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    • 4. 发明授权
    • Carbon dioxide remediation via oxygen-enriched combustion using dense ceramic membranes
    • 通过使用致密陶瓷膜的富氧燃烧进行二氧化碳修复
    • US06173663B1
    • 2001-01-16
    • US09336791
    • 1999-06-21
    • Uthamalingam BalachandranArun C. BoseHoward G. McIlvried
    • Uthamalingam BalachandranArun C. BoseHoward G. McIlvried
    • F23D100
    • C01B13/0251C01B21/0444C01B2210/0046F23C2202/30F23D1/00F23L7/007Y02E20/322Y02E20/344
    • A method of combusting pulverized coal by mixing the pulverized coal and an oxidant gas to provide a pulverized coal-oxidant gas mixture and contacting the pulverized coal-oxidant gas mixture with a flame sufficiently hot to combust the mixture. An oxygen-containing gas is passed in contact with a dense ceramic membrane of metal oxide material having electron conductivity and oxygen ion conductivity that is gas-impervious until the oxygen concentration on one side of the membrane is not less than about 30% by volume. An oxidant gas with an oxygen concentration of not less than about 30% by volume and a CO2 concentration of not less than about 30% by volume and pulverized coal is contacted with a flame sufficiently hot to combust the mixture to produce heat and a flue gas. One dense ceramic membrane disclosed is selected from the group consisting of materials having formulae SrCo0.8Fe0.2Ox, SrCo0.5FeOx and La0.2Sr0.8Co0.4Fe0.6Ox.
    • 通过混合粉煤和氧化剂气体来燃烧粉煤的方法,以提供粉煤氧化剂气体混合物,并将粉煤氧化剂气体混合物与足够热的火焰混合以使混合物燃烧。 使含氧气体与具有电子传导性和氧离子传导性的金属氧化物材料的致密陶瓷膜接触,其是不透气的,直到膜一侧的氧浓度不低于约30体积%。 氧浓度不小于约30体积%,不低于约30体积%的CO 2浓度的氧化剂气体和粉煤接触足够热的火焰以燃烧混合物以产生热量和烟道气 。 所公开的一种致密陶瓷膜选自具有式SrCo0.8Fe0.2Ox,SrCo0.5FeOx和La0.2Sr0.8Co0.4Fe0.6Ox的材料。
    • 7. 发明授权
    • Method to remove ammonia using a proton-conducting ceramic membrane
    • 使用质子传导陶瓷膜去除氨的方法
    • US06630116B2
    • 2003-10-07
    • US09917615
    • 2001-07-25
    • Uthamalinga BalachandranArun C. Bose
    • Uthamalinga BalachandranArun C. Bose
    • C01B304
    • B01D53/8634B01D53/228
    • An apparatus and method for decomposing NH3. A fluid containing NH3 is passed in contact with a tubular membrane that is a homogeneous mixture of a ceramic and a first metal, with the ceramic being selected from one or more of a cerate having the formula of M′Ce1-x M″3-&dgr;, zirconates having the formula M′Zr1-xM″O3-&dgr;, stannates having the formula M′Sn1-xM′O3-&dgr;, where M′ is a group IIA metal, M″ is a dopant metal of one or more of Ca, Y, Yb, In, Nd, Gd or mixtures thereof and &dgr; is a variable depending on the concentration of dopant and is in the range of from 0.001 to 0.5, the first metal is a group VIII or group IB element selected from the group consisting of Pt, Ag, Pd, Fe, Co, Cr, Mn, V, Ni, Au, Cu, Rh, Ru and mixtures thereof. The tubular membrane has a catalytic metal on the side thereof in contact with the fluid containing NH3 which is effective to cause NH3 to decompose to N2 and H2. When the H2 contacts the membrane H+ ions are formed which pass through the membrane driving the NH3 decomposition toward completion.
    • 一种用于分解NH3的装置和方法。 含有NH 3的流体与陶瓷和第一金属的均匀混合物的管状膜接触,陶瓷选自一种或多种具有式M'Ce1-x M'3的铈酸盐 具有式M'Zr1-xM'O3-δ的锆酸盐,具有式M'Sn1-xM'O3-δ的锡酸盐,其中M'是IIA族金属,M“是一种掺杂剂金属 或更多的Ca,Y,Yb,In,Nd,Gd或其混合物,并且Δ是根据掺杂剂的浓度而变化的,并且在0.001至0.5的范围内,第一金属是VIII族或1B族元素 选自Pt,Ag,Pd,Fe,Co,Cr,Mn,V,Ni,Au,Cu,Rh,Ru及其混合物。 管状膜的侧面具有与含有NH 3的流体接触的催化金属,其有效地使NH 3分解成N 2和H 2。 当H 2接触膜时,形成H +离子,其通过膜驱动NH 3分解完成。