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    • 2. 发明申请
    • OPTIMIZATION OF AMMONIA DOSING DURING REGENERATION
    • 在再生过程中优化奥米尼定量
    • US20150285124A1
    • 2015-10-08
    • US14394838
    • 2012-04-16
    • Shyam SanthanamBradley Jay Adelman
    • Shyam SanthanamBradley Jay Adelman
    • F01N11/00F01N3/08F01N3/20
    • F01N11/002F01N3/0842F01N3/208F01N2610/02F01N2610/146F01N2900/1606Y02T10/24Y02T10/47
    • A method for managing ammonia dosing during a regeneration event for a nitrogen oxide particulate filter in (NPF) includes a selective catalytic reduction system and a particulate filter. Embodiments include utilizing monitored pressure changes across the NPF to predict the soot load and when the soot load will reach a level that triggers a regeneration event. The predicted timing of the regeneration event is used to utilize ammonia absorbed on the NPF and adjust the amount or rate of dosing ammonia to manage ammonia levels in the NPF during the regeneration event. Prior to the regeneration event, the amount of dosing ammonia may be reduced so that ammonia released from the NPF is utilized in converting nitrogen oxides to nitrogen gas and water. After the released ammonia has been utilized, the amount of dosing ammonia may be increased so that the conversion of the nitrogen oxides continues.
    • 在(NPF)中的氮氧化物微粒过滤器的再生事件期间管理氨剂量的方法包括选择性催化还原系统和颗粒过滤器。 实施例包括利用跨越NPF的监测的压力变化来预测烟灰负荷以及烟灰负荷何时达到触发再生事件的水平。 再生事件的预测时间被用于利用在NPF上吸收的氨,并调节在再生事件期间给予氨的量或速率以管理NPF中的氨水平。 在再生事件之前,可以减少给料量的氨,使得从NPF释放的氨被用于将氮氧化物转化为氮气和水。 在释放的氨被利用之后,可以增加给料量的氨,以使氮氧化物的转化继续进行。
    • 3. 发明申请
    • LOWER TEMPERATURE MIXING ZONE FOR NH3
    • 较低温度的NH3混合区
    • US20130216459A1
    • 2013-08-22
    • US13882927
    • 2010-11-01
    • Brad J. AdelmanEdward M. DerybowskiShyam Santhanam
    • Brad J. AdelmanEdward M. DerybowskiShyam Santhanam
    • B01D53/92
    • B01D53/92F01N3/0226F01N3/0821F01N3/108F01N3/2073F01N13/009F01N2240/20F01N2570/18F01N2610/02Y02A50/2325Y02T10/20
    • A method fluidly coupling components of an exhaust gas treatment system to an exhaust gas system, then injecting gaseous ammonia into the gas treatment system, beginning reaction of gaseous ammonia with exhaust gas at a temperature of less than about 180° C., preferably about 150° C., and then continuing reaction of gaseous ammonia with exhaust gas during operation of the vehicle, is disclosed. The gas treatment system includes a mixing chamber for reacting gaseous ammonia with exhaust gas to reduce NOx in the exhaust gas. Other components of the system include a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NOx slip catalyst (NSC) canister, wherein the DOC, DPF and NSC are all fluidly coupled together and to the mixing chamber, an injection port for adding gaseous ammonia to the mixing chamber, and a solid ammonia source for supplying gaseous ammonia to the injection port.
    • 一种将废气处理系统的部件流体耦合到废气系统,然后将气态氨注入气体处理系统中的方法,在低于约180℃,优选约150℃的温度下开始气态氨与废气的反应 ℃,然后在车辆操作期间气态氨与废气的持续反应。 气体处理系统包括用于使氨气与废气反应的混合室,以减少废气中的NOx。 该系统的其它组分包括柴油氧化催化剂(DOC),柴油微粒过滤器(DPF),NOx滑动催化剂(NSC)罐,其中DOC,DPF和NSC都流体耦合在一起并连接到混合室, 用于向混合室中加入气态氨的注入口,以及用于向注入口供应气态氨的固体氨源。
    • 7. 发明授权
    • Method and apparatus for de-sulfurization on a diesel oxidation catalyst
    • 在柴油机氧化催化剂上脱硫的方法和装置
    • US08302387B2
    • 2012-11-06
    • US12546717
    • 2009-08-25
    • Shyam SanthanamBrad Adelman
    • Shyam SanthanamBrad Adelman
    • F01N3/00F01N1/00
    • F01N3/2033F01N3/103F01N3/2053F01N13/0093F01N2410/00Y02A50/2322Y02T10/26
    • A diesel exhaust after-treatment system (110, 210) for a vehicle includes a precious metal primary diesel oxidation catalyst (DOC1) and a precious metal secondary diesel oxidation catalyst (DOC2). The primary diesel oxidation catalyst (DOC1) is located on an exhaust pipe (116, 250) and in fluid communication with and between an engine (12) and an exhaust gas outlet (126, 226). The secondary diesel oxidation catalyst (DOC2) is disposed in fluid communication with the primary diesel oxidation catalyst (DOC1) on a second exhaust pipe (130, 230, 232) and in fluid communication with the engine (12). At least one valve (128, 228, 246) is disposed on the exhaust pipe (116, 216) for selectively permitting the continuous, positive flow of exhaust gas through the secondary diesel oxidation catalyst (DOC2). When the primary diesel oxidation catalyst (DOC1) has a pre-determined amount of sulfur saturation, the valve (128, 228, 246) is switched to permit the continuous, positive flow of exhaust gas through the secondary diesel oxidation catalyst (DOC2).
    • 用于车辆的柴油机废气后处理系统(110,210)包括贵金属一级柴油氧化催化剂(DOC1)和贵金属二级柴油氧化催化剂(DOC2)。 主柴油氧化催化剂(DOC1)位于排气管(116,250)上并与发动机(12)和排气出口(126,226)流体连通并且在发动机(12)和废气出口(126,226)之间流体连通。 二次柴油氧化催化剂(DOC2)在第二排气管(130,230,232)上与主柴油机氧化催化剂(DOC1)流体连通并与发动机(12)流体连通地设置。 至少一个阀(128,228,246)设置在排气管(116,216)上,用于选择性地允许废气通过二次柴油机氧化催化剂(DOC2)的连续的正向流动。 当初级柴油氧化催化剂(DOC1)具有预定量的硫饱和时,阀(128,228,246)被切换以允许废气通过二次柴油氧化催化剂(DOC2)的连续的正向流动。