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In Situ Synthesis of Olefin Hydration Molecular Sieve Catalysts with MFI Structure

An in-situ synthesis and olefin hydration technology, which is applied in molecular sieve catalysts, molecular sieves and base exchange compounds, chemical instruments and methods, etc., can solve the problem of in-situ synthesis of olefin hydration catalyst preparation methods report few reports, catalyst activity and stability decline, catalyst problems such as the loss of sulfonic acid groups, to achieve the effect of suitable grain size, reduced catalyst cost, high catalytic activity and selectivity

Inactive Publication Date: 2019-07-30
HAO HUA CHENGDU TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The traditional process of olefin hydration adopts sulfuric acid indirect hydration method, which was gradually eliminated due to equipment corrosion and waste acid treatment problems. After that, Texaco Company of the United States developed a medium-pressure, low-temperature direct hydration method using strong acidic cation exchange resin as a catalyst. Preparation of isopropanol by hydration method can obtain higher conversion rate of propylene and selectivity of isopropanol, but the catalyst has poor thermal stability, the use temperature must be lower than 175°C, and the catalyst has the problem of loss of sulfonic acid groups; China Patent CN1245738A developed a zeolite molecular sieve olefin hydration catalyst. Zeolite molecular sieve is a solid acid that does not cause acid loss. Therefore, this molecular sieve catalyst overcomes the shortcomings of resin catalysts and successfully solves the problem of catalyst thermal stability. However, the zeolite molecular sieve The catalyst must undergo ion exchange and metal element solution impregnation, the preparation process is complicated, and this will destroy the molecular sieve lattice, thereby forming a skeleton defect, which will eventually lead to a decrease in the activity and stability of the catalyst. If it is frequently regenerated, its skeleton structure will also be destroyed. service life
[0005] In recent years, with the continuous breakthrough of in-situ synthesis technology, the use of in-situ synthesis technology to improve the performance of catalysts has been valued by various research units, but there are few reports on the preparation methods of in-situ synthesis of olefin hydration catalysts.

Method used

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  • In Situ Synthesis of Olefin Hydration Molecular Sieve Catalysts with MFI Structure

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Component content: in parts by weight, get 400 parts of silica sol, 500 parts of deionized water, 20 parts of tetrapropylammonium hydroxide and Al 2 o 3 The number of moles is SiO in silica sol 2 1 / 50 of the molar number of aluminum nitrate, the inorganic alkali solution is sodium hydroxide solution.

[0054] (1) Add 500 parts of deionized water to 400 parts of silica sol for dilution and stir evenly, then add 20 parts of tetrapropylammonium hydroxide dropwise to obtain the first solution;

[0055] (2) In the first solution, aluminum nitrate is added dropwise, and an aqueous solution containing 10 parts of phosphoric acid and 0.3 part of palladium chloride is added simultaneously, and the mixture is evenly stirred to obtain the second solution;

[0056] (3) adding an appropriate amount of sodium hydroxide solution to the second solution to adjust the pH value to 13.0 to obtain a third solution;

[0057] (4) Add the third solution into the autoclave, stir continuously...

Embodiment 2

[0061] Component content: in parts by weight, get 312.5 parts of ethyl orthosilicate, 200 parts of deionized water, 5 parts of tetrabutylammonium hydroxide and Al 2 o 3 The number of moles is SiO in silica sol 2 1 / 25 of the molar amount of aluminum chloride, hydrochloric acid is selected as the inorganic acid solution.

[0062] (1) Add 200 parts of deionized water to 312.5 parts of ethyl orthosilicate to dilute and stir evenly, then add 5 parts of tetrabutylammonium hydroxide dropwise to obtain the first solution;

[0063] (2) Add aluminum chloride dropwise to the first solution, and simultaneously add an aqueous solution containing 40 parts of copper nitrate and 1 part of germanium nitrate, and stir evenly to obtain the second solution;

[0064] (3) adding an appropriate amount of hydrochloric acid to the second solution to adjust the pH value to 10.0 to obtain a third solution;

[0065] (4) Add the third solution into the autoclave, stir continuously at 60°C and crystalli...

Embodiment 3

[0069] Component content: in parts by weight, get 312.5 parts of ethyl orthosilicate, 400 parts of deionized water, 15 parts of tetraethylammonium hydroxide and Al 2 o 3 The number of moles is SiO in silica sol 2 The aluminum nitrate of 1 / 80 of the molar number, and the inorganic alkali solution is potassium hydroxide solution.

[0070] (1) Add 400 parts of deionized water to 312.5 parts of ethyl orthosilicate to dilute and stir evenly, then add 15 parts of tetraethylammonium hydroxide dropwise to obtain the first solution;

[0071] (2) Add aluminum nitrate dropwise to the first solution, and simultaneously add an aqueous solution containing 5 parts of lanthanum nitrate, and stir evenly to obtain the second solution;

[0072] (3) adding an appropriate amount of sodium bicarbonate solution to the second solution to adjust the pH value to 10.0 to obtain a third solution;

[0073] (4) Add the third solution into the autoclave, stir continuously at 150° C. and crystallize for 1...

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Abstract

The invention discloses an in-situ synthesizing method for an olefin-hydration molecular sieve based catalyst. The catalyst is a mixed element modified molecular sieve based catalyst with an MFI structure. A mixed element modifier, namely a water solution containing at least one element of Cu, P, La, Ge, Pd and Nb, is utilized as a modifying source to be introduced into a hydrothermal synthesis system prepared from a silicon source, an aluminum source, a template, alkali and distilled water to react to prepare an in-situ modified molecular sieve. According to a preparation method disclosed bythe invention, a disposable in-situ synthesizing technology is utilized, a synthesizing process is simplified, preparation cost is reduced, and industrial popularization is facilitated. The prepared molecular sieve based catalyst has the advantages of higher strength and stability; furthermore, the catalyst has the advantages of better low temperature activity and catalyst activity and high selectivity to lower alcohol; in addition, the service life of the catalyst is prolonged.

Description

technical field [0001] The invention belongs to the technical field of catalyst synthesis, and more specifically relates to an in-situ synthesis method of an olefin hydration molecular sieve catalyst with an MFI structure. Background technique [0002] Low carbon mixed alcohol refers to C 1 ~C 6 Alcohol mixtures, neither aromatic nor sulfur, have broad application prospects. (1) Low-carbon mixed alcohols are important chemicals and organic chemical raw materials. In recent years, the chemical application prospects of low-carbon mixed alcohols are gradually promising. Low-carbon mixed alcohols can be further separated to obtain ethyl, propylene, butanol and pentanols with higher prices. (2) Low-carbon mixed alcohols can also be directly used as clean fuels. Due to the presence of oxygen in alcohols, their combustion is more complete than that of gasoline and diesel, and CO, NO x It has less emissions and is an environmentally friendly fuel; (3) low-carbon mixed alcohol is ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/06C01B39/10C01B39/04B01J29/70C07C29/04C07C31/10
CPCB01J29/70C01B39/04C01B39/06C01B39/10C01P2002/72C07C29/04C07C31/10
Inventor 程牧曦谭亚南何霖韩伟
Owner HAO HUA CHENGDU TECH
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