A kind of method of producing guaiacol
A technology based on guaiacol and all the way, which is applied in the field of gas-phase catalytic synthesis of guaiacol, and can solve problems such as carbon deposition
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Embodiment 1
[0026] 1) Reaction device
[0027] Stainless steel fixed bed reactor, inner diameter 2000mm, filled with 5m3 Alpha-alumina balls. Part of the feed liquid phase methanol is vaporized through a vaporizer and then enters the catechol saturation column. The catechol is added and vaporized in the catechol saturation tower, mixed with methanol vapor, and the gas-phase compound is heated to the reaction temperature through the superheater and then enters the reactor.
[0028] 2) Method for adding catalytic components
[0029] The catalytic component is trimethyl phosphate. Part of the feed liquid phase methanol is vaporized through the vaporizer and then enters the trimethyl phosphate vaporizer. Trimethyl phosphate is added and vaporized in a trimethyl phosphate vaporizer, mixed with methanol vapor, and the gas-phase compound is heated to the reaction temperature through a superheater and then enters the reactor. The weight ratio of the feed liquid is: catechol:methanol=1:1.
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Embodiment 2
[0033] 1) Reaction device
[0034] Stainless steel fixed bed reactor, inner diameter 2000mm, filled with 5m3 Alpha-alumina balls. Part of the feed liquid phase methanol is vaporized through a vaporizer and then enters the catechol saturation column. The catechol is added and vaporized in the catechol saturation tower, mixed with methanol vapor, and the gas-phase compound is heated to the reaction temperature through the superheater and then enters the reactor.
[0035] 2) Method for adding catalytic components
[0036]The catalytic component is phosphoric acid. Part of the feed liquid phase methanol is vaporized through the vaporizer and then enters the phosphoric acid vaporizer. Phosphoric acid is added and vaporized in the phosphoric acid vaporizer, mixed with methanol vapor, and the gas-phase compound is heated to the reaction temperature through the superheater and then enters the reactor.
[0037] The weight ratio of the feed liquid is: catechol:methanol=1:1.
[00...
Embodiment 3
[0041] 1) Reaction device
[0042] Stainless steel single-tube reactor, inner diameter 32mm, length 1200mm, the upper layer of the reaction tube is the gasification and preheating section, filled Glass ball, height 40cm. The middle layer of the reaction tube is a catalyst bed, filled with 350cm3 Alpha-alumina ball, height 50cm. The lower layer of the reaction tube is a thermal insulation section, which is filled with Glass ball, height 40cm.
[0043] 2) Method for adding catalytic components
[0044] The catalytic component is phosphoric acid, which is directly added to the feed liquid. The weight ratio of the feed liquid is: catechol:methanol:phosphoric acid=1:1. The feed liquid phase feed liquid enters the top of the reaction tube through a pump.
[0045] Phosphoric acid is vaporized together with the feed liquid in the preheating section of the reaction tube.
[0046] 3) etherification reaction
[0047] The reaction temperature was 275°C, the feed flow rate was ...
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