘合涂层(12)施加到受到循环热负荷的构件的表面,特别是燃气轮机的叶片和/或叶片 )通过在第一步骤中确定垂直于粘合涂层(12)和热障壁之间的界面的法向应力(Deltasigman)的振幅,通过简化的计算得到更准确的结果, 在循环加载期间涂覆(14),并且在第二步骤中,计算根据公式sigma0的每个法向应力幅度(Deltasigman)的失效循环次数Ni是应力参考值,C(deltaox)和m( deltaox)是材料参数,其取决于位于热阻层(14)和粘合涂层(12)之间的氧化物层(13)的厚度(Deltaox),并以循环负载生长。
    • 8. 发明授权
    • Electrolyzer apparatus
    • 电解器
    • US09353450B2
    • 2016-05-31
    • US13988027
    • 2011-11-16
    • Philippe MorelleJoachim LangeChristoph Sommer
    • Philippe MorelleJoachim LangeChristoph Sommer
    • C25B15/02C25B1/24
    • C25B15/02C25B1/245
    • An electrolyzer apparatus for the electrolytic manufacture of elemental F2 from an electrolyte/HF-solution, e.g., KF×1.8 HF, comprising at least one electrolytic cell which contains at least two anodes, often 20 to 30 anodes, a metallic cathodic vessel, and at least two rectifiers such that each anode is allocated to one rectifier. In this manner, each anode can be controlled and regulated individually. Failure of each individual anode, e.g., anode break, causes the production of undesired side products, e.g., of CF4. Any faulty anode can be detected easily, and each anode can be shut off individually, if needed, and repaired.
    • 一种用于从电解质/ HF溶液(例如KF×1.8HF)电解制造元素F2的电解装置,其包括至少一个电解槽,其包含至少两个阳极,通常20至30个阳极,金属阴极容器和 至少两个整流器,使得每个阳极分配给一个整流器。 以这种方式,可以单独地控制和调节每个阳极。 每个单独阳极(例如阳极断裂)的故障导致产生不期望的副产物,例如CF 4。 可以容易地检测到任何有故障的阳极,如果需要,可以单独关闭阳极并进行维修。
    • 9. 发明申请
    • Electrolyzer Apparatus
    • 电解器
    • US20130233723A1
    • 2013-09-12
    • US13988027
    • 2011-11-16
    • Philippe MorelleJoachim LangeChristoph Sommer
    • Philippe MorelleJoachim LangeChristoph Sommer
    • C25B15/02C25B1/24
    • C25B15/02C25B1/245
    • An electrolyzer apparatus for the electrolytic manufacture of elemental F2 from an electrolyte/HF-solution, e.g., KF×1.8 HF, comprising at least one electrolytic cell which contains at least two anodes, often 20 to 30 anodes, a metallic cathodic vessel, and at least two rectifiers such that each anode is allocated to one rectifier. In this manner, each anode can be controlled and regulated individually. Failure of each individual anode, e.g., anode break, causes the production of undesired side products, e.g., of CF4. Any faulty anode can be detected easily, and each anode can be shut off individually, if needed, and repaired.
    • 一种用于从电解质/ HF溶液(例如KF×1.8HF)电解制造元素F2的电解装置,其包括至少一个电解槽,其包含至少两个阳极,通常20至30个阳极,金属阴极容器和 至少两个整流器,使得每个阳极分配给一个整流器。 以这种方式,可以单独地控制和调节每个阳极。 每个单独阳极(例如阳极断裂)的故障导致产生不期望的副产物,例如CF 4。 可以容易地检测到任何有故障的阳极,如果需要,可以单独关闭阳极并进行维修。