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    • 2. 发明申请
    • PROCESS AND FACILITY FOR REMOVING METAL CONTAMINANTS FROM FERTILIZER STREAMS
    • 从肥料流中除去金属污染物的工艺和设备
    • WO2003045535A1
    • 2003-06-05
    • PCT/US2002/038100
    • 2002-11-26
    • MARSULEX ENVIRONMENTAL TECHNOLOGIES, CORP
    • GANSLEY, Raymond, R.HAMMER, Michael, T.MENGEL, Michael, L.
    • B01D53/00
    • C05G3/0064B01D53/502C01C1/24C05C3/00
    • A process and system for producing fertilizers with reduced levels of contaminants, and particularly a flue gas scrubbing process and facility that produce a fertilizer byproduct which is treated to remove heavy metals originally present in the scrubbed flue gas. The process entails contacting a flue gas with a scrubbing solution to remove acidic gases and produce a byproduct containing a fertilizer compound precipitate and dissolved metals and/or metal compounds. A fertilizer solution containing dissolved fertilizer and dissolved metals and/or metal compounds is then produced by adding water to the byproduct, after which the pH of the fertilizer solution is adjusted one or more times with a gaseous and/or liquid alkali to form precipitates of one or more metal species. The precipitates are then removed from the fertilizer solution and the solution dewatered to yield a fertilizer product with lower contaminant levels.
    • 一种用于生产具有降低的污染物水平的肥料的方法和系统,特别是烟道气洗涤过程和设施,其产生肥料副产物,其被处理以除去最初存在于洗涤烟道气中的重金属。 该方法需要使烟气与洗涤溶液接触以除去酸性气体并产生含有肥料化合物沉淀物和溶解的金属和/或金属化合物的副产物。 然后通过向副产物中加入水来生产含有溶解的肥料和溶解的金属和/或金属化合物的肥料溶液,之后用气态和/或液态碱调节肥料溶液的pH一次或多次以形成沉淀物 一种或多种金属物种。 然后从肥料溶液中除去沉淀物,并将溶液脱水以产生具有较低污染物水平的肥料产品。
    • 3. 发明申请
    • FLUE GAS SCRUBBING APPARATUS AND PROCESS
    • 燃气清洗装置和工艺
    • WO2010065812A2
    • 2010-06-10
    • PCT/US2009/066699
    • 2009-12-04
    • MARSULEX ENVIRONMENTAL TECHNOLOGIES, CORPMURPHY, David William
    • MURPHY, David William
    • B01D53/78B01D53/50F23J15/04C01B17/00
    • B01D53/78B01D53/40B01D53/502B01D2251/102B01D2251/11B01D2251/206B01D2251/2062B01D2257/2045B01D2257/2047
    • An apparatus (10) and process for removing acidic gases from flue gases produced by, for example, utility and industrial facilities. The acidic gases are removed as the flue gas flows upward through a contact zone (16) within a passage (13), where the flue gas is contacted with an ammonium sulfate-containing scrubbing solution to absorb the acidic gases from the flue gas. The scrubbing solution and absorbed acidic gases therein are then accumulated, and ammonia and an oxygen-containing gas are injected into the accumulated scrubbing solution to react the absorbed acidic gases and produce ammonium sulfate. An acid solution (32) is flowed across the passage (13) above the contact zone (16) of the passage (13). The scrubbed flue gas is flowed upward through the acid solution (32) to remove unreacted ammonia from the scrubbed flue gas. The acid solution (32) is then removed from the passage (13) after the acid solution (32) has been contacted by the scrubbed flue gas.
    • 一种设备(10)和用于从例如公用事业和工业设施产生的烟道气中除去酸性气体的方法。 当烟道气向上流过通道(13)内的接触区(16)时,酸性气体被去除,其中烟道气与含硫酸铵的洗涤溶液接触以吸收来自烟道气的酸性气体。 然后将洗涤溶液和其中吸收的酸性气体累积,并将氨和含氧气体注入累积的洗涤溶液中以使吸收的酸性气体反应并产生硫酸铵。 酸溶液(32)流过通道(13)的接触区(16)上方的通道(13)。 经洗涤的烟气向上流过酸性溶液(32)以从洗涤的烟道气中除去未反应的氨。 然后在酸溶液(32)已被洗涤的烟气接触之后,从通道(13)中除去酸溶液(32)。
    • 4. 发明申请
    • FLUE GAS DESULFURIZATION PROCESS AND APPARATUS FOR REMOVING NITROGEN OXIDES
    • 氟气脱硫工艺及去除氮氧化物的设备
    • WO2003103803A2
    • 2003-12-18
    • PCT/US2003/017854
    • 2003-06-05
    • MARSULEX ENVIRONMENTAL TECHNOLOGIES, CORP.
    • HAMMER, Michael, T.MENGEL, Michael, L.
    • B01D53/00
    • B01D53/56B01D53/1456B01D53/73C01C1/185C01C1/242
    • An apparatus (10) and process for removing acidic gases and NOx from flue gases produced by utility and industrial plants. The process and apparatus (10) convert NOx, and particularly nitric oxide, to nitrogen dioxide, which is then reacted to form a valuable byproduct. The process generally entails contacting a flue gas with a scrubbing medium (14) to absorb acidic gases from flue gas and produce an intermediate flue gas. The intermediate flue gas is then cooled to cause nitric oxide present therein to be oxidized to form nitrogen dioxide, which is then absorbed from the flue gases to produce a nitrogen dioxide-containing solution (36) and a scrubbed flue gas. The nitrogen dioxide in the nitrogen dioxide-containing solution (36) is then reacted with ammonium hydroxide to form ammonium nitrate as a valuable byproduct.
    • 一种用于从公用事业和工厂生产的烟道气中除去酸性气体和NOx的装置(10)。 方法和装置(10)将NOx(特别是一氧化氮)转化为二氧化氮,然后将其反应以形成有价值的副产物。 该方法通常需要使烟气与洗涤介质(14)接触以吸收来自烟道气的酸性气体并产生中间烟道气。 然后将中间烟道气冷却以使其中存在的一氧化氮被氧化以形成二氧化氮,然后从烟道气中吸收二氧化氮,以产生含二氧化氮的溶液(36)和洗涤的废气。 然后将含二氧化氮的溶液(36)中的二氧化氮与氢氧化铵反应,形成硝酸铵作为有价值的副产物。
    • 5. 发明申请
    • PROCESS AND SYSTEM FOR REMOVING SULFUR DIOXIDE FROM FLUE GAS
    • 从烟气中去除二氧化硫的方法和系统
    • WO2017074347A1
    • 2017-05-04
    • PCT/US2015/057796
    • 2015-10-28
    • MARSULEX ENVIRONMENTAL TECHNOLOGIES, CORP
    • GAL, Eli
    • B01D53/14B01D53/50
    • B01D53/502B01D53/73B01D53/78B01D2251/108B01D2251/206B01D2258/0283C01D5/08
    • Processes and systems (10,110) for producing potassium sulfate (36) as a byproduct of a desulfurization process. Sulfur dioxide is absorbed (12) from a flue gas (14) using an ammonia-containing solution to produce an ammonium sulfate solution (24) that contains dissolved ammonium sulfate. At least a first portion (25) of the ammonium sulfate solution (24) is heated (26) before dissolving potassium chloride (22) therein to form a slurry (28) that contains potassium sulfate crystals (36) and an ammonium chloride solution. The slurry (28) is then cooled (32) to precipitate additional potassium sulfate crystals (36), after which the potassium sulfate crystals (36) are removed (34) to yield a residual ammonium chloride solution (38,48) that contains dissolved ammonium chloride and residual dissolved potassium sulfate. Ammonia (50) is then absorbed (40) into the residual ammonium chloride solution (38) to further precipitate potassium sulfate crystals (42), which are removed (44) to yield a residual ammonium chloride solution (46) that is substantially free of dissolved potassium sulfate.
    • 用于生产硫酸钾(36)作为脱硫工艺的副产物的方法和系统(10,110)。 使用含氨溶液从烟道气(14)吸收二氧化硫(12)以产生含有溶解的硫酸铵的硫酸铵溶液(24)。 在将氯化钾(22)溶解于其中之前,将硫酸铵溶液(24)的至少第一部分(25)加热(26)以形成含有硫酸钾晶体(36)和氯化铵溶液的浆液(28)。 然后将浆液(28)冷却(32)以沉淀另外的硫酸钾晶体(36),然后除去硫酸钾晶体(36)(34)以产生残余的氯化铵溶液(38,48) 氯化铵和残留溶解的硫酸钾。 然后将氨(50)吸收(40)到残留的氯化铵溶液(38)中以进一步沉淀硫酸钾晶体(42),将其除去(44)以产生基本上不含 溶解的硫酸钾。
    • 6. 发明申请
    • CIRCULATING DRY SCRUBBER SYSTEM AND METHOD
    • 循环干燥系统和方法
    • WO2015051360A1
    • 2015-04-09
    • PCT/US2014/059271
    • 2014-10-06
    • MARSULEX ENVIRONMENTAL TECHNOLOGIES, CORP
    • HENDRICKSEN, Rodney Alan
    • B01D53/02B01D46/00
    • B01D53/40B01D46/02B01D53/508B01D53/685B01D53/83B01D2251/404B01D2251/604B01D2257/2045B01D2257/2047B01D2257/302B01D2258/0283F23J15/025
    • A system and method suitable for the removal of pollutants from gases with a circulating dry scrubber system (12) having a circulating dry scrubber reactor (14) containing a fluidized bed adapted to contact the gas with a dry reagent within the fluidized bed. The system includes a housing (25) fluidically coupled to the reactor (14), a filter array (29) within the housing (25), and an internal hopper (28) within the housing (25) and adapted to return at least some of the particulates to the fluidized bed within the circulating dry scrubber reactor (14). The scrubbed gas stream exits the circulating dry scrubber reactor (14) and flows upward between an interior (26) of the housing (25) and an exterior of the internal hopper (28) before contacting the filter array (29). The exterior of the internal hopper (28) is exposed to the scrubbed gas stream, and the scrubbed gas stream is not recirculated to the circulating dry scrubber reactor (14) to maintain the fluidized bed therein.
    • 一种适用于用循环干洗涤器系统(12)除去气体污染物的系统和方法,该循环干洗涤器系统(12)具有循环的干式洗涤器反应器(14),该反应器含有流化床,该流化床适于使该气体与流化床内的干试剂接触。 该系统包括流体耦合到反应器(14)的壳体(25),壳体(25)内的过滤器阵列(29)和壳体(25)内的内部料斗(28),并且适于使至少一些 的颗粒流入循环干洗涤器反应器(14)内的流化床。 经过洗涤的气流离开循环的干洗涤器反应器(14),并在接触过滤器阵列(29)之前在壳体(25)的内部(26)和内部料斗(28)的外部之间向上流动。 内部料斗(28)的外部暴露于洗涤的气体流中,并且洗涤的气体流不再循环到循环的干式洗涤器反应器(14)以将流化床保持在其中。