WO2008046921A1 - Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene, procede de preparation et utilisation dans le traitement des gaz d'echappement - Google Patents
Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene, procede de preparation et utilisation dans le traitement des gaz d'echappement Download PDFInfo
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- WO2008046921A1 WO2008046921A1 PCT/EP2007/061236 EP2007061236W WO2008046921A1 WO 2008046921 A1 WO2008046921 A1 WO 2008046921A1 EP 2007061236 W EP2007061236 W EP 2007061236W WO 2008046921 A1 WO2008046921 A1 WO 2008046921A1
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
- B01D53/945—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific catalyst
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/20—Vanadium, niobium or tantalum
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
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- C01P2006/13—Surface area thermal stability thereof at high temperatures
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- Y02T10/12—Improving ICE efficiencies
Definitions
- the present invention relates to a composition with high acidity based on zirconium oxide, titanium oxide and tungsten oxide, its method of preparation and its use in particular in the treatment of exhaust gas.
- the object of the invention is to provide materials that can be used in the manufacture of catalysts that meet these needs.
- composition according to the invention is based on zirconium oxide, titanium oxide and tungsten oxide in the following proportions by mass in these different elements:
- tungsten oxide 1% -20% of the zirconium oxide supplement, and it is characterized in that it also has an acidity measured by the methylbutynol test of at least 90%.
- the composition is based on zirconium oxide, titanium oxide, tungsten oxide and at least one oxide of another element M selected from silicon , aluminum, iron, molybdenum, manganese, zinc, tin and rare earths in the following proportions by mass in these elements:
- - tungsten oxide 1% -20% - oxide of the element M: 1% -20% complement zirconium oxide, and it is characterized in that it also has an acidity measured by the methylbutynol test at least 90%.
- composition of the invention imparts good catalytic activity to the catalysts in the manufacture of which it is used.
- composition of the invention has improved resistance to sulfation.
- the term "specific surface” means the specific surface area B. AND. determined by nitrogen adsorption in accordance with ASTM D 3663-78 based on the BRUNAUER - EMMETT-TELLER method described in the journal "The Journal of the American
- Rare earth means the elements of the group consisting of yttrium and the elements of the periodic classification of atomic number inclusive between 57 and 71.
- the periodic table of elements referred to is that published in the Supplement to the Bulletin. of the Chemical Society of France n ° 1 (January 1966).
- the calcinations at which the surface values are given are calcinations under air.
- the contents are given in mass and oxide unless otherwise indicated.
- compositions according to the invention are characterized first of all by the nature of their constituents.
- these compositions are based on zirconium oxide (ZrO 2 ), titanium oxide (TiO 2 ) and tungsten oxide (WO 3 ) and in the proportions indicated.
- the proportion of zirconium oxide may be more particularly at least 40% and may be in particular between 40% and 60%.
- the proportion of zirconium oxide can be between 50% and 55%, that of titanium oxide between 30% and 35% and that of tungsten oxide between 5 and 10%, this variant being applicable to both embodiments of the invention.
- the element M its content may be more particularly between 1% and 10%.
- the element M may be more particularly cerium and yttrium.
- compositions of the invention may comprise one or more elements M in combination, it being understood that in the case of the presence of several elements M, the total content of these elements remains within the aforementioned range of 1% to 20%.
- multicomponent compositions M include compositions comprising, in addition to oxides of zirconium, titanium and tungsten, silicon oxide and an oxide of a rare earth, this rare earth being more particularly cerium or alternatively silicon oxide and iron oxide, or silicon oxide and manganese oxide or finally cerium oxide and manganese oxide.
- compositions of the invention are their acidity. This acidity is measured by the methylbutynol test, which will be described later, and it is at least 90% and, more particularly, it can be at least 95%. This acidity can also be evaluated by the acid activity which is also measured from the methylbutynol test and which characterizes an acidity of the product independently of its surface.
- This acid activity is at least 0.05 mmol / h / m 2 , more particularly at least 0.075 mmol / h / m 2 . It may be more particularly at least 0.09 mmol / h / m 2 and especially at least 0.13 mmol / h / m 2 .
- compositions of the invention have a large specific surface area.
- This surface may in fact be at least 50 m 2 / g after calcination at 750 ° C. for 2 hours.
- this surface measured under the same conditions, may be more particularly at least 100 m 2 / g.
- this surface may be at least 40 m 2 / g after calcination at 950 ° C. for 2 hours.
- compositions of the invention may be in the form of a mixture of the oxides of the various elements forming part of their constitution.
- the different phases present in the composition can be detected by the X-ray diffraction technique.
- the tungsten and M elements can not be demonstrated in the form of their corresponding oxide, which indicates that they are in solid solution with the other elements of the composition.
- these compositions may be in the form of a solid solution even after calcination at 750 ° C. for 2 hours.
- the tungsten and M elements are in solid solution in a phase which, in the case of the latter variant, is a single crystalline phase, which may be ZrTiO 4 , a tetragonal zirconia or else titanium oxide in anatase form depending on the relative proportions of zirconium and titanium in the composition.
- This feature can be demonstrated by X-ray diffraction analysis of the composition.
- the X-ray diagrams in this case do not reveal peaks corresponding to an oxide of the tungsten or M elements. These diagrams only show the presence of a single crystalline phase, for example of the type of those mentioned above.
- compositions of the invention may furthermore have a sulfate content which may be very low.
- This content may be at most 800 ppm, more particularly at most 500 ppm, even more particularly at most 100 ppm, this content being expressed as a mass of SO 4 with respect to the entire composition.
- This content is measured by a LECO type device or ELTRA that is to say by a technique implementing a catalytic oxidation of the product in an induction furnace and an IR analysis of SO2 formed.
- compositions of the invention may also have a chlorine content which can be very low.
- This content may be at most 500 ppm, especially at most 200 ppm, more precisely at most 100 ppm, more particularly at most 50 ppm and even more particularly at most 10 ppm. This content being expressed as a mass of Cl relative to the entire composition.
- compositions of the invention may also have an alkali content, in particular sodium content, of at most 500 ppm, in particular at most 200 ppm, more particularly at most 100 ppm, and even more particularly at not more than 50 ppm. This content being expressed in mass of element, for example mass of Na, relative to the entire composition.
- This method is characterized in that it comprises the following steps:
- the first step of the process therefore consists in bringing together in a liquid medium compounds of zirconium, titanium and, in the case of the second embodiment, a compound of the element M. These various compounds are present in the stoichiometric proportions necessary to obtain the desired final composition.
- the liquid medium is usually water.
- the compounds are preferably soluble compounds.
- the compounds of zirconium and titanium can be in particular oxysulphates, oxynitrates but, preferably, for these two elements, the oxychlorides are used.
- an alkali silicate may be used and sodium silicate may be mentioned more particularly.
- the silicon may also be provided by a silica sol such as for example Morrisol or Ludox marketed respectively by Morrisons Gas Related Products Limited and Grace Davison or by an organometallic compound such as sodium ortho-tetraethylsilicate (TEOS), potassium methylsiliconate or the like.
- TEOS sodium ortho-tetraethylsilicate
- inorganic or organic salts of these elements may be used. Chlorides or acetates and, more particularly, nitrates may be mentioned.
- ammonium heptamolybdate (NH 4 J 6 Mo 7 O 24 , 4H 2 O.
- the basic compound can be used the products of the hydroxide or carbonate type.
- alkali or alkaline earth hydroxides and ammonia there may be mentioned secondary, tertiary or quaternary amines. We can also mention urea.
- Sodium hydroxide can be used especially.
- the placing in the presence of the different compounds can be done in different ways.
- the various compounds can preferably be introduced in the following order: water, zirconium compound, titanium compound and then silicon compound and optionally that of element M, and the medium thus formed is brought into contact with the basic compound.
- step (a) of the process can be carried out at a temperature of between 15 ° C. and 80 ° C. in particular.
- step (b) the precipitate obtained in step (a) is separated off, this separation being possible by any conventional solid-liquid separation technique such as, for example, filtration, decantation, spinning. or centrifugation.
- the thus separated precipitate for example with water, may then be washed optionally and resuspended in water. It is on this suspension thus obtained that step (b) is then implemented. It may be interesting, before carrying out the next step and optionally the separation of the precipitate obtained in step
- the second step of the process consists in forming a suspension comprising the precipitate from step (a) or from the suspension resulting from step (a) and adding thereto a tungsten compound.
- the pH of the medium is adjusted to a value of between 1 and 7. This value can be more particularly between 3 and 5. It is also possible to proceed by first adjusting in the same value range. the pH of the slurry formed from the precipitate of step (a) and then adding the tungsten compound.
- the pH adjustment can be done for example by addition of nitric acid.
- the precipitate obtained after step (b) can be separated.
- This separation can be carried out by any known technique of solid-liquid separation for example by filtration, decantation, spinning or centrifugation.
- the precipitate can also be washed after separation, for example with water and then resuspended in water. Step (c) is then implemented on the suspension thus obtained. It may be advantageous, before carrying out the next step and optionally the separation of the precipitate obtained in step (b), to heat the medium to a temperature which may be between 40 ° C. and
- the third step of the process consists in carrying out a maturing of the suspension resulting from the preceding step (b).
- This ripening is done by heating the environment.
- the temperature at which the medium is heated is at least 60 ° C., more particularly at least 90 ° C. and even more particularly at least 140 ° C.
- the medium is maintained thus at a constant temperature for a period of time which is usually at most 6 hours.
- the ripening can be done at atmospheric pressure or possibly at a higher pressure.
- the pH of the medium can be adjusted to a value between 3 and 10, preferably between 3 and 5. The pH adjustment can be done for example by addition of nitric acid.
- a suspension is obtained which contains a mass of a solid precipitate which may optionally be dried and which is then calcined in the last step (d) of the process.
- the precipitate can be separated from its liquid medium by the aforementioned known techniques before the possible drying and before the calcination.
- the product thus obtained can be subjected to one or more washings with water or with acidic or basic aqueous solutions.
- the suspension obtained at the end of step (c) may also be calcined, possibly after a drying step, without liquid / solid separation.
- the drying temperature is generally between 50 ° C. and 300 ° C., preferably between 100 ° C. and 150 ° C.
- the suspension can be spray-dried.
- spray drying is used for the present description by spray drying of the suspension in a hot atmosphere (spray-drying).
- the atomization can be carried out using any sprayer known per se, for example by a spraying nozzle of the watering apple or other type. It is also possible to use so-called turbine atomizers.
- the inlet temperature of the gases may be between 200 ° C. and 600 ° C., preferably between 300 ° C. and 400 ° C.
- Drying can also be done by lyophilization.
- the powder obtained can then be calcined under the conditions which are given below.
- step (d) makes it possible to develop the crystallinity of the product formed and it can also be adjusted according to the temperature of subsequent use reserved for the composition, and this taking into account the fact that the specific surface of the product is even lower than the calcination temperature used is higher and / or the duration calcination is important. Such calcination is generally performed under air.
- the calcination temperature is generally limited to a range of values between 500 ° C. and 900 ° C., more particularly between 700 ° C. and 900 ° C.
- duration of this calcination may vary within wide limits, it is in principle all the greater as the temperature is low. By way of example only, this duration can vary between 2 hours and 10 hours.
- the method comprises the following steps:
- - (b ') forming a suspension comprising the precipitate from step (a') or starting from the suspension from step (a 1 ), a tungsten compound and a compound of the element M, and the pH of the medium is adjusted to a value between 1 and 7;
- - (c ') is optionally carried out a maturing of the suspension from the previous step;
- a third embodiment of the method can also be implemented for the preparation of compositions comprising at least two elements M.
- the method according to this third embodiment comprises the following steps:
- step (b ) is formed a suspension comprising the precipitate from step (a") or starting from the suspension from step (a "), there is added a compound of tungsten and a compound of at least one of the elements M, and the pH of the medium is adjusted to a value of between 1 and 7;
- step (e ) is calcined, possibly after drying, the product from the previous step.
- This third mode differs from the second by an additional step (d") in which the second element M is introduced. similarities between the embodiments, what has been described above for the common parts of these different modes also applies here. It will be noted that the drying of step (e ") can be done more particularly by atomization.
- step (b) forming a suspension comprising the precipitate from step (a1) or starting from the suspension resulting from step (a1), adding a tungsten compound and a compound of at least one other M elements, and the pH of the medium is adjusted to a value between 1 and 7;
- compositions of the invention as described above or as obtained by the process mentioned above are in the form of powders but they may optionally be shaped to be in the form of tablets, granules, beads, cylinders or monoliths or filters in the form of honeycombs of varying sizes.
- These compositions can be applied on any support usually used in the field of catalysis, ie in particular thermally inert supports.
- This support may be chosen from alumina, titanium oxide, cerium oxide, zirconium oxide, silica, spinels, zeolites, silicates, crystalline silicoaluminium phosphates, phosphates of crystalline aluminum.
- compositions can also be used in catalytic systems.
- the invention therefore also relates to catalytic systems containing compositions of the invention.
- These catalytic systems may comprise a coating (wash coat) with catalytic properties and based on these compositions, on a substrate of the type for example metallic monolith or ceramic.
- the coating may also include a support of the type mentioned above. This coating is obtained by mixing the composition with the support so as to form a suspension which can then be deposited on the substrate.
- the compositions of the invention may be used in combination with transition metals; they play the role of support for these metals. Transition metal means the elements of groups NIA to MB of the Periodic Table.
- transition metals there may be mentioned more particularly vanadium and copper as well as precious metals, such as platinum, rhodium, palladium, silver or iridium.
- precious metals such as platinum, rhodium, palladium, silver or iridium.
- the nature of these metals and the techniques for incorporating them into the support compositions are well known to those skilled in the art.
- the metals may be incorporated into the compositions by impregnation.
- the systems of the invention can be used in the gas treatment.
- gases that can be treated in the context of the present invention are, for example, those emitted by fixed installations such as gas turbines or boilers of thermal power plants. It may also be the gases from internal combustion engines and especially the exhaust gases of diesel engines
- compositions of the invention may be used in combination with metals of the transition metal type such as vanadium or copper.
- MBOH methylbutynol
- an amount (m) of about 400 mg of composition is placed in a quartz reactor.
- the composition is first subjected to pretreatment at 400 ° C. for 2 h under a gaseous stream of N 2 at a flow rate of 4 L / h.
- the temperature of the composition is then brought back to 180 ° C.
- the composition is then periodically brought into contact with given amounts of MBOH. This periodic contact is to circulate during a 4-minute injection a synthetic mixture of 4% by volume of MBOH in N 2 with a flow rate of 4 L / h which corresponds to a molar hourly flow rate of methylbutynol (Q ) of 7.1 mmol / h. There are 10 injections. At the end of each injection, the gas flow at the outlet of the reactor is analyzed by gas chromatography to determine the nature of the products of the reaction (see Table 1) and their amount.
- An acidic, amphoteric or basic selectivity which is equal to the sum of the selectivities of the products formed for the acidic, amphoteric and basic reactions respectively.
- the acid (S [acid]) selectivity is equal to the sum of the selectivities of 2-methyl-1-buten-3-yne and 3-methyl-2-butenal.
- the rate of transformation of methylbutynol (TT) during the test is calculated by averaging the conversion rates of methylbutynol over the last 5 injections of the test.
- the acid activity (A [acid]) of the composition expressed in mmol / h / m 2, can also be defined from the degree of conversion of methylbutynol (TT expressed in%), the hourly molar rate of methylbutynol (Q expressed in mmol / h), the acid selectivity (S [acid] expressed in%), the amount of composition analyzed (m expressed in g) and the specific surface of the composition (SBET expressed in m 2 / g) according to the following relation:
- This example relates to the preparation of a composition based on oxides of zirconium, titanium and tungsten in the respective proportions by mass of oxide of 47.5%, 47.5% and 5%.
- 1520 g of sodium hydroxide (concentration 10% by weight) are stirred in a reactor and heated at 60 ° C.
- a mixture of the following solutions is prepared with stirring: 110 g of deionized water, 84 g of acid sulfuric acid at 20% as sulphate source, 220 g of zirconium oxychloride solution (concentration 21.6% by weight of ZrO 2 ) and 264 g of a solution of titanium oxychloride (concentration 18.0% by weight TiO 2 ).
- the suspension is filtered on a Buchner funnel and the solid is washed with 6 liters of deionized water at 60 ° C. The solid is then redispersed in deionized water with appropriate stirring in a volume of 1 liter. The suspension is then treated at 144 ° C. for 5 hours.
- the product thus obtained is finally calcined in air at 750 ° C. for 2 hours in step.
- This product is characterized by a surface area of 55 m 2 / g. It has 2 X-ray diffraction phases: the TiO 2 anatase and the ZrTiO 4 phase which is the majority. The X-ray diagram does not show the presence of WO3 tungsten oxide.
- the specific surface area is equal to 26 m 2 / g.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- This example relates to the preparation of a composition based on oxides of zirconium, titanium, tungsten and silicon in the respective proportions by mass of oxide of 54%, 34.7%, 7.5% and 3, 8%.
- the suspension is filtered on a Buchner funnel and the solid is washed with 6 liters of deionized water at 60 ° C. The solid is then redispersed in deionized water with appropriate stirring in a volume of 1 liter. The suspension is then treated at 144 ° C. for 5 hours.
- the product thus obtained is finally calcined in air at 900 ° C. for 2 hours in steps.
- This product is characterized by a specific surface area of 73 m 2 / g. It has 2 X-ray diffraction phases: the TiO 2 anatase and the ZrTiO 4 phase which is the majority.
- the X-ray diagram does not reveal the presence of tungsten oxide WO 3 or silicon oxide SiO 2 .
- the specific surface area is equal to 45 m 2 / g.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- This example relates to the preparation of a composition based on oxides of zirconium, titanium, tungsten, silicon and yttrium in the respective proportions by mass of oxide of 53.4%, 34.3%, 7 , 5%, 3.8% and 1%.
- the suspension is brought to 60 ° C. and maintained at this temperature for 1 hour. After 1 hour, the suspension is filtered on a Buchner funnel and the solid is washed with 6 liters of deionized water at 60 ° C. The solid is then redispersed in deionized water with appropriate stirring in a volume of 1 liter. The suspension is then treated at 144 ° C. for 5 hours.
- the product thus obtained is finally calcined in air at 750 ° C. for 2 hours in step.
- This product is characterized by a surface area of 129 m 2 / g and a pure ZrTiO 4 phase.
- the X-ray diagram does not show the presence of tungsten oxide WO 3 , or of silicon oxide SiO 2 or yttrium oxide Y 2 O 3 .
- the specific surface is equal to 42 m 2 / g.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- a gamma transition alumina marketed by Condéa is impregnated with a solution of lanthanum nitrate so as to obtain, after drying and calcining in air at 500 ° C., an alumina stabilized with 10% by weight of lanthanum oxide.
- the specific surface is equal to 120 m 2 / g.
- EXAMPLE 5 This example describes a catalytic oxidation test of carbon monoxide CO and HC hydrocarbons using the compositions prepared in the previous examples.
- compositions prepared in the preceding examples are impregnated with a platinum (II) tetramine hydroxide salt (Pt (NH 3 ) 4 (OH) 2 ) in order to obtain a catalyst composition containing 1% by weight of platinum with respect to the mass of oxides.
- a platinum (II) tetramine hydroxide salt Pt (NH 3 ) 4 (OH) 2
- the catalytic compositions obtained are dried at 120 ° C. overnight and then calcined at 500 ° C. under air for 2 hours. They are then subjected to aging before the catalytic test.
- a synthetic gaseous mixture containing 10% vol of O 2 and 10% vol of H 2 O in N 2 in a quartz reactor containing the catalytic compound is continuously circulated over 400 mg of catalyst composition.
- the temperature of the reactor is raised to 750 ° C. for
- a synthetic gas mixture containing 20 vpm of SO 2 , 10% vol of O 2 and 10% vol of H 2 O in N 2 is continuously circulated in a quartz reactor containing the catalytic compound.
- the temperature of the reactor is raised to 300 ° C. for 12 hours in stages.
- the sulfur element content S of the catalytic composition is measured at the end of aging to evaluate its resistance to sulphation. Under aging conditions, the maximum sulfur content that can be captured by the catalyst composition is 1.28% by weight. The lower the sulfur content of the catalytic composition after aging, the higher its resistance to sulfation.
- the aged catalytic compositions are then evaluated as a catalytic temperature initiation test (light-off type) for the oxidation reactions of CO, propane C 3 H 8 and propene C 3 H 6 .
- a synthetic mixture representative of a diesel engine exhaust gas containing 2000 vpm of CO, 667 vpm of H 2 , 250 vpm of C 3 H 6 and 250 vpm of C 3 is passed over the catalytic composition.
- H 8 150 vpm NO, 10% vol CO 2 , 13% vol O 2 and 10% vol H 2 O in N 2 .
- the gaseous mixture is continuously circulated at a rate of 30 L / hr in a quartz reactor containing between 20 mg of catalytic compound diluted in 180 mg of silicon carbide SiC.
- SiC is inert with respect to oxidation reactions and here acts as a diluent making it possible to ensure the homogeneity of the catalytic bed.
- the conversion of CO, propane C3H8 and propene C3H6 is measured as a function of the temperature of the catalytic composition.
- the catalytic composition is thus subjected to a temperature ramp of 10 ° C./min between 100 ° C. and 450 ° C. while the synthetic mixture circulates in the reactor.
- the gases leaving the reactor are analyzed by infrared spectroscopy at intervals of about 10 seconds in order to measure the conversion of CO and hydrocarbons to CO2 and H 2 O.
- T10% and T50% at which temperature is measured respectively 10% and 50% conversion of CO, propane C 3 H 8 or propene C 3 H 6 .
- compositions according to the invention are significantly more resistant to sulphation because the sulfur content captured during the sulphation test is low.
- This example relates to the preparation of a composition based on oxides of zirconium, titanium, silicon, tungsten and cerium in the respective proportions by mass of oxide of 51.5%, 33%, 3.5% , 7% and 5%.
- a solution A is prepared by mixing in a beaker with stirring 152.5 g of zirconyl chloride (20 wt% ZrO 2 ), 97 g of titanyl chloride (20 wt% TiO 2 ) and 25 g of sulfuric acid (97 g). % wt) with 125.5 g of distilled water. 675 g of sodium hydroxide solution (10% wt. NaOH) are introduced into a stirred reactor and then solution A is gradually added with stirring. The pH of the medium reaches a value of at least 12.5, and then a solution is added. sodium hydroxide solution. The precipitate obtained is filtered and washed at 60 ° C. with 3 L of distilled water. The solid is resuspended in 1 L of distilled water.
- the solid is resuspended in 900 ml of distilled water and 11 g of cerium nitrate (III) (496 g / L CeO 2) are added.
- the medium is finally atomized on B ⁇ chi atomizer at 110 ° C (gas outlet temperature).
- the dried solid is calcined in air at 750 ° C. for 2 hours in stages.
- This product is characterized by a specific surface area of 100 m 2 / g and a pure ZrTiO 4 phase.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- This example relates to the preparation of a composition based on oxides of zirconium, titanium, silicon, tungsten and cerium in the respective proportions by mass of oxide of 48%, 31%, 3.5%, , 5% and 10%.
- a solution A is prepared by mixing in a beaker with stirring 134.5 g of zirconyl chloride (20% by weight ZrO 2 ), 86.5 g of titanyl chloride (20% by weight of TiO 2 ), 22 g of sulfuric acid. (97% wt) and 20g of cerium nitrate (III) (496 g / L CeO 2 ) with 90 g of distilled water.
- 661 g of sodium hydroxide solution (10% wt. NaOH) are introduced and then solution A is gradually added with stirring.
- the pH of the medium reaches a value of at least 12.5, and then a solution is added.
- sodium hydroxide solution. 8 g of hydrogen peroxide (30% vol) are introduced into the medium. After stirring for 30 minutes, the precipitate obtained is filtered and washed at 60 ° C. with 3 L of distilled water. The solid is resuspended in 1 L of distilled water.
- the solid is dried overnight in an oven at 120 ° C and the product obtained is calcined in air at 750 ° C for 2 hours in stages.
- This product is characterized by a specific surface area of 99 m 2 / g and a pure ZrTiO 4 phase.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- EXAMPLE 8 This example relates to the preparation of a composition based on oxides of zirconium, titanium, silicon, tungsten and manganese in the respective proportions by mass of oxide of 51.5%, 33%, 3.5% , 7% and 5%.
- Example 6 The procedure is as in Example 6 except that 7.5 g of manganese nitrate (II) are introduced before the atomization.
- the dried solid is calcined in air at 750 ° C. for 2 hours in stages.
- This product is characterized by a specific surface area of 75 m 2 / g and a pure ZrTiO 4 phase.
- the product contains less than 120 ppm of sulphates, 50 ppm of sodium and less than 10 ppm of chlorides.
- Table 7 below gives the acidity values of the compositions which are the subject of Examples 6 to 8.
- a ZSM5 zeolite with an SiO 2 / Al 2 O 3 molar ratio of 30 is exchanged with a solution of iron acetylacetonate to obtain a Fe-ZSM5 zeolite containing 3% by weight of iron.
- the product is dried overnight in an oven at 120 0 C and calcined under air at 500 ° C.
- the specific surface is greater than 300 m 2 / g.
- This example describes a catalytic test for the reduction of NOx nitrogen oxides by ammonia NH 3 (NH 3 -SCR) using the compositions prepared in the previous examples.
- a synthetic gaseous mixture containing 10% vol of O 2 and 10% by volume of H 2 O is circulated continuously over 400 mg of catalytic composition.
- the fresh or aged catalytic compositions are then evaluated as a catalytic NOx conversion test by selective catalytic reduction with NH 3 (SCR).
- SiC is inert with respect to oxidation reactions and here acts as a diluent making it possible to ensure the homogeneity of the catalytic bed.
- a "light-off" type test the NOx conversion and the formation of N 2 O are monitored as a function of the temperature of the catalytic composition.
- the catalytic composition is thus subjected to a temperature ramp of 5 ° C./min between 150 ° C. and 500 ° C. while the synthetic mixture circulates in the reactor.
- the gases leaving the reactor are analyzed by mass spectroscopy in order to monitor the concentrations of the various constituents of the gas mixture.
- the results are expressed as the NOx conversion level at 200 ° C., 300 ° C. and 400 ° C. and the maximum concentration of N 2 O formed during the test.
- Tables 8 and 9 show that the compositions according to the invention make it possible to obtain high NOx conversions in the temperature range of the Diesel application while forming very little N 2 O and this even after severe aging or aging. NO 2 / NO ratios are variable.
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Biomedical Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Analytical Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
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Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/446,184 US20100247411A1 (en) | 2006-10-20 | 2007-10-19 | Highly acidic compositions comprising zirconium oxide, titanium oxide and tungsten oxide and treatment of exhaust gases therewith |
CN2007800390763A CN101534931B (zh) | 2006-10-20 | 2007-10-19 | 含氧化锆、氧化钛和氧化钨的高酸性组合物,其制备方法以及在处理废气中的用途 |
KR1020097007969A KR101165499B1 (ko) | 2006-10-20 | 2007-10-19 | 지르코늄 산화물, 티타늄 산화물 및 텅스텐 산화물을 함유하는 산성이 높은 조성물, 이의 제조 방법 및 배기 가스 처리에서의 이의 용도 |
JP2009532822A JP5219297B2 (ja) | 2006-10-20 | 2007-10-19 | 酸化ジルコニウム、酸化チタンおよび酸化タングステンを含有する高酸性度組成物、この調製方法、ならびに排気ガスの処理におけるこの使用 |
CA002666626A CA2666626A1 (fr) | 2006-10-20 | 2007-10-19 | Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene, procede de preparation et utilisation dans le traitement des gaz d'echappement |
EP07821600A EP2079542A1 (fr) | 2006-10-20 | 2007-10-19 | Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene, procede de preparation et utilisation dans le traitement des gaz d'echappement |
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FR0609223A FR2907445B1 (fr) | 2006-10-20 | 2006-10-20 | Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene,procede de preparation et utilisation dans le traitement des gaz d'echappement |
FR0609223 | 2006-10-20 |
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PCT/EP2007/061236 WO2008046921A1 (fr) | 2006-10-20 | 2007-10-19 | Composition a acidite elevee a base d'oxyde de zirconium, d'oxyde de titane et d'oxyde de tungstene, procede de preparation et utilisation dans le traitement des gaz d'echappement |
Country Status (9)
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US (1) | US20100247411A1 (fr) |
EP (1) | EP2079542A1 (fr) |
JP (1) | JP5219297B2 (fr) |
KR (1) | KR101165499B1 (fr) |
CN (1) | CN101534931B (fr) |
CA (1) | CA2666626A1 (fr) |
FR (1) | FR2907445B1 (fr) |
RU (1) | RU2426583C2 (fr) |
WO (1) | WO2008046921A1 (fr) |
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WO2011116907A2 (fr) | 2010-03-26 | 2011-09-29 | Umicore Ag & Co. Kg | Zrox, ce-zrox, ce-zr-reox au titre de matrices hôtes pour des cations à activité redox pour catalyseurs de réduction sélective à basse température, à durabilité hydrothermique satisfaisante et résistants à l'empoisonnement |
WO2011144601A1 (fr) * | 2010-05-19 | 2011-11-24 | Rhodia Operations | Composition a base de cerium, de zirconium et de tungstene, procede de preparation et utilisation en catalyse |
EP2432589A2 (fr) * | 2009-05-19 | 2012-03-28 | Millennium Inorganic Chemicals, Inc. | Promoteurs de catalyseur dans un catalyseur mobile sans vanadium |
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- 2007-10-19 JP JP2009532822A patent/JP5219297B2/ja not_active Expired - Fee Related
- 2007-10-19 RU RU2009118959/05A patent/RU2426583C2/ru not_active IP Right Cessation
- 2007-10-19 CN CN2007800390763A patent/CN101534931B/zh not_active Expired - Fee Related
- 2007-10-19 US US12/446,184 patent/US20100247411A1/en not_active Abandoned
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US8465714B2 (en) | 2009-02-16 | 2013-06-18 | Cristal Usa Inc. | Catalyst promoters in vanadium-free mobile catalyst |
EP2432589A2 (fr) * | 2009-05-19 | 2012-03-28 | Millennium Inorganic Chemicals, Inc. | Promoteurs de catalyseur dans un catalyseur mobile sans vanadium |
CN102405102A (zh) * | 2009-05-19 | 2012-04-04 | 美礼联无机化工公司 | 无钒汽车催化剂的催化剂助催化剂 |
EP2432589A4 (fr) * | 2009-05-19 | 2013-04-03 | Millennium Inorganic Chem | Promoteurs de catalyseur dans un catalyseur mobile sans vanadium |
CN102405102B (zh) * | 2009-05-19 | 2015-10-14 | 水晶美国股份公司 | 无钒汽车催化剂的催化剂助催化剂 |
FR2950821A1 (fr) * | 2009-10-07 | 2011-04-08 | Rhodia Operations | Composition catalytique pour le traitement d'un gaz pour la conversion des oxydes d'azote en azote et procede utilisant cette composition |
WO2011116907A2 (fr) | 2010-03-26 | 2011-09-29 | Umicore Ag & Co. Kg | Zrox, ce-zrox, ce-zr-reox au titre de matrices hôtes pour des cations à activité redox pour catalyseurs de réduction sélective à basse température, à durabilité hydrothermique satisfaisante et résistants à l'empoisonnement |
WO2011144601A1 (fr) * | 2010-05-19 | 2011-11-24 | Rhodia Operations | Composition a base de cerium, de zirconium et de tungstene, procede de preparation et utilisation en catalyse |
FR2960231A1 (fr) * | 2010-05-19 | 2011-11-25 | Rhodia Operations | Composition a base de cerium, de zirconium et de tungstene, procede de preparation et utilisation en catalyse, notamment pour le traitement des gaz d'echappement |
US9169129B2 (en) | 2010-05-19 | 2015-10-27 | Rhodia Operations | Composition based on cerium, zirconium and tungsten, preparation process and use in catalysis |
CN104562177A (zh) * | 2015-02-10 | 2015-04-29 | 哈尔滨工业大学 | 一种五氧化二钒/氧化钨共沉积立方晶的制备方法 |
CN104562177B (zh) * | 2015-02-10 | 2016-10-12 | 哈尔滨工业大学 | 一种五氧化二钒/氧化钨共沉积立方晶的制备方法 |
Also Published As
Publication number | Publication date |
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CA2666626A1 (fr) | 2008-04-24 |
CN101534931A (zh) | 2009-09-16 |
KR101165499B1 (ko) | 2012-07-13 |
JP2010506713A (ja) | 2010-03-04 |
FR2907445A1 (fr) | 2008-04-25 |
JP5219297B2 (ja) | 2013-06-26 |
CN101534931B (zh) | 2012-06-13 |
KR20090075694A (ko) | 2009-07-08 |
US20100247411A1 (en) | 2010-09-30 |
FR2907445B1 (fr) | 2010-09-03 |
EP2079542A1 (fr) | 2009-07-22 |
RU2009118959A (ru) | 2010-11-27 |
RU2426583C2 (ru) | 2011-08-20 |
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