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    • 4. 发明申请
    • REDUCING CARBON DIOXIDE TO PRODUCTS
    • 减少二氧化碳产品
    • WO2013134418A1
    • 2013-09-12
    • PCT/US2013/029425
    • 2013-03-06
    • LIQUID LIGHT, INC.
    • COLE, Emily, BartonSIVASANKAR, NarayanappaPARAJULI, RishiKEETS, Kate A.KEYSHAR, Kunttal
    • C25B3/04
    • C25B3/04C25B1/00C25B1/003
    • A method reducing carbon dioxide to one or more products may include steps (A) to (C). Step (A) may bubble said carbon dioxide into a solution of an electrolyte and a catalyst in a divided electrochemical cell. The divided electrochemical cell may include an anode in a first cell compartment and a cathode in a second cell compartment. The cathode may reduce said carbon dioxide into said products. Step (B) may adjust one or more of (a) a cathode material, (b) a surface morphology of said cathode, (c) said electrolyte, (d) a manner in which said carbon dioxide is bubbled, (e), a pH level of said solution, and (f) an electrical potential of said divided electrochemical cell, to vary at least one of (i) which of said products is produced and (ii) a faradaic yield of said products. Step (C) may separate said products from said solution.
    • 将二氧化碳还原成一种或多种产品的方法可包括步骤(A)至(C)。 步骤(A)可以将分散的电化学电池中的二氧化碳气泡化成电解质和催化剂的溶液。 分隔的电化学电池可以包括第一电池室中的阳极和第二电池室中的阴极。 阴极可以将所述二氧化碳减少到所述产品中。 步骤(B)可以调节(a)阴极材料,(b)所述阴极的表面形态,(c)所述电解质,(d)所述二氧化碳鼓泡的方式中的一种或多种,​​(e) 所述溶液的pH值,和(f)所述分隔电化学电池的电位,以改变(i)产生哪种产物和(ii)所述产品的法拉利产率中的至少一种。 步骤(C)可以将所述产物与所述溶液分开。
    • 10. 发明申请
    • MULTIPHASE ELECTROCHEMICAL REDUCTION OF CO2
    • 多相电化学还原二氧化碳
    • WO2014042783A1
    • 2014-03-20
    • PCT/US2013/053560
    • 2013-08-05
    • LIQUID LIGHT, INC.
    • SIVASANKAR, NarayanappaKACZUR, Jerry, J.COLE, Emily, Barton
    • C25B3/00
    • C25B3/04C25B1/24C25B9/06C25B9/08C25B13/02C25B13/04
    • Disclosed is a system and method for reducing carbon dioxide into a carbon based product. The system includes an electrochemical cell having a cathode region which includes a cathode and a non-aqueous catholyte; an anode region having an anode and an aqueous or gaseous anolyte; and an ion permeable zone disposed between the anode region and the cathode region. The ion permeable zone is at least one of (i) the interface between the anolyte and the catholyte, (ii) an ion selective membrane; (iii) at least one liquid layer formed of an emulsion or (iv) a hydrophobic or glass fiber separator. The system and method includes a source of energy, whereby applying the source of energy across the anode and cathode reduces the carbon dioxide and produces an oxidation product.
    • 公开了将二氧化碳还原成碳基产品的系统和方法。 该系统包括具有阴极区域的电化学电池,阴极区域包括阴极和非水性阴极电解液; 具有阳极和水性或气态阳极电解液的阳极区域; 以及设置在阳极区域和阴极区域之间的离子渗透区域。 离子渗透区域是(i)阳极电解液和阴极电解液之间的界面中的至少一种,(ii)离子选择性膜; (iii)由乳液形成的至少一个液体层或(iv)疏水或玻璃纤维分离器。 该系统和方法包括能量源,其中通过阳极和阴极施加能量源来减少二氧化碳并产生氧化产物。