Recovery of sulphur
    1.
    发明授权
    Recovery of sulphur 失效
    恢复硫磺

    公开(公告)号:US3781445A

    公开(公告)日:1973-12-25

    申请号:US3781445D

    申请日:1971-12-10

    Inventor: MOSS G ROSBOROUGH D

    CPC classification number: B01D53/8615 C01B17/0413

    Abstract: TAIL GAS FROM A CLAUS UNIT IS CONTACTED WITH A BED OF FLUIDIZED SULPHUR REACTIVE MATERIAL SUCH AS LIME UNDER OXI DIZING CONDITIONS IN AN ABSORBER MIN ORDER TO REMOVE SULFUR COMPOUNDS THEREIN. ESSENTIALLY SULPHUR-FREE GAS IS DISCHARGED FROM THE ABSORBER. ABSORBER BED MATERIAL CONTAINING SULFATE (E.G., CASO4) IS TRANSFERRED TO A REGENERATOR WHERE THE CORRESPONDING OXIDE (E.G., CAO) IS REGENERATED UNDER REDUCING CONDITIONS.

    Reduction of sulphur oxides
    3.
    发明授权
    Reduction of sulphur oxides 失效
    减少硫氧化物

    公开(公告)号:US3810972A

    公开(公告)日:1974-05-14

    申请号:US22882972

    申请日:1972-02-24

    Inventor: HUMPHREY R MOSS G

    CPC classification number: C01B17/0482 B01D53/508

    Abstract: A SUBSTRATE IS COKED BY CONTACT WITH OIL AT CRACKING TEMPERATURE, AND THE COKED SUBSTRATE IS THEN CONTACTED WITH SULPHUR OXIDES-CONTAINING GASES TO REDUCE THE SULPHUR OXIDES TO SULPHUR (WHICH IS RECOVERED) AND TO OXIDIZE COKE TO CARBON OXIDES. THE CRACKED OIL VAPORS ARE ALSO RECOVERED. THE PROCESS IS OPERATED EITHER CYCLICALLY. INTERMITTTENLY OR CONTINOUSLY.

    Purifications of fuels
    4.
    发明授权
    Purifications of fuels 失效
    燃料净化

    公开(公告)号:US3807090A

    公开(公告)日:1974-04-30

    申请号:US31271872

    申请日:1972-12-06

    Inventor: MOSS G

    CPC classification number: F23C10/005 B01D53/48 C10G25/09 C10K1/20 Y10T436/186

    Abstract: Fuels containing sulphur are purified by (a) partial combustion or (b) full combustion, at 800*-950*C in a bed of CaO and/or MgO which combines with the sulphur. The sulphurized CaO or MgO is reactivated by contact with a regenerator gas at 1,000*-1,150*C with the evolution of SO2. Vanadium and sodium removal from the fuel is enhanced by the presence of iron and alumina, respectively.

    Abstract translation: 含硫的燃料通过(a)部分燃烧或(b)完全燃烧在800-950℃在与硫结合的CaO和/或MgO的床中纯化。 硫化CaO或MgO通过与1,000-2-150℃的再生气体的接触与SO2的释放而再活化。 分别通过铁和氧化铝的存在来提高从燃料中除去的钒和钠。

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