Catalyst for synthesizing p-hydroxybenzonitrile (2-hydroxybenzonitrile) and preparation method of catalyst

A technology for hydroxybenzonitrile and methyl hydroxybenzoate is applied in the preparation of catalysts, the catalyst for synthesizing p-hydroxybenzonitrile and the field of preparation thereof, and can solve the problems of complicated operation process, high reaction pressure, many reaction steps and the like, Achieve the effects of high product selectivity, high raw material conversion rate and simple process

Active Publication Date: 2017-05-24
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] There are many synthetic methods of hydroxybenzonitrile, which can be divided into hydroxybenzoic acid dehydration ammoniation method, hydroxybenzaldehyde ammoniation method, diazonium salt method, p-cresol method and p-cresol sodium method according to different raw materials: Benzoic acid dehydration ammonification method usually obtains p-hydroxybenzonitrile by ammoxidation reaction of p-cresol in a fluidized bed. Although the process adopts a fluidized bed continuous reaction, under the reaction conditions, a higher The reaction temperature obtains a lower p-hydroxybenzonitrile yield, and the yield is only 50 to 65%, and the unsafety of the reaction system is increased due to the existence of oxygen in the reaction process
Hydroxybenzaldehyde ammonification method adopts p-hydroxybenzaldehyde and hydroxylamine hydrochloride to prepare p-hydroxybenzonitrile under the effect of tungsten catalyst, but in this reaction process, the catalyst consumption is too large, which is about 9% of the raw material p-hydroxybenzaldehyde amount times, and the reaction process is slow; at the same time, the most important thing is that the process adopts the batch reaction form, which further restricts the large-scale production requirements
The diazonium salt method, the p-cresol method and the sodium p-cresol method, etc. basically adopt a batch reaction, which is not suitable for large-scale continuous production, and the reaction pressure is also high, which increases the investment in equipment; in addition, the reaction There are many steps and complicated operation process, which limits the large-scale production of p-hydroxybenzonitrile
[0004] Therefore, in the process of synthesizing p-(o)hydroxybenzonitrile, the continuous production mode that simplifies the reaction steps, reduces the process flow, reduces equipment requirements, and reduces the discharge of three wastes is urgently needed for industrial production; but it limits the success of this continuous production mode The main factor is the lack of a catalyst suitable for this mode with good stability, good selectivity and high yield

Method used

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Experimental program
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Effect test

Embodiment 1

[0032] A kind of catalyst that is used for synthesizing p-(ortho) hydroxybenzonitrile is prepared by following method:

[0033] (1) Preparation of strip-shaped all-silicon molecular sieve: mix 50g Silicalite-1 former powder and 2g Tianqing powder evenly, add in 29g silica sol solution (silicon dioxide mass fraction is 30%), knead after fully mixing, and then use Extrude into a cylindrical shape with a diameter of φ3mm; put the cylindrical product in an oven and dry it at 90°C for 12 hours, and then roast it in a muffle furnace at 500°C for 6 hours to obtain a strip-shaped all-silicon molecular sieve;

[0034] (2) load active components: 5.28g phosphoric acid (mass fraction is 85%), 0.91g copper nitrate, 1.46g stannous oxalate and 2.58g ammonium molybdate are dissolved in 45g deionized water and are prepared into impregnating solution, step ( 1) The obtained strip-shaped all-silicon molecular sieve is immersed in the active component solution for 24 hours at room temperature; ...

Embodiment 2

[0038] The preparation method of embodiment 2 is substantially the same as embodiment 1, and difference is that the add-on of phosphoric acid (massfraction is 85%) is 2.03g in the step (2), and the prepared catalyst mark is CP-2, through X After detection by the fluorescence spectrometer, it is known that each active component accounts for the mass percentage of the carrier as P 2 o 5 2.5%, CuO 0.6%, SnO 1.9%, MoO 3 0.6%.

Embodiment 3

[0040] The preparation method of embodiment 3 is substantially the same as embodiment 1, and difference is that the add-on of phosphoric acid (massfraction is 85%) is 6.50g in the step (2), and the prepared catalyst mark is CP-3, through X After detection by the fluorescence spectrometer, it is known that each active component accounts for the mass percentage of the carrier as P 2 o 5 8%, CuO 0.6%, SnO 1.9%, MoO 3 0.6%.

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Abstract

The invention discloses a catalyst for synthesizing p-hydroxybenzonitrile (2-hydroxybenzonitrile) and a preparation method of the catalyst. Phosphoric acid, copper nitrate, stannous oxalate and ammonium molybdate are dissolved in deionized water, an impregnation liquid is prepared, and a bar-shaped Silicalite-1 molecular sieve is impregnated in the impregnation liquid for 12-24 h at the room temperature; the impregnated molecular sieve is dried in a drying oven at 80-120 DEG C for 6-24 h and roasted in a muffle furnace at 450-600 DEG C for 4-12 h, and the catalyst is obtained. The catalyst is prepared from active components in terms of the mass percentage of the carrier as follows: 0.5-15% of P2O5, 0.1%-3.0% of CuO, 0.5%-4.5% of SnO and 0.2%-2% of MoO3. The catalyst is prepared with a conventional impregnation method, and the technological process is simple and easy to operate; the all-silicon molecular sieve is used as an active carrier and has a synergistic effect with all active oxide components, and the prepared catalyst is applicable to the continuous production process of p-hydroxybenzonitrile (2-hydroxybenzonitrile) by use of a fixed bed reactor and has the advantages of high raw material conversion rate, high product selectivity and long service life in the p-hydroxybenzonitrile (2-hydroxybenzonitrile) synthesis process.

Description

technical field [0001] The invention relates to a preparation method of a catalyst, in particular to a catalyst for synthesizing p-(o)hydroxybenzonitrile and a preparation method thereof, belonging to the technical field of chemical industry. Background technique [0002] p-Hydroxybenzonitrile, also known as p-cyanophenol, p-hydroxybenzonitrile, etc., is an extremely important fine organic chemical raw material and intermediate, widely used in the synthesis of various medicines, spices, pesticides, liquid crystal materials and buffers Agents, etc., especially as pesticide intermediates, can be used to synthesize a variety of pesticides such as "fenonitrile", "benzonilphos", "bromoxynil", "hydroxychlorenil" and "chlorothalonil". With the development of my country's agricultural modernization, the demand for pesticides has increased significantly, and the demand for p-hydroxybenzonitrile has also increased significantly. O-hydroxybenzonitrile, also known as salicylonitrile, c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/035C07C253/22C07C255/53
Inventor 李进李永宾王建青王庆吉严继业
Owner CHINA CATALYST HLDG CO LTD
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