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    • 2. 发明授权
    • Electrode for peroxide generator and method for preparing it
    • 用于过氧化物发生器的电极及其制备方法
    • US5695622A
    • 1997-12-09
    • US754003
    • 1996-11-21
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • C25B1/30C25B11/03C25B11/04H01M4/90
    • H01M4/9083C25B1/30C25B11/035C25B11/0473H01M4/90
    • In the disclosed electrochemical cell for the production of an alkaline solution of peroxide, especially on-site production, the electrolyte is divided into an aqueous alkaline catholyte and an aqueous alkaline anolyte, and the cathode is a gas-diffusion electrode. The active material of the electrolyte side of the gas-diffusion cathode comprises a particulate catalyst support material having a surface area of about 50 to about 2000 m.sup.2 /g, and, deposited on the particles of this support material, 0.1 to 50 weight-%, based on the weight of the active layer, of gold or gold alloy particles having an average size >40 but less than about 200 .ANG.. These gold or gold alloy particles are substantially selectively catalytic for the reduction of oxygen to peroxide (e.g. HOO.sup..crclbar.). The electrolyte flow patterns are designed to avoid loss of peroxide resulting from oxidation at the anode. In the operation of the cell, a product with a hydroxyl:perhydroxyl ratio lees than 2:1 can be obtained.
    • 在所公开的用于生产过氧化物碱性溶液的电化学电池中,特别是现场生产,电解质分为碱性阴极电解液和碱性阳极电解液,阴极是气体扩散电极。 气体扩散阴极的电解质侧的活性材料包括具有约50至约2000m 2 / g的表面积的颗粒状催化剂载体材料,并沉积在该载体材料的颗粒上,0.1至50重量% 基于活性层的重量,具有平均尺寸> 40但小于约200的金或金合金颗粒。 这些金或金合金颗粒对于将氧还原成过氧化物(例如HOO( - ))基本上是选择性催化的。 电解质流动图案被设计为避免由阳极氧化引起的过氧化物的损失。 在电池的操作中,可以获得羟基:全羟基比例为2:1的产品。
    • 3. 发明授权
    • Process for making peroxide
    • 制造过氧化物的方法
    • US5647968A
    • 1997-07-15
    • US633563
    • 1996-04-17
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • C25B1/30C25B11/03C25B11/04H01M4/90
    • H01M4/9083C25B1/30C25B11/035C25B11/0473H01M4/90
    • In the disclosed electrochemical cell for the production of an alkaline solution of peroxide, especially on-site production, the electrolyte is divided into an aqueous alkaline catholyte and an aqueous alkaline anolyte, and the cathode is a gas-diffusion electrode. The active material of the electrolyte side of the gas-diffusion cathode comprises a particulate catalyst support material having a surface area of about 50 to about 2000 m.sup.2 /g, and, deposited on the particles of this support material, 0.1 to 50 weight-%, based on the weight of the active layer, of gold or gold alloy particles having an average size >40 but less than about 200.ANG.. These gold or gold alloy particles are substantially selectively catalytic for the reduction of oxygen to peroxide (e.g. HOO.sup..crclbar.). The electrolyte flow patterns are designed to avoid loss of peroxide resulting from oxidation at the anode. In the operation of the cell, a product with a hydroxyl:perhydroxyl ratio less than 2:1 can be obtained.
    • 在所公开的用于生产过氧化物碱性溶液的电化学电池中,特别是现场生产,电解质分为碱性阴极电解液和碱性阳极电解液,阴极是气体扩散电极。 气体扩散阴极的电解质侧的活性材料包括具有约50至约2000m 2 / g的表面积的颗粒状催化剂载体材料,并沉积在该载体材料的颗粒上,0.1至50重量% 基于活性层的重量,具有平均尺寸> 40但小于约200的金或金合金颗粒。 这些金或金合金颗粒对于将氧还原成过氧化物(例如HOO( - ))基本上是选择性催化的。 电解质流动图案被设计为避免由阳极氧化引起的过氧化物的损失。 在电池的操作中,可以获得羟基:全羟基比小于2:1的产物。
    • 4. 发明授权
    • Electrochemical peroxide generator
    • 电化学过氧化物发生器
    • US5565073A
    • 1996-10-15
    • US463752
    • 1995-06-05
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • Mark E. FraserAlan S. WoodmanEverett B. AndersonE. Jennings Taylor
    • C25B1/30C25B11/03C25B11/04H01M4/90C25B9/00
    • H01M4/9083C25B1/30C25B11/035C25B11/0473H01M4/90
    • In the disclosed electrochemical cell for the production of an alkaline solution of peroxide, especially on-site production, the electrolyte is divided into an aqueous alkaline catholyte and an aqueous alkaline anolyte, and the cathode is a gas-diffusion electrode. The active material of the electrolyte side of the gas-diffusion cathode comprises a particulate catalyst support material having a surface area of about 50 to about 2000 m.sup.2 /g, and, deposited on the particles of this support material, 0.1 to 50 weight-%, based on the weight of the active layer, of gold or gold alloy poly-crystal particles having an average size .gtoreq.5 but less than about 20 nanometers. These poly-crystal gold or gold alloy particles have a structure consisting essentially of combined individual monocrystals and are substantially selectively catalytic for the reduction of oxygen to peroxide ion or hydrogen peroxide (e.g. HOO.sup..theta.). The electrolyte flow patterns are designed to avoid loss of peroxide resulting from oxidation at the anode. In the operation of the cell, a product with a hydroxyl:perhydroxyl ratio less than 2:1 can be obtained.
    • 在所公开的用于生产过氧化物碱性溶液的电化学电池中,特别是现场生产,电解质分为碱性阴极电解液和碱性阳极电解液,阴极是气体扩散电极。 气体扩散阴极的电解质侧的活性材料包括具有约50至约2000m 2 / g的表面积的颗粒状催化剂载体材料,并沉积在该载体材料的颗粒上,0.1至50重量% 基于活性层的重量,具有平均尺寸≥5但小于约20纳米的金或金合金多晶粒子。 这些多晶金或金合金颗粒具有基本上由组合的单个单晶组成的结构,并且对于将氧还原成过氧化物离子或过氧化氢(例如HOOO)基本上是选择性催化的。 电解质流动图案被设计为避免由阳极氧化引起的过氧化物的损失。 在电池的操作中,可以获得羟基:全羟基比小于2:1的产物。