Preparation method of high-purity 2,6-di-tert-butyl p-cresol
A di-tert-butyl and p-cresol technology, applied in the preparation of organic compounds, chemical instruments and methods, catalyst activation/preparation, etc., can solve the problems of BHT yield reduction, corrosion equipment, low synthesis efficiency, etc., and achieve equipment The effect of increasing the service life, reducing the corrosion of equipment, and improving the conversion rate
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Embodiment 1
[0036] A kind of high-purity 2, the preparation method of 6-di-tert-butyl-p-cresol is characterized in that, comprises the following steps:
[0037] Step S0: the step of preparing 2,6-di-tert-butyl-p-cresol crude product
[0038] (1) The liquefied isobutene from the tanker is connected to the liquefied hydrocarbon crane pipe, and after the static grounding and other safety facilities are completely connected and checked, the liquefied hydrocarbon unloading pump is started, and the liquefied hydrocarbon crane pipe is unloaded to the isobutylene liquefied buried storage tank; pipelines are used The nitrogen gas is delivered to the isobutene liquefaction storage tank, and the liquefied isobutene is pressed into the isobutene vaporizer through the regulating valve; the isobutene vaporizer is heated by hot water, and the temperature of the hot water is 80°C. After the isobutene is vaporized, it enters the gas storage tank. 0.3 MPa; the modified mesoporous silica supported Nb / Mo / Cu ...
Embodiment 2
[0049] Embodiment 2: a kind of preparation method of high-purity 2,6-di-tert-butyl-p-cresol,
[0050] Step S0: the step of preparing 2,6-di-tert-butyl-p-cresol crude product
[0051] (1) The liquefied isobutene from the tanker is connected to the liquefied hydrocarbon crane pipe, and after the static grounding and other safety facilities are completely connected and checked, the liquefied hydrocarbon unloading pump is started, and the liquefied hydrocarbon crane pipe is unloaded to the isobutylene liquefied buried storage tank; pipelines are used The nitrogen gas is delivered to the isobutene liquefaction storage tank, and the liquefied isobutene is pressed into the isobutene vaporizer through the regulating valve; the isobutene vaporizer is heated by hot water, and the temperature of the hot water is 75°C. After the isobutene is vaporized, it enters the gas storage tank. 0.27 MPa; the modified mesoporous silica supported Nb / Mo / Cu trimetallic active center catalyst was added i...
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