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Titanium silicon molecular sieve, preparation method and application thereof and phenol hydroxylation method

A titanium-silicon molecular sieve and molecular sieve technology, applied in the field of molecular sieves, can solve the problems of occupying land resources and storage space, and achieve good catalytic effects

Active Publication Date: 2019-04-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this way, valuable land resources and storage space are taken up, and the recovery and utilization technology development of deactivated ammoximation catalysts is urgently needed

Method used

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  • Titanium silicon molecular sieve, preparation method and application thereof and phenol hydroxylation method
  • Titanium silicon molecular sieve, preparation method and application thereof and phenol hydroxylation method
  • Titanium silicon molecular sieve, preparation method and application thereof and phenol hydroxylation method

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preparation example Construction

[0028] The present invention also provides a preparation method of a titanium-silicon molecular sieve, the method comprising:

[0029] (1) Mix the catalyst containing titanium-silicon molecular sieve with the first heat treatment liquid, then perform the first heat treatment, and then separate to obtain the first solid, the first heat treatment liquid is an acid solution with a concentration>0.1mol / L, and the first heat treatment liquid is an acid solution with a concentration>0.1mol / L. 1. The temperature of heat treatment is 10-200°C, preferably, the time is 0.5-36h;

[0030] (2) Mix the first solid with the second treatment liquid, and then perform the second heat treatment, the second treatment liquid contains titanium source, silicon source, alkali source and water, the temperature of the second heat treatment is 100- 200°C, preferably, the time is 6-96h;

[0031] Among them, SiO 2 In other words, the molar ratio of the catalyst containing titanium-silicon molecular sieve ...

Embodiment approach

[0050] According to a preferred embodiment of the present invention, the maintenance time of the preferred stage (1) is 2-24 hours, preferably 4-16 hours; the maintenance time of the stage (2) is 0.1-12 hours, preferably 2-6 hours ; The maintenance time of stage (3) is 4-24 hours, preferably 4-12 hours.

[0051] According to the method provided by the present invention, preferably, with SiO 2 In other words, the molar ratio of the catalyst containing titanium-silicon molecular sieve in step (1) to the silicon source in step (2) is 100:(1-15), more preferably 100:(4-10). Adopting the preferred embodiment of the present invention is more conducive to adjusting the micropore size distribution of the prepared titanium-silicon molecular sieve, and enables the prepared titanium-silicon molecular sieve to be used in the phenol hydroxylation reaction process to obtain a more stable catalytic effect.

[0052] According to the method of the present invention, preferably, the method of ...

Embodiment 1

[0102] This example illustrates the methods and products provided by the invention.

[0103] At normal temperature (20°C, the rest of the comparative examples are the same as the examples) and normal pressure (0.1MPa, the rest of the comparative examples are the same as the examples), the deactivated cyclohexanone oximation catalyst SH-1 was mixed with 1mol / L hydrochloric acid The aqueous solution was mixed and beaten, and then the mixed slurry was mixed and stirred at 80°C for 12 hours; after solid-liquid separation, the solid, silicon-sourced ethyl orthosilicate, titanium-sourced titanium sulfate and sodium hydroxide aqueous solution (pH 12) were mixed and mixed Put the liquid into a stainless steel sealed reaction kettle, and treat it at 170°C for 12 hours, wherein, the molar composition of the material is an inactivated cyclohexanone oximation catalyst: silicon source: titanium source: acid: alkali: water = 100:5:1:10 :5:250, deactivated cyclohexanone oximation catalyst wi...

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Abstract

The invention relates to the field of molecular sieves, and discloses a titanium silicon molecular sieve, preparation method and application thereof and a phenol hydroxylation method. The molecular sieve comprises titanium element, silicon element and oxygen element, and meet the formula that X(1-1.8) / X(0.4-0.9) equals to C, wherein C is more than 0.1 and less than 0.9, optimally C is more than 0.15 and less than 0.7; X(0.4-0.9) is the proportion of the micropore diameter of the molecular sieve accounting for the total microporous diameter distribution in the range of 0.4-0.9nm, and X(1-1.8) is the proportion of the micropore diameter of the molecular sieve accounting for the total microporous diameter distribution in the range of 1-1.8nm. The titanium silicon molecular sieve has a specialphysicochemical characteristic structure, is favorable to improving the phenol conversion rate and modulating the selectivity of a target product hydroquinone in the phenol hydroxylation.

Description

technical field [0001] The invention relates to the field of molecular sieves, in particular to a titanium-silicon molecular sieve, a preparation method of the titanium-silicon molecular sieve, an application of the titanium-silicon molecular sieve in a phenol hydroxylation reaction and a phenol hydroxylation method. Background technique [0002] Titanium-silicon molecular sieve is a molecular sieve whose skeleton is composed of silicon, titanium and oxygen elements, and has broad application prospects in petroleum refining and petrochemical industry. Among them, TS-1 molecular sieve is a new type of titanium-silicon molecular sieve with excellent catalytic selective oxidation performance formed by introducing transition metal element titanium into the molecular sieve framework with ZSM-5 structure. [0003] TS-1 not only has the catalytic oxidation of titanium, but also has the shape-selective effect and excellent stability of ZSM-5 molecular sieve, and has successfully rea...

Claims

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Application Information

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IPC IPC(8): C01B39/08B82Y30/00B82Y40/00B01J29/88C07C37/60C07C39/08
CPCB01J29/88B82Y30/00B82Y40/00C01B39/08C07C37/60C07C39/08Y02P20/52
Inventor 史春风林民朱斌
Owner CHINA PETROLEUM & CHEM CORP