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    • 1. 发明授权
    • Process for the synthetic generation of methane
    • 甲烷合成生成工艺
    • US08313544B2
    • 2012-11-20
    • US10589158
    • 2005-01-24
    • Martin SeemannSerge BiollazSamuel Stucki
    • Martin SeemannSerge BiollazSamuel Stucki
    • B23K35/38
    • C07C1/046C07C1/043C07C2523/755C07C9/04
    • In a process for the synthetic generation of methane from a feed gas mixture, a feed gas mixture including carbon monoxide, hydrogen, water vapor, CO2, volatile hydrocarbons comprising C2 and higher, unsaturated C2 components and aromatic hydrocarbons in the range of 1 to 10 vol % is provided. The feed gas mixture is contacted with a fluidized bed catalyst having catalyst particles having a catalytic active component selected from the group consisting of a metal, a metal compound and combinations thereof. The contacting occurs at an elevated temperature in the range of 250 to 450° C., a feed gas pressure in the range of 0.8 to 70 bar, a gas hourly space velocity of 1000 to 50000 h−1, and a concentration of H2/CO in the gas mixture in the range of 0.25 to 5.
    • 在从进料气体混合物合成生成甲烷的方法中,包括一氧化碳,氢气,水蒸汽,CO 2,包含C2和更高级别的不饱和C2组分和芳族烃的挥发性烃的进料气体混合物的范围为1至10 提供vol%。 进料气体混合物与具有催化剂颗粒的流化床催化剂接触,催化剂颗粒具有选自金属,金属化合物及其组合的催化活性组分。 接触在250至450℃的升高的温度,0.8至70巴的进料气体压力,1000至50000h -1的气时空速和H 2 / CO在气体混合物中的范围为0.25至5。
    • 9. 发明申请
    • Process for the Synthetic Generation of Methane
    • 甲烷合成生成工艺
    • US20070299288A1
    • 2007-12-27
    • US10589158
    • 2005-01-24
    • Martin SeemannSerge BiollazSamuel Stucki
    • Martin SeemannSerge BiollazSamuel Stucki
    • C07C1/10
    • C07C1/046C07C1/043C07C2523/755C07C9/04
    • In a process for the synthetic generation of methane from a feed gas mixture, a feed gas mixture including carbon monoxide, hydrogen, water vapor, CO2, volatile hydrocarbons comprising C2 and higher, unsaturated C2 components and aromatic hydrocarbons in the range of 1 to 10 vol % is provided. The feed gas mixture is contacted with a fluidized bed catalyst having catalyst particles having a catalytic active component selected from the group consisting of a metal, a metal compound and combinations thereof. The contacting occurs at an elevated temperature in the range of 250 to 450° C., a feed gas pressure in the range of 0.8 to 70 bar, a gas hourly space velocity of 1000 to 50000 h−1, and a concentration of H2/CO in the gas mixture in the range of 0.25 to 5.
    • 在从进料气体混合物合成生成甲烷的方法中,包括一氧化碳,氢气,水蒸气,CO 2的进料气体混合物,包含C 2 H 2的挥发性烃, 并且提供更高的不饱和C 2 H 2成分和1至10体积%范围内的芳族烃。 进料气体混合物与具有催化剂颗粒的流化床催化剂接触,催化剂颗粒具有选自金属,金属化合物及其组合的催化活性组分。 接触在250至450℃的升高的温度,0.8至70巴的进料气体压力,1000至50000小时-1的气时空速下进行。 ,气体混合物中的H 2 H 2 / CO浓度在0.25〜5的范围内。
    • 10. 发明授权
    • Process for the synthetic production of ozone by electrolysis and use
thereof
    • 通过电解合成生产臭氧的方法及其用途
    • US4416747A
    • 1983-11-22
    • US373107
    • 1982-04-29
    • Anton MenthSamuel Stucki
    • Anton MenthSamuel Stucki
    • C01B13/10C02F1/461C02F1/467C02F1/78C25B1/13C25B1/02
    • C25B1/13C01B13/10C02F1/4672C02F1/78C02F2001/46128C02F2001/46133C02F2001/46152C02F2201/46115C02F2201/782
    • Electrolytic production of ozone by a process wherein an oxygen-saturated mixture of water and oxygen, or air, is led along both sides of a solid electrolyte (1), which acts as an ion-exchange membrane and carries coatings (2,3) of electrically conductive materials, both on the cathode side and on the anode side, ozone being evolved, in addition to oxygen, on the anode side and, on the cathode side, the evolution of hydrogen being suppressed by the depolarizing effect of the oxygen which is entrained in the water stream, and merely water being formed. The electrolysis is carried out under an increased pressure.Individual electrolysis cell bounded by bipolar plates (6), and comprising a solid electrolyte (1), provided, in each case, with a surface coating (2,3), and centrally located between current-collectors (4) and adjoining open metallic structures (5). A plurality of individual cells integrated together between end plates (7), electrically connected in series and hydrodynamically connected in parallel, combined to form a block.Use in water-treatment, and as a component of chemical processes (oxidation processes).
    • 通过其中氧和氧的氧饱和的混合物或空气的氧饱和的电解生产通过用作离子交换膜并承载涂层(2,3)的固体电解质(1)的两侧引导, 的导电材料,在阴极侧和阳极侧,在阳极侧除了氧之外还产生臭氧,在阴极侧,通过氧的去极化效应抑制氢的释放 被夹带在水流中,仅形成水。 电解在增压下进行。 由双极板(6)界定并且包括固体电解质(1)的单个电解槽,在每种情况下都具有表面涂层(2,3),并且位于集电体(4)和邻接的开放金属 结构(5)。 在串联电连接并并联流体动力连接的端板(7)之间集成在一起的多个单个电池组合在一起形成一块。 用于水处理和作为化学过程(氧化过程)的组成部分。