• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method for cleaning diesel engine exhaust gas is described. The exhaust gas is passed over a catalytic converter with an active material which contains (% by weight) 70-95% TiO2, 2-10% WO3 and/or MoO3, 0.1-5% V2O5, 0.1-8% CaO, 0.1-8% Al2O3, 0.1-5% B2O3 and 0.1-10% SiO2. A reducing agent for a reduction of nitrogen oxides is metered into the exhaust-gas stream upstream of the catalytic converter.
    公开号:US20010004452A1
    申请号:US09/725,340
    申请日:2000-11-29
    公开日:2001-06-21
    发明作者:Wieland Mathes；Ronald Neufert；Dietmar Weisensel；Klaus Wenzlawski
    申请人:Siemens AG；
    IPC主号:B01D53-945
    专利说明:
    [0001] This is a continuation of copending International Application PCT/DE99/01504, filed May 19, 1999, which designated the United States. [0001] BACKGROUND OF THE INVENTION Field of the Invention
    [0002] The invention relates to a method for cleaning diesel engine exhaust gas. It is known that the combustion of diesel fuel leads to the formation of a large number of different pollutants and hydrocarbon-enriched soot particles (referred to below as particles for short), which are removed or at least reduced by suitable catalytic converters with active materials which have a specific action and with separate particle filters. Furthermore, if SCR catalytic converters are used, a device that can be used to meter a reducing agent into the exhaust-gas stream is required. For example, Published, European Patent Application EP 0 341 832 A2 describes a method for cleaning diesel engine exhaust gases in which a device with a platinum-containing catalytic converter is combined with a device for filtering out particles. Furthermore, adsorbers that adsorb pollutants in the lower temperature range and desorb them again at elevated temperatures are frequently used. [0002] SUMMARY OF THE INVENTION
    [0003] It is accordingly an object of the invention to provide a method for cleaning diesel engine exhaust gas that overcomes the above-mentioned disadvantages of the prior art methods of this general type, which is simplified in terms of the outlay on equipment. [0003]
    [0004] With the foregoing and other objects in view there is provided, in accordance with the invention, a method for cleaning diesel engine exhaust gas. The method includes the steps of metering a reducing agent suitable for reducing nitrogen oxides into an exhaust-gas stream upstream of a catalytic converter; and [0004]
    [0005] passing the exhaust gas through the catalytic converter having an active material composed (in % by weight) of: [0005]
    [0006] 70-95% TiO[0006] 2,
    [0007] 2-10% at least one of WO[0007] 3 and MoO3,
    [0008] 0.1-5% V[0008] 2O5,
    [0009] 0.1-8% CaO, [0009]
    [0010] 0.1-8% Al[0010] 2O3,
    [0011] 0.1-5% B[0011] 2O3, and
    [0012] 0.1-10% SiO[0012] 2.
    [0013] In accordance with an added feature of the invention, the active material has a BET surface area of 40-150 m[0013] 2/g.
    [0014] In accordance with an additional feature of the invention, the active material has a pore volume measured using a Hg penetration method of 200-600 mm[0014] 3/g.
    [0015] In accordance with another feature of the invention, the active material has a monomodal pore radius distribution, a frequency maxima of a pore radii lying in a range of 5-10,000 nm. [0015]
    [0016] In accordance with a further feature of the invention, there is the step of using TiO[0016] 2 in its anatase modification.
    [0017] In accordance with a concomitant feature of the invention, the active material has a polymodal pore radius distribution, a frequency maxima of a pore radii lying in a range of 5-10,000 nm. [0017]
    [0018] Other features which are considered as characteristic for the invention are set forth in the appended claims. [0018]
    [0019] Although the invention is described herein as embodied in a method for cleaning diesel engine exhaust gas, it is nevertheless not intended to be limited to the details described, since various modifications and structural changes may be made therein without departing from the spirit of the invention and within the scope and range of equivalents of the claims. [0019]
    [0020] The construction and method of operation of the invention, however, together with additional objects and advantages thereof will be best understood from the following description of specific embodiments. [0020] DESCRIPTION OF THE PREFERRED EMBODIMENT
    [0021] Surprisingly, it has been found that if an active material which contains (in % by weight) 70-95% TiO[0021] 2, 2-10% WO3 and/or MoO3, 0.1-5% V2O5, 0.1-8% CaO, 0.1-8% Al2O3, 0.1-5% B2O3 and 0.1-10% SiO2 is used, the levels of nitrogen oxides, hydrocarbons and particles can be reduced simultaneously. As a result, a single-stage catalytic process is available, in which there is no need for a separate particle filter system or primary-side measures for reducing the levels of particles.
    [0022] The advantages of a method of this type in terms of the outlay on equipment and in terms of the installation space required are obvious. The cleaning method proposed operates in the customary way. For example, to reduce the nitrogen oxides using a selective catalytic reduction (SCR) process, a nitrogen-containing reducing agent is injected into the exhaust-gas stream upstream of the catalytic converter according to the invention. The amount of reducing agent required is determined in the usual way from the engine and engine exhaust-gas data by characteristic diagram control or sensor control. Conventional NO[0022] x, NH3, HC, CO, O2, temperature or other sensors are used for this purpose. It is preferable to use a catalytic converter whose active material has a BET surface area of 40-150 m2/g (BET method, see S. Brunaurer, P. H. Emmett, and E. Teller, JACS Vol. 60, 309 (1938)). A pore volume—measured using the Hg penetration method—is preferably 200-600 mm3/g. The monomodal or polymodal pore radius distribution is selected in such a way that the frequency maxima of the pore radii lie in the range of 5-10,000 nm. The TiO2 modification used is preferably the anatase modification.
    [0023] To produce a catalytic converter that can be used for the method according to the invention, TiO[0023] 2 is mixed with the other oxides or their precursor compounds, which can be converted into the oxides by calcining at 200-800° C., and the mixture is homogenized. A mixture of this type is activated by milling or kneading and is processed into unsupported catalysts using standard ceramic processes or is used to coat inert support bodies using conventional methods. In both cases, the method is completed by drying at between room temperature and 100° C. and calcining at 200-800° C. Forms of catalytic converter obtained in this way include, for example, unsupported honeycomb catalyst extrudates, coated metal grids or foils, coated inert or refractory ceramic supports.
    [0024] A 63 liter catalytic converter with an active material which is composed of (% by weight) 75% TiO[0024] 2, 8% WO3, 3% V2O5, 8% SiO2, 1.5% Al2O3, 2% CaO and 0.5% B2O3 was tested in a diesel engine with a 12 l capacity and 315 KW output. The measurement was carried out on an engine test bed in a test cycle in accordance with ECE-R.49 (13-stage test). The measurements determined that 76% of the nitrogen oxides, 87% of the hydrocarbons and 50% of the particles were converted.
    权利要求:
    Claims (6)
    [1" id="US-20010004452-A1-CLM-00001] 1. A method for cleaning diesel engine exhaust gas, which comprises the steps of:
    metering a reducing agent suitable for reducing nitrogen oxides into an exhaust-gas stream upstream of a catalytic converter; and
    passing the exhaust gas through the catalytic converter having an active material composed (in % by weight) of:
    70-95% TiO2,
    2-10% at least one of WO3 and MoO3,
    0.1-5% V2O5,
    0.1-8% CaO,
    0.1-8% Al2O3,
    0.1-5% B2O3, and
    0.1-10% SiO2.
    [2" id="US-20010004452-A1-CLM-00002] 2. The method according to
    claim 1 , wherein the active material has a BET surface area of 40-150 m2/g.
    [3" id="US-20010004452-A1-CLM-00003] 3. The method according to
    claim 1 , wherein the active material has a pore volume measured using a Hg penetration method of 200-600 mm3/g.
    [4" id="US-20010004452-A1-CLM-00004] 4. The method according to
    claim 1 , wherein the active material has a monomodal pore radius distribution, a frequency maxima of a pore radii lying in a range of 5-10,000 nm.
    [5" id="US-20010004452-A1-CLM-00005] 5. The method according to
    claim 1 , which comprises using TiO2 in its anatase modification.
    [6" id="US-20010004452-A1-CLM-00006] 6. The method according to
    claim 1 , wherein the active material has a polymodal pore radius distribution, a frequency maxima of a pore radii lying in a range of 5-10,000 nm.
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    同族专利:
    公开号 | 公开日
    KR20010043862A|2001-05-25|
    WO1999062619A2|1999-12-09|
    EP1079910B1|2003-04-09|
    WO1999062619A3|2000-02-17|
    JP2002516739A|2002-06-11|
    AT236706T|2003-04-15|
    US6488903B2|2002-12-03|
    EP1079910A2|2001-03-07|
    DE59904961D1|2003-05-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US20080247929A1|2004-10-19|2008-10-09|Millennium Inorganic Chemicals, Inc.|HIGH ACTIVITY TITANIA SUPPORTED METAL OXIDE DeNOx CATALYSTS|
    US20140056793A1|2012-08-24|2014-02-27|Cristal Usa Inc.|Catalyst support materials, catalysts, methods of making them and uses thereof|
    EP2719454A1|2012-10-11|2014-04-16|Treibacher Industrie AG|Thermostable Vanadia SCR catalyst and a process of preparation thereof|
    GB2562611A|2017-03-30|2018-11-21|Johnson Matthey Plc|A catalyst for treating an exhaust gas, an exhaust system and a method|JPS5730532B2|1976-04-08|1982-06-29|||
    JPH0811194B2|1986-12-08|1996-02-07|株式会社日本触媒|Nitrogen oxide removal catalyst|
    US4902487A|1988-05-13|1990-02-20|Johnson Matthey, Inc.|Treatment of diesel exhaust gases|
    US5198403A|1989-02-28|1993-03-30|Degussa Ag|Process for producing a catalyst for selective reduction of nitrous oxides with ammonia|
    JP2778801B2|1990-04-23|1998-07-23|三菱重工業株式会社|Exhaust gas treatment catalyst|
    JP2781639B2|1990-05-07|1998-07-30|三菱重工業株式会社|Exhaust gas treatment method|
    US5215953A|1990-06-08|1993-06-01|Degussa Aktiengesellschaft|Catalyst for the oxidation of sulfur dioxide and method for the production of the catalyst|
    US5427601A|1990-11-29|1995-06-27|Ngk Insulators, Ltd.|Sintered metal bodies and manufacturing method therefor|
    DE4229471A1|1992-09-03|1994-03-10|Man Nutzfahrzeuge Ag|Process for the purification of exhaust gases from diesel engines|
    DE4321555C1|1993-06-29|1994-09-15|Bayer Ag|Process for producing mixed-oxide powders for denitration catalysts|
    US5658546A|1993-07-30|1997-08-19|Nippon Shokubai Co., Ltd.|Denitration catalyst|
    DE19546612A1|1995-12-13|1997-06-19|Basf Ag|Process for the reduction of NOx from exhaust gases|
    DE19635893A1|1996-09-04|1998-03-05|Basf Ag|Catalyst composition and method for the selective reduction of NO¶x¶ while largely avoiding the oxidation of SO¶x¶ in oxygen-containing combustion exhaust gases|DE10323607B4|2003-05-20|2019-05-09|Robert Bosch Gmbh|Device for cleaning exhaust gases of an internal combustion engine|
    JP2005342711A|2004-05-07|2005-12-15|Mitsubishi Chemical Engineering Corp|Denitration method of diesel engine exhaust gas|
    US8481452B2|2009-12-15|2013-07-09|Millennium Inorganic Chemicals, Inc.|Capture of volatilized vanadium and tungsten compounds in a selective catalytic reduction system|
    US9283519B2|2010-02-01|2016-03-15|Johnson Matthey Public Limited Company|Filter comprising combined soot oxidation and NH3-SCR catalyst|
    RU2637510C2|2011-08-03|2017-12-05|Джонсон Мэтти Плс|Extruded honeycomb catalyst|
    CN103240078B|2013-05-22|2014-12-10|重庆远达催化剂制造有限公司|Wear-resistant SCRdenitration catalyst and preparation method thereof|
    法律状态:
    2002-10-22| AS| Assignment|Owner name: SIEMENS AKTIENGESELLSCHAFT, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:MATHES, WIELAND;NEUFERT, RONALD;WEISENSEL, DIETMAR;AND OTHERS;REEL/FRAME:013405/0586;SIGNING DATES FROM 20010116 TO 20010220 |
    2006-06-21| REMI| Maintenance fee reminder mailed|
    2006-12-04| LAPS| Lapse for failure to pay maintenance fees|
    2007-01-03| STCH| Information on status: patent discontinuation|Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
    2007-01-30| FP| Expired due to failure to pay maintenance fee|Effective date: 20061203 |
    优先权:
    申请号 | 申请日 | 专利标题
    DE19824206||1998-05-29||
    DE19824206.9||1998-05-29||
    DE19824206||1998-05-29||
    PCT/DE1999/001504|WO1999062619A2|1998-05-29|1999-05-19|Method for cleaning diesel engine exhaust gas|
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