Method for simultaneously producing hydroquinone and catechol
A technology for hydroquinone and catechol, which is applied in the field of simultaneous production of hydroquinone and catechol, can solve the problems of high content of benzoquinone and needs to be further improved, and achieves that the preparation method is simple and easy to popularize. Application, Environmentally Friendly Effects
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[0022] According to one embodiment of the present invention, the preparation method of the catalyst may include: contacting the heteroatom molecular sieve with a solution containing the zinc compound, loading the solution on the heteroatom molecular sieve and drying, The raw material containing the zinc compound and the heteroatom molecular sieve is obtained, and the raw material is calcined, so as to obtain the catalyst used in the method according to the present invention.
[0023] According to the present invention, the solvent of the solution containing the zinc compound may be various solvents capable of dissolving the zinc compound. According to the present invention, the zinc compound is usually soluble in water, and from the viewpoints of environmental protection and energy saving, the solvent is preferably water.
[0024] According to the present invention, the method of contacting the heteroatom molecular sieve with the solution containing the zinc compound can be a ...
Embodiment 1
[0049] This example is used to illustrate the method for simultaneous production of hydroquinone and catechol according to the present invention.
[0050] Mix 10g of zinc oxide with 50g of titanium-silicon molecular sieve (the titanium-silicon molecular sieve is TS-1 titanium-silicon molecular sieve, wherein the molar ratio of silicon atoms to titanium atoms is 56:1), and the obtained mixture is heated in an air atmosphere at 550° C. Calcined at a temperature of 5 hours to obtain catalyst A. In the catalyst A, the molar ratio of zinc atoms to titanium atoms is 5:1.
[0051] Phenol, hydrogen peroxide, methanol and catalyst A were reacted in an autoclave at a temperature of 30° C. and a pressure of 1.2 MPa for 2 hours. Wherein, the molar ratio of phenol to hydrogen peroxide is 1:2, the mass ratio of methanol to catalyst A is 20:1, and the mass ratio of phenol to catalyst A is 10:1. After 2 hours of reaction, the results were as follows: the conversion rate of phenol was 68%, t...
Embodiment 2
[0053] This example is used to illustrate the method for simultaneous production of hydroquinone and catechol according to the present invention.
[0054] Take by weighing 20g titanium-silicon molecular sieve (this titanium-silicon molecular sieve is TS-1 titanium-silicon molecular sieve, wherein, the molar ratio of silicon atom and titanium atom is 39: 1), with the aqueous solution of 20 milliliters of zinc carbonates (containing 2g zinc carbonate) at 25 The titanium-silicon molecular sieve was impregnated at 25° C. for 2 hours, dried at 25° C. for 10 hours, and then calcined at 650° C. for 2 hours in an air atmosphere to obtain catalyst B. In this catalyst B, the molar ratio of zinc atoms to titanium atoms is 2:1.
[0055] Phenol, hydrogen peroxide, acetone and catalyst B were reacted in an autoclave at a temperature of 60° C. and a pressure of 2 MPa for 2 hours. Wherein, the molar ratio of phenol to hydrogen peroxide is 1:1, the mass ratio of acetone to catalyst B is 5:1, ...
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Abstract
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