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    • 5. 发明申请
    • METHOD FOR PRODUCTION OF SULFUR
    • WO2020089099A1
    • 2020-05-07
    • PCT/EP2019/079233
    • 2019-10-25
    • HALDOR TOPSØE A/S
    • THELLEFSEN, MortenBRORHOLT, Lars PiilmannSØRENSEN, Per AggerholmLYKKE, Mads
    • C01B17/04B01D53/86B01J20/06
    • The present invention relates to process plant comprising a Claus reaction furnace, a Claus waste heat boiler, a SO 3 destruction section and a Claus conversion section, wherein the Claus reaction furnace has an inlet and an outlet, the Claus waste heat boiler has a gas inlet, a gas outlet and optional an elemental sulfur outlet, the SO 3 destruction section has a gas inlet and a gas outlet and the Claus conversion section has a gas inlet, a gas outlet and an elemental sulfur outlet, and wherein the inlet of the Claus reaction furnace is configured for receiving a feedstock gas, sulfuric acid, fuel, an oxidant and an optional sulfuric acid atomization media, and the outlet of the Claus reaction furnace is configured for being in fluid communication with the inlet of the Claus waste heat boiler, wherein the outlet of the Claus waste heat boiler is configured for being in fluid communication with the inlet of the SO 3 destruction section, wherein the outlet of the SO 3 destruction section is in fluid communication with the inlet of the Claus conversion section. The process has the associated benefit of such a process avoiding undesired poisoning (sulfation) of Claus catalyst and contamination of elemental sulfur product with sulfuric acid in the Claus conversion section.
    • 9. 发明申请
    • A SYSTEM AND METHOD FOR DECOMPOSING GASEOUS HYDROGEN SULFIDE INTO HYDROGEN GAS AND ELEMENTARY SULFUR
    • WO2019035789A1
    • 2019-02-21
    • PCT/TR2017/050724
    • 2017-12-29
    • TURKIYE PETROL RAFINERILERI ANONIM SIRKETI TUPRAS
    • KARAKAYA, Cuneyt
    • C01B17/04C01B3/00C25B1/02
    • A decomposition system is developed with the present invention for decomposing gaseous hydrogen sulfide (H 2 S), this system comprising at least one pump (1) supplying H 2 S gas in the form of bubbles; an aqueous acidic phase (2a) having at least one redox couple which do not mix with each other because of density difference and thus form an interface (2c) where they contact each other; and at least one column reactor (2) comprising an organic phase (2b) with a density above the density of water and capable to dissolve elementary sulfur, wherein an oxidation reaction takes place in the interface (2c) by which the H 2 S bubbles carried into the organic phase (2b) through the pump (1) are converted into elementary sulfur; at least one cooling unit (3) which provides the crystallization of elementary sulfur to be taken out of the system; at least one photo-/electrochemical cell (5) comprising a first chamber (5A) comprising an anode electrode, a second chamber (5B) coprisingg a cathode electrode, and a membrane (5C) separating the first chamber (5A) from the second chamber (5B), and to which the aqueous acidic phase (2a) in the reactor is transferred and in which the oxidation of the redox couple and the reduction reaction of H + to H 2 take place, wherein following the reduction reaction, the aqueous acidic phase (2a) is transferred back to the column reactor (2); and an energy source (6) generating the required potential difference to be conducted to one of the electrodes for the oxidation of the redox couple and the reduction reaction of H + to H 2 .