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公开(公告)号:US07610751B2
公开(公告)日:2009-11-03
申请号:US11490910
申请日:2006-07-21
IPC分类号: F01N3/00
CPC分类号: F01N3/035 , F01N3/0253 , F01N3/0871 , F01N13/0097 , F01N2240/30 , F01N2610/1453 , Y02A50/2325
摘要: One concept relates to power generation system, comprising a diesel engine, an exhaust manifold, a turbocharger, and an exhaust line in which are configured a fuel reformer and a LNT. A fuel injector is configured to inject fuel into the manifold upstream of the turbine. The high temperatures upstream of the turbine cause the fuel to crack into smaller molecules, releasing heat and providing a boost to the turbocharger. The fuel injected into the manifold also undergoes intense mixing as it passes through the turbocharger. Injecting fuel in this manner provides several benefits for reformer operation. Another concept relates to a manifold fuel injector used to provide fuel for heating a DPF.
摘要翻译: 一个概念涉及发电系统,其包括柴油发动机,排气歧管,涡轮增压器和排气管,其中构成燃料重整器和LNT。 燃料喷射器构造成将燃料喷射到涡轮机上游的歧管中。 涡轮上游的高温使得燃料裂解成更小的分子,释放热量并为涡轮增压器提供增压。 注入歧管的燃料在通过涡轮增压器时也经受强烈的混合。 以这种方式注入燃料为重整器操作提供了几个好处。 另一个概念涉及用于提供用于加热DPF的燃料的歧管燃料喷射器。
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公开(公告)号:US20080016849A1
公开(公告)日:2008-01-24
申请号:US11490910
申请日:2006-07-21
CPC分类号: F01N3/035 , F01N3/0253 , F01N3/0871 , F01N13/0097 , F01N2240/30 , F01N2610/1453 , Y02A50/2325
摘要: One concept relates to power generation system, comprising a diesel engine, an exhaust manifold, a turbocharger, and an exhaust line in which are configured a fuel reformer and a LNT. A fuel injector is configured to inject fuel into the manifold upstream of the turbine. The high temperatures upstream of the turbine cause the fuel to crack into smaller molecules, releasing heat and providing a boost to the turbocharger. The fuel injected into the manifold also undergoes intense mixing as it passes through the turbocharger. Injecting fuel in this manner provides several benefits for reformer operation. Another concept relates to a manifold fuel injector used to provide fuel for heating a DPF.
摘要翻译: 一个概念涉及发电系统,其包括柴油发动机,排气歧管,涡轮增压器和排气管,其中构成燃料重整器和LNT。 燃料喷射器构造成将燃料喷射到涡轮机上游的歧管中。 涡轮上游的高温使得燃料裂解成更小的分子,释放热量并为涡轮增压器提供增压。 注入歧管的燃料在通过涡轮增压器时也经受强烈的混合。 以这种方式注入燃料为重整器操作提供了几个好处。 另一个概念涉及用于提供用于加热DPF的燃料的歧管燃料喷射器。
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公开(公告)号:US08069654B2
公开(公告)日:2011-12-06
申请号:US11653745
申请日:2007-01-16
IPC分类号: F01N3/00
CPC分类号: F01N3/0814 , B01D53/9418 , B01D53/9422 , B01D53/9477 , B01D2251/208 , B01D2255/1025 , B01D2255/202 , B01D2255/204 , B01D2255/91 , B01D2255/911 , B01D2258/012 , F01N3/0842 , F01N3/0878 , F01N3/0885 , F01N3/2073 , F01N13/009 , F01N13/011 , F01N2240/30 , F01N2610/03 , Y02A50/2325 , Y02T10/24
摘要: Rhodium utilization in LNT/SCR-based exhaust after treatment systems for medium and heavy duty trucks is reduced by operating inline fuel reformers in a certain manner. The fuel processors are operated at steam reforming temperatures to produce a reformate-containing exhaust having a hydrogen to CO ratio of at least about 3:2 or at least about 3% hydrogen, This generally involves operating the fuel reformers at temperatures from about 500 to about 625° C. and with an overall fuel to air ratio from about 1.10 to about 1.40. In this manner, regeneration can be efficiently carried out while limiting the catalyst loading of the fuel processors to no more than about 1.0 grams rhodium per liter maximum displacement of the diesel engine and the catalyst loading of the LNTs to no more than about 0.50 grams rhodium per liter maximum displacement of the diesel engine.
摘要翻译: 通过以某种方式运行直列式燃料重整器,减少了中型和重型卡车处理系统后的LNT / SCR型尾气中的铑利用。 燃料处理器在蒸汽重整温度下运行以产生具有至少约3:2或至少约3%氢的氢至CO比的重整油含量排气。这通常涉及在约500至 约625℃,总燃料空气比约为1.10至约1.40。 以这种方式,可以有效地进行再生,同时将燃料处理器的催化剂负载限制在不超过约1.0克铑/升柴油发动机的最大排量和催化剂负载量至不超过约0.50克的铑 每升最大排量的柴油发动机。
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公开(公告)号:US20080168763A1
公开(公告)日:2008-07-17
申请号:US11653745
申请日:2007-01-16
IPC分类号: F01N3/023
CPC分类号: F01N3/0814 , B01D53/9418 , B01D53/9422 , B01D53/9477 , B01D2251/208 , B01D2255/1025 , B01D2255/202 , B01D2255/204 , B01D2255/91 , B01D2255/911 , B01D2258/012 , F01N3/0842 , F01N3/0878 , F01N3/0885 , F01N3/2073 , F01N13/009 , F01N13/011 , F01N2240/30 , F01N2610/03 , Y02A50/2325 , Y02T10/24
摘要: Rhodium utilization in LNT/SCR-based exhaust aftertreatment systems for medium and heavy duty trucks is reduced by operating inline fuel reformers in a certain manner. The fuel processors are operated at steam reforming temperatures to produce a reformate-containing exhaust having a hydrogen to CO ratio of at least about 3:2 or at least about 3% hydrogen, This generally involves operating the fuel reformers at temperatures from about 500 to about 625° C. and with an overall fuel to air ratio from about 1.10 to about 1.40. In this manner, regeneration can be efficiently carried out while limiting the catalyst loading of the fuel processors to no more than about 1.0 grams rhodium per liter maximum displacement of the diesel engine and the catalyst loading of the LNTs to no more than about 0.50 grams rhodium per liter maximum displacement of the diesel engine.
摘要翻译: 通过以一定的方式运行直列式燃料重整器,减少了中型和重型卡车的LNT / SCR排气后处理系统中的铑利用。 燃料处理器在蒸汽重整温度下运行以产生具有至少约3:2或至少约3%氢的氢至CO比的重整油含量排气。这通常涉及在约500至 约625℃,总燃料空气比约为1.10至约1.40。 以这种方式,可以有效地进行再生,同时将燃料处理器的催化剂负载限制在不超过约1.0克铑/升柴油发动机的最大排量和催化剂负载量至不超过约0.50克的铑 每升最大排量的柴油发动机。
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公开(公告)号:US6159442A
公开(公告)日:2000-12-12
申请号:US129294
申请日:1998-08-05
申请人: Jeffrey R. Thumm , Michael A. Lento , Jerome S. Higgins , David Lassen King , David Mark Ginter , Laurent DAny Kieken
发明人: Jeffrey R. Thumm , Michael A. Lento , Jerome S. Higgins , David Lassen King , David Mark Ginter , Laurent DAny Kieken
IPC分类号: B01F3/08 , B01F5/02 , B01J3/00 , B01J4/02 , B01J14/00 , B01J19/00 , B01J19/26 , B01J23/80 , C01B13/36 , C01B33/26 , C01F11/18 , C01F11/46 , C01G1/02 , C01G9/00 , C01B3/12
CPC分类号: B01J19/26 , B01F5/0256 , B01J14/00 , B01J19/0093 , B01J23/80 , B01J3/00 , B01J4/02 , C01B13/36 , C01B13/363 , C01B33/26 , C01F11/181 , C01F11/462 , C01G1/02 , C01G9/006 , B01F13/0059 , B01F3/08 , B01J2208/00672 , B01J2219/00162 , B01J2219/00164 , B01J2219/00889 , B01J2219/00891 , C01P2002/22 , C01P2002/72 , C01P2004/38 , C01P2004/52 , C01P2004/61 , C01P2004/62
摘要: Processes for use of a controlled continuous high pressure multiple reactant streams flowing into a chemical mixer/reactor. Individual reactant streams are pressurized to about 8,000 to 50,000 psi and achieve velocities up to about 250 meters/second in the final stage of the chemical mixer/reactor.
摘要翻译: 使用流入化学混合器/反应器的受控连续高压多反应物流的方法。 单个反应物流被加压至约8,000至50,000psi,并且在化学搅拌器/反应器的最后阶段达到高达约250米/秒的速度。
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