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    • 1. 发明授权
    • Method of operating a Claus-plant
    • 操作装置的方法
    • US5100640A
    • 1992-03-31
    • US635473
    • 1990-12-28
    • Rainer DittmerManfred GrossUlrich Meisl
    • Rainer DittmerManfred GrossUlrich Meisl
    • C01B17/04
    • C01B17/0421C01B17/0404Y02P20/129
    • The method of performing the Claus process includes the steps of connecting in parallel two combustion furnaces with waste heat boilers, further reacting, after the partial combusting in the combusion furnaces, in a single Claus reactor which is connected to both of the waste heat boilers of the combustion furnaces so as to receive partially combusted gas from the combustion furnaces, and partially combusting the reactant gas in only one of the combustion furnaces, when a hydrogen sulfide mass flow rate of the hydrogen sulfide fed with the reactant gas is below a certain threshold, and partially combusting of the reactant gas in both of the combustion furnaces, when the hydrogen sulfide mass flow rate of the hydrogen sulfide is greater than the threshold value. The production capacity of the single Claus reactor is designed for a maximum expected hydrogen sulfide mass flow rate in the inflowing reactant gas. The fluctuations or variations of the hydrogen sulfide mass flow rates in the reactant gas can be handles, while minimizing investment and operating costs. Savings of 10 to 15% inoperating and investment costs can result from using this Claus-plant operating process.
    • 执行克劳斯方法的方法包括以下步骤:将两个燃烧炉与废热锅炉并联连接,在混合炉中部分燃烧之后,在单个克劳斯反应器中进一步反应,该克劳斯反应器连接到两个废热锅炉 所述燃烧炉从所述燃烧炉接收部分燃烧的气体,并且当所述反应气体供给的所述硫化氢的硫化氢质量流量低于某一阈值时,在仅一个所述燃烧炉中部分燃烧所述反应气体 ,并且当硫化氢的硫化氢质量流量大于阈值时,在两个燃烧炉中部分地燃烧反应气体。 单个克劳斯反应器的生产能力设计用于流入反应气体中最大预期的硫化氢质量流量。 反应气体中硫化氢质量流量的波动或变化可以是手柄,同时最小化投资和运行成本。 节省10至15%的运营成本和投资成本可能是由于使用这个Claus工厂的运营过程。
    • 2. 发明授权
    • Process for the elimination of waste water produced upon the
desulfurization of coking oven gas by means of wash solution containing
organic oxygen-carrier, with simultaneous recovery of elemental sulfur
    • 通过含有机氧载体的洗涤溶液消除焦化炉气体脱硫产生的废水的方法,同时回收元素硫
    • US4511549A
    • 1985-04-16
    • US396691
    • 1982-07-09
    • Peter DiemerWerner BrakeRainer Dittmer
    • Peter DiemerWerner BrakeRainer Dittmer
    • B01D53/52C01B17/05C02F11/10
    • B01D53/52C01B17/05C02F11/10Y02P20/129Y02W10/40Y10S210/909
    • A process is disclosed for the elimination of waste water falling out with the desulfurization of coking oven gas by means of an organic oxygen carrier--containing washing solution with simultaneous recovery of elemental sulfur. The waste water is decomposed in a combustion chamber in a reducing atmosphere at temperatures between about 1000.degree. and 1100.degree. C. under such conditions that the mole ratio of H.sub.2 S:SO.sub.2 in the exhaust gas of the combustion chamber amounts to at least 2:1. Sulfur falling out is separated and the sensible heat of the exhaust gas is utilized for steam generation. The cooled and desulfurized exhaust gas is added to the coking oven gas before the pre-cooling. Sulfur falling out from the washing solution in the oxidizer is separated out and lead into the combustion chamber together with the part of the washing solution discharged as waste water from the washing solution circulation. Preferred embodiments include that the sulfur loading of the waste water can amount to up to about 370 kg sulfur per m.sup.3 waste water; having the cooling of sulfur--containing exhaust gas leaving the combustion chamber follow in a waste heat boiler and a sulfur condenser heated by pre-heated boiler feed water, from which condenser sulfur is discharged in liquid state.
    • 公开了一种通过具有同时回收元素硫的含有机氧载体的洗涤溶液消除利用焦化炉气体脱硫而排出的废水的方法。 废水在约1000〜1100℃的还原气氛中的燃烧室中分解,在燃烧室排气中的H 2 S:SO 2的摩尔比为至少2:1 。 脱落的硫分离,排气的显热用于蒸汽发生。 冷却和脱硫废气在预冷之前被加到焦化炉气中。 从氧化剂中的洗涤溶液中流出的硫分离出来,并与作为洗涤液循环的废水排出的洗涤溶液的一部分一起导入燃烧室。 优选的实施方案包括废水的硫负荷可以达到每立方米废水高达约370kg硫; 离开燃烧室的含硫废气的冷却遵循废热锅炉和通过预热的锅炉给水加热的硫冷凝器,冷凝器硫从该热水锅炉供给水以液态排出。