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Pd/Ce-F/MCM-48 catalyst as well as preparation method and application thereof

A catalyst and reagent technology, applied in the field of Pd/Ce-F/MCM-48 catalyst and its preparation, can solve the problems of low concentration of surface acid centers and lack of catalytic oxidation reaction ability

Active Publication Date: 2022-06-17
HEILONGJIANG BAYI AGRICULTURAL UNIVERSITY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, since the MCM-48 silicon-oxygen tetrahedron is a charge balance system, there are few lattice defects in the pure silicon mesoporous molecular sieve framework, the concentration of acid centers on the surface is low, and it does not have the ability to catalyze oxidation reactions, so it usually cannot be directly used as a catalyst. Mesoporous molecular sieves are functionally modified. The most common modification method is heteroatomization for different catalytic reactions. Another important carrier modification method is to introduce anions into the molecular sieve framework. There are still few researches on the modification of catalysts, and it is still our goal to develop new catalysts by using different materials to mine catalysts with high-quality factors, understand their coordination environment and catalytic performance, and develop new catalysts.

Method used

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  • Pd/Ce-F/MCM-48 catalyst as well as preparation method and application thereof
  • Pd/Ce-F/MCM-48 catalyst as well as preparation method and application thereof
  • Pd/Ce-F/MCM-48 catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Example 1. Preparation of anion-doped mesoporous material Ce-F / MCM-48 with high degree of order

[0054] Using CTAB as a template, NaF and Ce(NO 3 ) 6H 2 O is an additive reagent, prepared by hydrothermal synthesis under alkaline conditions.

[0055] First, dissolve NaOH in deionized water and stir well, then add NaF and Ce(NO 3 ) 6H 2 Stir for 30min, add CTAB to the mixture in small amounts and stir for 90min under heating in a water bath at 35°C, the solution is transparent at this time, and then use a 3mL long pasteurized plastic pipette to slowly add TEOS (ethyl silicate) dropwise and intermittently. In this solution, continue stirring for 60min, and the molar ratio of the reaction mixture raw materials is n(TEOS):n(CTAB):n(H 2 O):n(NaOH):n(Ce):n(NaF)=1.0:0.65:62:0.5:0.02:0.10. The prepared initial gel was transferred into a stainless steel reaction kettle lined with PTFE, and then placed in a drying oven for 72h at 110°C for constant temperature crystallizatio...

Embodiment 2

[0056] Example 2. Preparation of a catalyst supporting metal active components

[0057] In the catalyst supporting metal active components, the active component is precious metal palladium, and the carrier is the mesoporous material Ce-F / MCM-48 prepared in Example 1; the catalyst is Pd-Ce-F / MCM-48.

[0058] The catalyst was prepared by impregnation method, and the loading (mass fraction) of Pd was 0.4%. Pd was dissolved in a porcelain crucible of deionized water, and Ce-F / MCM-48-0.10 was then immersed in it. Ultrasonic dispersion at 50°C for 20min. After standing at room temperature for more than 6 hours, drying at 90°C for 4 hours on an electric hot plate, drying at 105°C for 5 hours in a drying oven, and calcining at 400°C for 4 hours, a Pd-supported catalyst was obtained, denoted as 0.4% Pd-Ce-F / MCM-48.

Embodiment 3、0

[0061] Example 3. Evaluation of catalytic reaction performance of 0.4% Pd-Ce-F / MCM-48 for catalyzing the isomerization of n-heptane

[0062] The evaluation of catalytic reaction performance was carried out on a fixed-bed micro-reaction device, and the prepared catalyst was tableted and sieved to obtain 60-80 mesh particles, which were used for later use. The filling amount is 0.3 g, which is mixed with quartz sand and then loaded into a reaction tube, and the inner diameter of the reaction tube is 6 mm. Before the reaction, the catalyst was activated in a hydrogen atmosphere at a pressure of 1.0 MPa and 300 °C for 4 h, and then cooled to a temperature in the range of 220-360 °C for modulation. The reaction evaluation process conditions are pressure n-C 7 Flow rate 6.0mL / h, n-H 2 Flow rate 30mL / min, MHSV is 7.6h -1 . Sampling was started after 30 minutes of stability, and the product was separated by a chromatographic column and analyzed on-line with a gas chromatograph FID...

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Abstract

The invention discloses a Ce-F / MCM-48 mesoporous material and a Pd catalyst with the Ce-F / MCM-48 mesoporous material as a carrier. According to the invention, Ce-F / MCM-48 is synthesized by using a NaF and Ce in-situ doping hydrothermal synthesis method, and the Pd-loaded Pd / Ce-F / MCM-48 bimetallic catalyst taking Ce-F / MCM-48 as a carrier is prepared by using an impregnation method. The catalytic performance of the catalyst on the n-heptane isomerization reaction is investigated. Results show that the molecular sieve prepared after NaF doping has the advantages that the specific surface area and the pore volume are increased, the pore size distribution tends to be uniform, and the acidity is mild and moderate. When the optimal loading capacity of the noble metal Pd is 0.4% by mass, the reaction temperature is 280 DEG C and the reaction time is 120 min, the catalytic performance is relatively stable, the conversion rate of n-heptane isomerization is 79.7%, and the selectivity of isoheptane is 91.5%. The catalyst is expected to be an important catalyst for hydroisomerization of n-heptane.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and in particular relates to a Pd / Ce-F / MCM-48 catalyst and a preparation method and application thereof. Background technique [0002] The quality upgrade of FCC gasoline will be the main problem that my country must face and solve in the next few years. Converting straight-chain alkanes to branched-chain alkanes is the most important means to ensure gasoline octane number. Therefore, the preparation of heptane isomerization catalysts has also attracted much attention. At present, most of the heptane isomerization catalysts are prepared by supported metal catalysts. The properties of the support have a great influence on the catalyst. In the preparation of support materials, scientists from Mobil Corporation first reported the synthesis of M41S in the early 1990s [BeckJ S, Vartuli J C, Roth W J, et al. A new family of mesoporous molecular sieves prepared with liquid crystal templates[J].J.am...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/03B01J37/02B01J37/10C07C5/27C07C9/16
CPCB01J29/0308B01J29/0325B01J37/0201B01J37/10C07C5/2775C07C5/2791B01J2229/20B01J2229/40C07C9/16Y02P20/584
Inventor 崔艳红王彦宏汪颖军孙鹏所艳华张微卢志涛
Owner HEILONGJIANG BAYI AGRICULTURAL UNIVERSITY
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