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    • 1. 发明授权
    • Ammonia removal from fly ash
    • 从粉煤灰去除氨
    • US06755901B1
    • 2004-06-29
    • US09807643
    • 2001-07-16
    • Bruce W. RammeBryan C. Fisher
    • Bruce W. RammeBryan C. Fisher
    • C04B1808
    • B09B3/00B01D53/56B09B3/0083C22B7/02Y02P10/212
    • A method and apparatus for the application of beat to remove ammonia compounds from fly ask, thereby making the fly ash a marketable product is disclosed. The method includes the steps of providing an amount of fly ash wherein at least a portion of the amount of fly ash comprises particulates having ammonia compounds affixed to the particulates, and exposing the fly ash to flowing air having a temperature of at least 1,500° F. (815 ° C.) such that the fly ash is maintained in the flowing air until the fly ash reaches a temperature of at last 900° F. (482 ° C.). The apparatus (8,9) includes a source of fly ash (10) comprising particulates having ammonia compounds affixed to at least some of the fly ash particulates, a beating chamber (17) including a treatment bed comprising a floor (20) having openings a fly ash supply conduit (16) in communication with the heating chamber (17) and the source of fly ash (10) for transferring fly ash from the source of fly ash to the treatment bed of the heating chamber, a source of heated air (45), an air supply conduit (55) in communication with the source of heated of heated air (45) and the heating chamber (17) for providing a flow of heated air to the treatment bed of the beating chamber for contacting the fly ash on the treatment bed with the flow of air, a heated air conduit (27) in communication with the beating chamber (17) for transferring the flow of heated air form the heating chamber, and an ash removal conduit (31) in communication with the heating chamber (17) for transferring heated fly ash from the heating chamber.
    • 公开了一种用于从飞蝇问题中应用节拍以除去氨化合物的方法和装置,从而使飞灰成为可销售的产品。 该方法包括以下步骤:提供一定量的飞灰,其中飞灰含量的至少一部分包含附着在微粒上的氨化合物的微粒,并将飞灰暴露于温度至少为1500°F (815℃),使得飞灰保持在流动的空气中,直到飞灰达到最后900°F(482℃)的温度。 装置(8,9)包括飞灰源(10),其包括具有附着到至少一些飞灰颗粒的氨化合物的微粒,包括处理床的打浆室(17),该处理床包括具有开口 与加热室(17)和用于将飞灰从飞灰源转移到加热室的处理床的飞灰源(10)的飞灰供应管道(16),加热空气源 (45),与加热空气(45)和加热室(17)的加热源连通的空气供应管道(55),用于向打浆室的处理床提供加热空气流,用于接触飞行 处理床上的灰尘与空气流动,与打浆室(17)连通的加热空气管道(27),用于将加热空气流转移到加热室;以及灰尘去除管道(31),其与 用于传送加热的飞灰的加热室(17) 在加热室。
    • 2. 发明授权
    • Mercury removal from activated carbon and/or fly ash
    • 从活性炭和/或飞灰中除去汞
    • US07217401B2
    • 2007-05-15
    • US10717293
    • 2003-11-19
    • Bruce W. RammeTerry L. CoughlinBryna D. GoecknerBryan C. FisherJohn J. Noegel
    • Bruce W. RammeTerry L. CoughlinBryna D. GoecknerBryan C. FisherJohn J. Noegel
    • B01D47/00
    • B09B3/00B01D53/56B09B3/0083C22B7/02Y02P10/212
    • A method for reducing the amount of mercury affixed to a sorbent and/or fly ash is disclosed. The method includes the steps of providing an amount of sorbent and/or fly ash wherein at least a portion of the amount of sorbent and/or fly ash has particulates having mercury compounds affixed to the particulates; and exposing the amount of sorbent and/or fly ash to heated flowing air until mercury compounds are liberated from at least some of the particulates. Preferably, the amount of sorbent and/or fly ash is maintained in the heated flowing air until the sorbent reaches a temperature of at least 700° F. (372° C.). When the sorbent is activated carbon, it is preferred that the amount of sorbent and/or fly ash is maintained in the heated flowing air until the activated carbon reaches a temperature in the range of 700° F. (372° C.) to 1000° F. (538° C.).
    • 公开了一种减少附着在吸附剂和/或飞灰上的汞的量的方法。 该方法包括提供一定量的吸附剂和/或飞灰的步骤,其中吸附剂和/或飞灰的量的至少一部分具有附着在颗粒物上的汞化合物的微粒; 并将吸附剂和/或飞灰的量暴露于加热的流动空气中,直到汞化合物从至少一些颗粒物中释放出来。 优选地,吸附剂和/或飞灰的量保持在加热的流动空气中,直到吸附剂达到至少700°F(372℃)的温度。 当吸附剂是活性炭时,优选吸附剂和/或飞灰的量保持在加热的流动空气中,直到活性炭达到700°F(372℃)至1000 °F(538℃)。
    • 3. 发明授权
    • Ammonia removal from fly ash
    • 从粉煤灰去除氨
    • US06945179B2
    • 2005-09-20
    • US10442030
    • 2003-05-20
    • Bruce W. RammeBryan C. Fisher
    • Bruce W. RammeBryan C. Fisher
    • F23J1/00B01D53/56B09B3/00C04B18/08C22B7/02F23N5/00
    • B09B3/00B01D53/56B09B3/0083C22B7/02Y02P10/212
    • An apparatus for the application of heat to remove ammonia compounds from fly ash is disclosed. The apparatus includes a source of fly ash comprising particulates having ammonia compounds affixed to the fly ash particulates, a heating chamber including a treatment bed comprising a media having openings, a fly ash supply conduit for transferring fly ash from the source of fly ash to the treatment bed of the heating chamber, a source of heated air, an air supply conduit for providing a flow of heated air to the treatment bed of the heating chamber for contacting the fly ash on the treatment bed with the flow of heated air, a heated air conduit in communication with the heating chamber for transferring the flow of heated air from the heating chamber, and an ash removal conduit in communication with the heating chamber for transferring heated fly ash from the heating chamber.
    • 公开了一种用于从飞灰中除去氨化合物的热量的装置。 该装置包括飞灰源,其包含附着在飞灰颗粒上的氨化合物的微粒,加热室,其包括具有开口的介质的处理床,用于将飞灰从飞灰源转移到 加热室的处理床,加热空气源,用于向加热室的处理床提供加热空气流的空气供应管道,用于使处理床上的飞灰与热空气流接触,加热的 与加热室连通的空气管道,用于将来自加热室的加热空气流传送,以及与加热室连通的除灰管道,用于从加热室输送加热的飞灰。
    • 10. 发明授权
    • Coal combustion products recovery process
    • 煤燃烧产物回收过程
    • US06637354B2
    • 2003-10-28
    • US09979480
    • 2002-02-28
    • Bruce W. Ramme
    • Bruce W. Ramme
    • F23B700
    • F23C1/00F23G2204/101F23G2206/201F23G2209/30F23K1/00F23K3/02F23K2201/501Y02E20/363
    • A process for recovering the byproducts of a process that burns coal and for reusing the byproducts is disclosed. The process includes the steps of identifying a disposal site that contains the byproducts (typically flyash and bottom ash), removing at least a portion of the byproducts from the disposal site, analyzing a sample of the portion of the byproducts to determine the loss on ignition of the portion of the byproducts, introducing the portion of the byproducts along with pulverized coal into a pulverized coal furnace if the portion of byproducts have a loss on ignition greater than or equal to a predetermined loss on ignition value (typically greater than or equal to 1 to 5%), and burning the portion of the byproducts in the furnace with the pulverized coal to render the byproducts into a commercially valuable fly ash and bottom ash having very low loss on ignition, typically lower than 3%.
    • 公开了一种用于回收燃烧煤和再利用副产物的方法的副产物的方法。 该方法包括以下步骤:鉴定包含副产物(通常为飞灰和底灰)的处置场所,从处置场地除去至少一部分副产物,分析副产物部分的样品以确定点火损失 的副产物的部分,如果副产物的一部分具有大于或等于预定的点燃值损失(通常大于或等于),将副产物的一部分与粉煤一起引入粉煤炉中 1%至5%),并用粉煤燃烧炉内副产物的一部分,使副产物成为具有极低损耗损耗(通常低于3%)的商业上有价值的飞灰和底灰。