摘要:
Disclosed is a reactive filter, that is a selective catalytic reduction filter or an oxidative reaction filter, including a porous substrate including internal pores having their inner surface, totally or partially, directly coated with a catalytic zeolite material resulting from an in situ hydrothermal synthesis. Also disclosed is a process for preparing such a reactive filter and the use thereof in an engine exhaust depolluting system.
摘要:
A method for the transalkylation of a heavy reformate is provided. The heavy reformate is contacted with a transalkylation catalyst and hydrogen gas in a transalkylation reactor to selectively convert the heavy reformate to a xylenes-rich product stream. Light alkanes produced during the reaction can be supplied to a steam cracker where they are converted to light olefins.
摘要:
The present invention relates to an improved process for the production of conjugated polyunsaturated fatty acids (PUFA), preferably conjugated linoleic acid (CLA), using finely dispersed heterogeneous metal catalysts on a mesoporous support, in the absence of Hg. The present invention also relates to a method to increase the large microporosity and (optionally) the small mesoporosity of a zeolite, thus obtaining a modified zeolite having a large and highly accessible internal surface.
摘要:
A honeycomb structure includes a honeycomb unit containing a zeolite and an inorganic binder and having plural separating walls disposed in the longitudinal direction of the honeycomb unit, defining plural through-holes separated by the separating walls. The zeolite includes a first zeolite ion-exchanged with one or more kinds of metal selected from the group consisting of Cu, Mn, Ag, and V, and a second zeolite ion-exchanged with one or more kinds of metal selected from the group consisting of Fe, Ti, and Co. The ratio of the first zeolite by weight to a total weight of the first and second zeolites is greater at a center of the separating wall than at a surface thereof. The ratio of the second zeolite by weight to the total weight of the first and second zeolites is greater at the surface of the separating wall than at the center thereof.
摘要:
The present disclosure relates to a naphtha reforming process for obtaining reformed naphtha comprising contacting naphtha with a catalyst, the catalyst comprising a chloride free zeolite coated alumina support impregnated with 0.01 wt % to 0.5 wt % active metal and 0.01 wt % to 0.5 wt % promoter metal, wherein the thickness of the zeolite coating on the alumina support ranges from 100 μm to 200 μm, which results in formation of reformed products of naphtha and ethylbenzene formed in-situ.
摘要:
The present disclosure relates to a naphtha reforming process for obtaining reformed naphtha comprising contacting naphtha with a catalyst, the catalyst comprising a chloride free zeolite coated alumina support impregnated with 0.01 wt % to 0.5 wt % active metal and 0.01 wt % to 0.5 wt % promoter metal, wherein the thickness of the zeolite coating on the alumina support ranges from 100 μm to 200 μm, which results in formation of reformed products of naphtha and ethylbenzene formed in-situ.
摘要:
The present invention relates to a catalyst for glycerin dehydration, a preparation method thereof, and a preparation method of acrolein. The catalyst for glycerin dehydration exhibits a high glycerin conversion ratio, minimizes by-product formation to improve acrolein selectivity, and also maintains high catalytic activity during reaction.
摘要:
The present invention provides a process for producing propylene, comprising contacting at least one of raw material selected from the group consisting of ethylene and ethanol with a catalyst containing a medium pore diameter zeolite in a fluidized bed reactor wherein the catalyst containing the medium pore diameter zeolite satisfies the following (a) through (e): (a) a particle diameter of catalyst particles at 90% by weight or more is within a range of 10 to 197 µm; (b) a bulk density of the catalyst particles is within a range of 0.7 to 1.1 g/cm 3 ; (c) a mean compressive strength of the catalyst particles having a particle diameter within a range of 30 to 70 µm is 15 MPa or more, and a compressive strength of the catalyst particles at 90% by weight or more is 10 MPa or more; (d) an angle of repose is 20 to 30°; and (e) a pore volume of pores having a pore radius within a range of 2000 to 20000 nm is 0.050 cc/g or less,
摘要:
A catalyst for converting hydrocarbons, which catalyst contains, based on the weight of the catalyst, 1-60% by weight of a zeolite, 0.1-10% by weight of an assistant catalytic component, 5-98% by weight of a thermotolerant inorganic oxide, and 0-70% by weight of a clay in terms of the oxide. Said zeolite is a MFI-structured zeolite containing phosphor and transition metal(s) or a mixture of said zeolite and a macroporous zeolite, which comprises, based on the weight of the mixture, 75-100% by weight of said MFI-structured zeolite containing phosphor and transition metal(s) and 0-25% by weight of the macroporous zeolite. In terms of the mass of the oxide, said MFI-structured zeolite containing phosphor and transition metal(s) has the following anhydrous chemical formula:
(0-0.3)Na 2 O · (0.3-5.5)Al 2 O 3 · (1.0-10)P 2 O 5 · (0.7-15)M1 x O y · (0.01-5)M2 m O n · (0-10)RE 2 O 3 · (70-97)SiO 2 I
or
(0-0.3)Na 2 O · (0.3-5)Al 2 O 3 · (1.0-10)P 2 O 5 · (0.7-15)M p O q · (0-10)RE 2 O 3 · (70-98)SiO 2 II
Said assistant catalytic component is one or more selected from the group consisting of the alkali earth metals, Group IVB metals, non-noble metals of Group VIII, and rare earth metals of the Periodic Table of the Elements. This catalyst has a higher ability to convert petroleum hydrocarbons and higher yields for propylene, ethylene, and light aromatics.
摘要翻译:一种用于烃转化催化剂,其催化剂含有,基于催化剂的重量,按重量计的沸石的1-60%(重量)的辅助催化剂成分的0.1-10%(重量)的耐热无机的5-98% 氧化物,并且在氧化物换算为0-70重量%的粘土。 所述沸石是MFI结构的沸石含磷和过渡金属(S)或所述沸石的混合物和大孔沸石,其包括,基于所述混合物的重量,重量的所述MFI结构沸石的75-100% 按重量计大孔沸石的含有磷和过渡金属(S)和0-25%。 在该氧化物的质量换算,说MFI结构沸石含磷和过渡金属(一个或多个)具有以下无水化学式:€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ(0-0.3) 的Na 2 O·(0.3-5.5)的Al 2 O 3·(1.0-10)P 2 O 5·(0.7-15)米1×○ÿ·(0.01-5)M2 M O对N·(0-10)RE 2 O 3·(70-97)的SiO 2€€ƒƒƒ€€€ƒƒi或ƒ€€€ƒƒƒ€€€ƒƒƒ€€ƒ(0-0.3)的Na 2 O·(0.3- 5)的Al 2 O 3·(1.0-10)p 2 O 5·(0.7-15)M p 2 O q·(0-10)RE 2 O 3·(70-98)的SiO 2€€ƒƒƒ€ €ƒ€ƒII说帮手催化成分是一种或选自碱土金属的多个所选择的,IVB族金属,第VIII族的非贵金属,和元素周期表的稀土金属。 该催化剂具有转换石油烃和更高的产量为丙烯,乙烯和轻质芳烃更高的能力。