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    • 62. 发明授权
    • Gas purification
    • 气体净化
    • US3966876A
    • 1976-06-29
    • US425715
    • 1973-12-18
    • Frank Henry SingletonDerek Vernon GosdenGraham Woodhouse
    • Frank Henry SingletonDerek Vernon GosdenGraham Woodhouse
    • B01D53/52C01B17/05C01B17/04
    • B01D53/52C01B17/05
    • Gas purification processes for removing hydrogen sulphide (H.sub.2 S) from a foul gas stream, such as coal carbonization gases, involving a circulating liquid reagent in which the H.sub.2 S is absorbed and converted to sulphur which is recovered and the reagent regenerated and recycled exhibit progressive deterioration of the circulating reagent due to contamination by process by-products. The invention provides a method of decontaminating such a circulating reagent by subjecting a bled-off sidestream to high temperature hydrolysis, so producing gaseous products recyclable to the foul gas stream. Solid products may also be produced which may be recycled to the reagent, perhaps after high-temperature reduction.
    • 用于从恶臭气流(例如煤碳化气体)中除去硫化氢(H2S)的气体净化方法,其涉及循环液体试剂,其中H 2 S被吸收并转化成硫并被回收并且再生和再循环的试剂表现出逐渐恶化 循环试剂由于过程副产物污染。 本发明提供了一种通过使排出侧流进行高温水解来净化这种循环试剂的方法,从而产生可回收到恶臭气流的气态产物。 还可以生产固体产物,其可以在高温还原后再循环到试剂中。
    • 66. 发明授权
    • Removal and recovery of sulfur from a gas stream containing hydrogen sulfide
    • 从含有硫化氢的气体流中除去和回收硫
    • US3728441A
    • 1973-04-17
    • US3728441D
    • 1971-07-19
    • UNIVERSAL OIL PROD CO
    • HAMBLIN R
    • C01B17/05C01B17/04
    • C01B17/05
    • H2S is removed from a gas stream and sulfur is produced by the steps of: (1) sequentially scrubbing the gas stream with a first recycle water stream containing NH4OH and then with a second recycle water stream which is sbustantially free of NH4OH to produce a treated gas stream which is reduced in H2S content and is substantially free of NH3 and a bottom water stream containing NH4HS; (2) catalytically treating the bottom water stream with an air stream to produce an effluent stream containing ammonium polysulfide; (3) treating the ammonium polysulfide-containing stream to recover sulfur and to produce a water stream which is substantially free of NH4OH and a water stream containing NH4OH; and, (4) separately recycling at least a portion of these last two streams to the scrubbing step.
    • 从气流中除去H 2 S,并通过以下步骤产生硫:(1)用含有NH 4 OH的第一再循环水流,然后用第二再循环水流顺次地洗涤气流,所述第二循环水流是非常不含NH 4 OH以产生处理过的 气流中H2S含量降低且基本上不含NH 3和含有NH 4 HS的底部水流; (2)用空气流催化处理底部水流以产生含有多硫化铵的流出物流; (3)处理含多硫化铵的料流以回收硫并产生基本上不含NH 4 OH的水流和含有NH 4 OH的水流; 和(4)将这两个最后两个流的至少一部分分别回收到洗涤步骤。
    • 67. 发明授权
    • Process for treating two gas streams
    • 处理两个气体流的过程
    • US3672837A
    • 1972-06-27
    • US3672837D
    • 1970-10-01
    • UNIVERSAL OIL PROD CO
    • URBAN PETER
    • B01D53/52C01B17/05C01B17/14
    • C01B17/05B01D53/52
    • A FIRST GAS STREAM CONTAINING H2S AND A SECOND GAS STREAM CONTAINING SO2 ARE SIMULTANEOUSLY TREATED IN ORDER TO REMOVE SO2 AND H2S FROM THE RESPECTIVE STREAMS AND TO PRODUCE ELEMENTAL SULFUR BY THE STEPS OF: (A) SCRUBBING THE FIRST GAS STREAM WITH AN AQUEOUS SCRUBBING SOLUTION TO PRODUCE AN EFFLUENT STREAM CONTAINING A WATER-SOLUBLE SULFIDE COMPOUND; (B) CONTACTING THE SECOND GAS STREAM WITH AN AQUEOUS SCRUBBING SOLUTION AND WITH A REDUCNG AGENT AT REACTION CONDITIONS SELECTED TO RESULT IN AN EFFLUENT STREAM CONTAINING A WATER-SOLUBLE THIOSULFATE COMPOUND; (C) SUBJECTING A MIXTURE OF THE EFFLUENT STREAMS FROM STEP (A) AND (B) TO REDUCTION CONDITIONS SELECTED TO RESULT IN AN EFFLUENT STREAM CONTAINING A POLYSULFIDE COMPOUND; (D) DECOMPOSING THE RESULTING POLYSULFIDE COMPOUND TO FORM ELEMENTAL SULFUR, HYDROGEN SULFIDE, AND A REGENERATED SCRUBBING SOLUTION; (E) PASSING THE RESULTING HYDROGEN SULFIDE TO STEP (A); AND (F) RECIRCULATING THE REGENERATED SCRUBBING SOLUTION TO STEPS (A) AND (B).
    • 68. 发明授权
    • Treatment of an aqueous stream containing water-soluble inorganic sulfide compounds
    • 含有水溶性无机硫化合物的水溶液处理
    • US3672836A
    • 1972-06-27
    • US3672836D
    • 1970-12-21
    • UNIVERSAL OIL PROD CO
    • BROWN KENNETH M
    • C01B17/05C02F1/72C02F11/08C01B17/06
    • C02F11/08C01B17/05C02F1/725
    • AN AQUEOUS STREAM CONTAINING A WATER-SOLUBLE, INORGANIC SULFIDE COMPOUND IS TREATED BY CONTACTNG THE AQUEOUS STREAM AND OXYGEN, IN AN AMOUNT SELECTED TO REACT LESS THAN 0.5 MOLE OF O2 PER MOLE OF SULFIDE COMPOUND, WITH A FIRST OXIDIZING CATALYST AT OXIDIZING CONDITIONS, INCLUDING A RELATIVELY LOW PRESSURE AND TEMPERATURE, SELECTED TO FORM AN EFFLUENT STREAM CONTAINING A WATER-SOLUBLE POLYSULFIDE; AND THEREAFTER BY CONTACTING THE POLYSULFIDE-CONTAINING EFFLUENT STREAM AND OXYGEN IN AN AMOUNT LESS THAN THE AMOUNT UTILIZED IN THE FIRST STEP, WITH A SECOND OXIDIZING CATALYST AT OXIDIZING CONDITIONS, INCLUDING A TEMPERATURE GREATER THAN OR EQUAL TO THE MELTING POINT OF SULFUR AND A PRESSURE SUFFICIENT TO MAINTAIN AT LEAST A PORTIN OF THE EFFLUENT STREAM IN THE LIQUID PHASE, SELECTED TO PRODUCE LIQUID SULFUR AND A SUBSTANTIALLY SULFIDE-FREE TREATED WATER STREAM. KEY FEATURES OF THE DISCLOSED METHOD INVOLVE THE USE OF A FIRST CATALYTIC OXIDATION STEP WHICH IS RUN AT RELATIVELY LOW TEMPERATURES AND PRESSURES TO PRODUCE POLYSULFIDE, COUPLED WITH A SECOND CATALYTIC OXIDATION STEP WHICH IS RUN AT RELATIVELY HIGH TEMPERATURES AND PRESSURES TO SELECTIVELY OXIDIZE THE POLYSULFIDE TO ELEMENTAL SULFUR, THEREBY PREVENTING THE DEPOSITION OF ELEMENTAL SULFUR ON THE CATALYST USED DURING THESE OXIDATION STEPS, WHILE SIMULTANEOUSLY MINIMIZING THE AMOUNT OF OXYGEN WHICH MUST BE SUPPLIED AT THE RELATIVELY HIGH PRESSURES.