Abstract:
A method for the direct synthesis of a crystalline material with the AEI zeolithic structure containing iron-species and being essentially free of alkali ions, comprising the following steps: (i) preparation of a mixture containing water, a high-silica zeolite as a main source of silica and alumina, an alkyl-substituted cyclic ammonium cation as organic structure directing agent (OSDA), a source of iron, and a source of an alkali metal ion [Alk], to obtain a final synthesis mixture having the following molar composition: SiO 2 : a AI 2 O 3 : b Fe : c OSDA : d Alk : e H 2 O wherein a is in the range from 0.001 to 0.2; wherein b is in the range from 0.001 to 0.2; wherein c is in the range from 0.01 to 2; wherein d is in the range from 0.001 to 2; wherein e is in the range from 1 to 200; (ii) crystallization of the mixture achieved in (i); (iii) recovery of the crystalline material achieved in (ii); (iv) calcination of the crystalline material from step (iii); and (v) removal of the alkali metal cation, present in the calcined crystalline material after step (iv) to obtain a final molar composition: SiO 2 : o AI 2 O 3 : p Fe : q Alk wherein o is in the range from 0.001 to 0.2, p is in the range from 0.001 to 0.2 and q is below 0.02.
Abstract:
A catalyst article having an extruded support having a plurality of channels through which exhaust gas flows during operation of an engine, and a single layer coating or a bi-layer coating on the support, where the extruded support contains a third SCR catalyst, the single layer coating and the bilayer-coating contain platinum on a support with low ammonia storage and a first SCR catalyst. The catalytic articles are useful for selective catalytic reduction (SCR) of NOx in exhaust gases and in reducing the amount of ammonia slip. Methods for producing such articles are described. Methods of using the catalytic articles in an SCR process, where the amount of ammonia slip is reduced, are also described.
Abstract:
This exhaust gas purification apparatus is provided with: an upstream catalyst section (10), which is disposed on the upstream side of an exhaust pipe (3); a downstream catalyst section (30), which is disposed further downstream in the exhaust pipe (3) than the upstream catalyst section (10); and a reducing agent solution supply means (50) for supplying a reducing agent solution for generating ammonia further upstream than the upstream catalyst section (10). The upstream catalyst section (10) and the downstream catalyst section (30) each comprise a SCR catalyst obtained from zeolite, which adsorbs ammonia and reduces NOx in the exhaust gas. The skeleton density (A) of the SCR catalyst contained in the upstream catalyst section (10) is smaller than the skeleton density (B) of the SCR catalyst contained in the downstream catalyst section (30) (A
Abstract:
Disclosed is a process for producing biphenyl esters, the process comprising contacting a feed comprising toluene, xylene or mixtures thereof with hydrogen in the presence of a hydroalkylation catalyst to produce a hydroalkylation reaction product comprising (methylcyclohexyl)toluene, wherein the hydroalkylation catalyst comprises a binder, a hydrogenation component, and an acidic component comprising a molecular sieve having a twelve membered (or larger) ring pore opening, channel or pocket and a largest pore dimension of 6.0 angstroms or more; dehydrogenating the hydroalkylation reaction product; contacting the dehydrogenation reaction product with an oxidizing gas to convert the methyl- substituted biphenyl compounds to biphenyl carboxylic acids; and reacting the biphenyl carboxylic acids with one or more C 1 to C 14 alcohols to produce biphenyl esters.
Abstract:
The invention relates to a catalyst for producing an isoparaffins-rich synthetic oil from CO and H2 and to a method for preparing this catalyst. An object of the present invention is to improve mass transfer of reagents inside of catalyst granules and increase content of isoparaffins in the produced oil. The catalyst is granulated porous composite material comprising a three-dimensional heat-conducting structure of metal aluminum and Raney cobalt, and a binding component comprising a H-form zeolite. The particles of Raney cobalt are in direct contact with the particles of the zeolite. The method for preparing the catalyst comprises mixing of binding component powders, peptizing the obtained mixture with a solution of nitric acid to obtain the binding component in the form of a homogeneous gel, mixing of the homogeneous gel with a fine powder of Raney cobalt, powder of metal aluminum and a liquid phase to form a homogeneous paste, extrusion of the prepared paste to form granules and calcination of the obtained granules. The H-form zeolite is used as one of the binding component powders.
Abstract:
A substrate monolith (6) having a length L and comprising a first zone (11) of substantially uniform length defined at one end by a first end of the substrate monolith, which first zone comprising a selective catalytic reduction (SCR) catalyst for reducing oxides of nitrogen with a nitrogenous reductant in exhaust gas emitted from an internal combustion engine and a second zone (8) of substantially uniform length less than L defined at one end by a second end of the substrate monolith, which second zone comprising (a) at least one particulate metal oxide or a mixture of any two or more thereof for trapping gas phase platinum group metal (PGM), which at least one particulate metal oxide does not act as a support for any other catalytic component; or (b) a component capable of trapping and/or alloying with gas phase PGM.
Abstract:
The present invention relates to a process for the production of a zeolitic material having a BEA-type framework structure comprising YO 2 and X 2 O 3 , wherein said process comprises the steps of (1) preparing a mixture comprising one or more sources for YO 2 , one or more sources for X 2 O 3 , and seed crystals comprising one or more zeolitic materials having a BEA-type framework structure; (2) crystallizing the mixture obtained in step (1); and (3) subjecting the zeolitic material having a BEA-type framework structure obtained in step (2) to an ion-exchange procedure with Cu and/or Fe; wherein Y is a tetravalent element, and X is a trivaient element, wherein the mixture provided in step (1) and crystallized in step (2) does not contain an organotemplate as structure-directing agent, and wherein the total amount of Cu and/or Fe in the ion-exchanged material obtained in step (3) ranges from 0.1 to 25 wt.-% calculated as Fe 2 O 3 and CuO, as well as to a zeolitic material having a BEA-type framework structure which may be obtained according to said process, and to a method for the treatment of NO x by selective catalytic reduction (SCR) using said zeolitic material.
Abstract translation:本发明涉及一种生产具有包含YO 2和X 2 O 3的BEA型骨架结构的沸石材料的方法,其中所述方法包括以下步骤:(1)制备包含一种或多种Y 2 O 2源,一种或多种 X2O3的来源,以及包含一种或多种具有BEA型骨架结构的沸石材料的晶种; (2)使步骤(1)中获得的混合物结晶; 和(3)使具有步骤(2)中获得的BEA型骨架结构的沸石材料与Cu和/或Fe进行离子交换程序; 其中Y是四价元素,X是三元素,其中在步骤(1)中提供并在步骤(2)中结晶的混合物不含作为结构导向剂的有机模板,并且其中Cu和/ 在步骤(3)中获得的离子交换材料中的Fe或Fe按照Fe 2 O 3和CuO计算为0.1至25重量%,以及具有BEA型骨架结构的沸石材料,其可以根据所述 方法以及使用所述沸石材料通过选择性催化还原(SCR)处理NOx的方法。
Abstract:
A system for filtering particulate matter (PM) from exhaust gas emitted from a positive ignition engine or a compression ignition engine, said system comprising a filter having inlet surfaces, outlet surfaces, and a porous structure between the inlet surfaces and the outlet surfaces; a selective catalytic reduction (SCR) washcoat com¬ prising a small pore zeolite promoted with at least one metal select¬ ed from the group consisting of Cr, Co, Cu, Fe, Hf, La, Ce, In, V, Mn, Ni, Zn, Ga, Ag, Au, Pt, Pd and Rh, wherein the washcoat provides a wash- coated filter for filtering the particulate matter; and a NOx absorber disposed upstream of the washcoat.