The preparation method of 2,6-dihydroxytoluene
A technology of dihydroxytoluene and diaminotoluene, which is applied in 2 fields, can solve the problems of short service life and large investment, and achieve the effects of avoiding the interference of acid liquid, high quality and short chemical path
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Embodiment 1
[0063] Such as figure 1 As shown, a 10cm high ceramic ring filler is filled at the bottom of the fixed bed tubular stainless steel reactor (inner diameter 3cm, length 1m), and then a 10g solid acid catalyst is filled (the solid acid catalyst is made of SO 4 2- / ZrO 2 A composite solid acid catalyst composed of solid acid and HZSM-5 molecular sieve, the HZSM-5 silicon-aluminum ratio is 20), and the upper part of the composite solid acid catalyst is filled with a 20cm high ceramic ring packing.
[0064] Turn on the power, set the internal temperature of the fixed bed reactor at 360°C, set the internal temperature of the steam heater (stainless steel tube, inner diameter 3cm, length 50cm) at 320°C, and start the peristaltic pump (BT1-100E, flow 0.07~98ml / min), input the deionized water into the steam heater, control the flow rate of deionized water to be 10ml / min, the water vapor is pumped in from the upper inlet of the fixed bed reactor, and exported from the lower end of the ...
Embodiment 2
[0069] On the basis of Example 1, only the loading amount of the composite solid acid catalyst was changed to 1 gram, the silicon-aluminum ratio of HZSM-5 was 25, and the temperature was raised to 150°C when 2,6-diaminotoluene was heated and melted. Other technological processes and parameters The results are shown in Table 1.
Embodiment 3
[0071] On the basis of Example 1, only change the loading amount of the composite solid acid catalyst to 2 grams, the HZSM-5 silicon-aluminum ratio is 30, 2,6-diaminotoluene is heated to 200 ° C when it is heated and melted, other process flow and parameters The results are shown in Table 1.
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