Method for inhibiting ethylbenzene hydroperoxide decomposition
A technology of ethylbenzene hydroperoxide and ethylbenzene, which is applied in the direction of peroxygen compound preparation, chemical instruments and methods, organic chemistry, etc., can solve problems such as unproposed solutions, and achieve the goal of reducing scaling problems and reducing by-products Effects that generate and improve stability
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Embodiment 1
[0051] A method for inhibiting the decomposition of ethylbenzene hydroperoxide, comprising the steps of:
[0052] Carried out in three identical bubble tower oxidation reactor devices, ethylbenzene and bisphosphonate compounds are mixed through a mixer, and then enter the first oxidation reactor, nitrogen and oxygen mixed gas containing 25v% oxygen Enter from the bottom of the reactor, and react, wherein the general formula of the bisphosphonate compound is as follows:
[0053]
[0054] In the above general formula, R 1 Methyl, R 2 is n-butyl, R 3 For n-propyl. In the first oxidation reactor, the ethylbenzene feed rate is 1kg / h, and the content of bisphosphonate compounds in the control ethylbenzene feed is 90mg / kg, and the reaction temperature is 155°C, and the reaction pressure is 0.25MPa. The phase residence time is 40min, then enters the second reactor, the reaction temperature is 152°C, the reaction pressure is 0.25MPa, the reaction liquid phase residence time is 4...
Embodiment 2
[0056] A method for inhibiting the decomposition of ethylbenzene hydroperoxide, comprising the steps of:
[0057] It is carried out in four identical bubble tower oxidation reactor devices. After mixing ethylbenzene and bisphosphonate compounds through a mixer, they enter the first oxidation reactor, and the mixed gas of nitrogen and oxygen containing 20v% oxygen Enter from the bottom of the reactor, and react, wherein the general formula of the bisphosphonate compound used is as follows:
[0058]
[0059] In the above general formula, R 1 is ethyl, R 2 is n-propyl, R 3 For n-butyl. In the first oxidation reactor, the feed amount of ethylbenzene is 1kg / h, the additive content in the ethylbenzene feed is controlled to be 120mg / kg, the reaction temperature is 165°C, the reaction pressure is 0.23MPa, and the residence time of the reaction liquid phase is 35min , then enter the second reactor, the reaction temperature is 160 ° C, the reaction pressure is 0.23 MPa, the react...
Embodiment 3
[0061] A method for inhibiting the decomposition of ethylbenzene hydroperoxide, comprising the steps of:
[0062] Carried out in five identical bubble tower oxidation reactor devices, after mixing ethylbenzene and bisphosphonate compounds through a mixer, enter the first oxidation reactor, nitrogen and oxygen mixed gas containing 23v% oxygen Enter from the bottom of the reactor, and react, wherein the general formula of the bisphosphonate compound used is as follows:
[0063]
[0064] In the above general formula, R 1 is isobutyl, R 2 is n-hexyl, R 3 for hydrogen. In the first oxidation reactor, the feed amount of ethylbenzene is 1kg / h, the additive content in the ethylbenzene feed is controlled to be 130mg / kg, the reaction temperature is 165°C, the reaction pressure is 0.20MPa, and the residence time of the reaction liquid phase is 35min , then enter the second reactor, the reaction temperature is 163 ° C, the reaction pressure is 0.20 MPa, the reaction liquid phase re...
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