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Dual-function catalyst applied to isomerization of C8 aromatic hydrocarbon and preparation method of dual-function catalyst

A dual-function catalyst, the technology of aromatic hydrocarbon isomerization, applied in the direction of isomerization to hydrocarbon, carbon compound catalyst, physical/chemical process catalyst, etc., can solve the problems of no performance, high xylene loss rate, poor catalyst selectivity, etc.

Active Publication Date: 2018-12-21
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

While catalysts based on ZSM-5 zeolite, which can be used alone or in combination with other zeolites such as mordenite, do not provide the best performance
[0006] CN1901991A discloses a kind of C 8 Aromatics isomerization catalyst, using MTW type zeolite or low silica ZSM-12 as the acidic component, platinum and germanium as active metal components, when the above catalyst is applied to the isomerization of C8 aromatics, although the conversion rate of ethylbenzene is relatively low High, but the loss rate of xylene is high, indicating that there are many side reactions, the selectivity of the catalyst is poor, and the p-xylene in the product stream has not reached the equilibrium quantity
[0010] The EUO structure molecular sieve preparation methods disclosed in the above documents mainly include traditional hydrothermal method and solid-phase in-situ method, but the molecular sieve structure is basically the same, its particle size is generally large, all in the micron level, and miscellaneous crystals are prone to appear. The lifespan is severely limited, and the product yield needs to be improved

Method used

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  • Dual-function catalyst applied to isomerization of C8 aromatic hydrocarbon and preparation method of dual-function catalyst
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  • Dual-function catalyst applied to isomerization of C8 aromatic hydrocarbon and preparation method of dual-function catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0068] Example 1: Preparation of EU-1 molecular sieve with hierarchically porous EUO structure:

[0069] Weigh a certain amount of cetyltrimethoxysilane and dissolve it in methanol to form a solution and stir to disperse to form a solution of cetyltrimethoxysilane; then add a quantitative amount of cetyltrimethoxysilane to the solution of cetyltrimethoxysilane Water glass, NaOH, 1,6-bis(N-methylpyrrolium)hexane and deionized water H 2 O, stirred at 40°C for 6 hours to obtain a silicon source mixed solution; at 60°C, put a quantitative amount of pseudo-boehmite into the silicon source mixed solution, stirred vigorously for 90 minutes, and aged at room temperature for 12 Obtain mixture mixed sol in hour, mixed sol is used as crystallization precursor mixture, and its composition is:

[0070] Na 2 O:SiO 2 :Al 2 o 3 :LCS:OSDA:H 2 O=0.072:1:0.0342:0.0247:0.12:45;

[0071] The obtained mixed sol was placed in a crystallization kettle, and crystallized at 170°C, wherein the he...

Embodiment 2~8

[0077] Examples 2-8: Preparation of EU-1 molecular sieve with hierarchical EUO structure:

[0078] Using the same synthetic method as in Example 1 to synthesize EU-1 molecular sieve with multi-level porous EUO structure, the selected silicon source, aluminum source, long-chain organosilane, double quaternary ammonium salt template type and feeding ratio, heating rate , crystallization temperature, crystallization time and other parameter selections, refer to Table 2; the names of the molecular sieve samples prepared in Examples 2-8 are respectively marked as A~H, and their physical and chemical properties are as shown in Table 3:

[0079] Table 2: Selection of parameters in the EU-1 molecular sieve synthesis method in the examples

[0080]

[0081] Table 3: Physical and chemical properties of EU-1 molecular sieve products synthesized in Examples and Comparative Examples

[0082] Numbering

Embodiment 9~16

[0083] Embodiment 9~16: preparation bifunctional catalyst:

[0084] Kneading molding: 20.00 g of the molecular sieves prepared in Examples 1 to 5 and Comparative Examples 1 to 3 were respectively pressed by molecular sieve and Al 2 o 3 The ratio of dry mass proportioning 30:70 and the pseudo-boehmite powder of 59.51g (produced by Shandong Aluminum Factory, A1 2 o 3 The content is 78.4wt%), 2.0g of turnip powder, and 30g of 2.0wt% citric acid aqueous solution were mixed uniformly, extruded, dried at 120°C for 12h, and then calcined at 550°C for 4h to obtain the initial carrier.

[0085] Ion exchange: Take 25.0g of the above initial carrier and 250g of NH with a concentration of 1.0mol / L 4 The Cl aqueous solution was subjected to ion exchange at 90°C under continuous stirring for 3 hours, and the exchange was repeated twice, washed with deionized water until there was no chloride ion, filtered and recovered, then the particles were dried at 110°C for 12 hours, and finally cal...

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Abstract

The invention discloses a dual-function catalyst applied to isomerization of C8 aromatic hydrocarbons and a preparation method of the dual-function catalyst. The catalyst is prepared from the following components: 10-89.9wt% of H type hierarchical-pore structure EUO molecular sieve, 9.9-89.9wt% of matrix and 0.01-2.0wt% of metal active component. The preparation method comprises the following steps: mixing the hierarchical-pore EUO molecular sieve, the matrix and a pore-enlarging agent, then adding an acid solution, kneading and forming, drying and roasting to remove the components such as thepore-enlarging agent to form a carrier, then dipping the carrier in a mixed solution containing metal salt and activating to obtain a formed catalyst. The hierarchical-pore EUO molecular sieve is crystallized and synthesized by taking a long-chain silane compound as a crystallization promoting agent and taking biquaternary ammonium salt with an alkane structure substituted by a di-penta-heterocycle group as an organic template agent. The catalyst shows favorable activity and selectivity in hydroisomerization reaction of C8 aromatic hydrocarbon and has a good industrial application prospect and a good economic value.

Description

technical field [0001] The invention relates to a bifunctional catalyst for the isomerization of C8 aromatic hydrocarbons and a preparation method thereof, belonging to the field of preparation of inorganic catalytic materials. Background technique [0002] C 8 Aromatics are a mixture of p-, m-, ortho-xylene and ethylbenzene, which can be obtained from catalytic reforming, petroleum cracking and other processes, among which p-xylene (PX) and o-xylene (OX) are important chemical raw materials , such as the basic raw material for polyester and phthalic anhydride. With the development of these industries, the demand for PX and OX is increasing rapidly. At present, the process technology for increasing the production of PX and OX is mainly xylene isomerization, which is an important means to convert m-xylene and ethylbenzene with low utilization value into PX and OX. Since the boiling points of ethylbenzene and xylene are very close, the separation is difficult, resulting in ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/74C07C5/27C07C15/08
CPCB01J29/7446C07C5/2737C07C5/2775C07C2529/74C07C15/08Y02P20/52
Inventor 王志光王建青李进
Owner CHINA CATALYST HLDG CO LTD
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