Solid base catalyst and preparation method and application of solid base catalyst
A solid base catalyst and potassium fluoride technology, applied in chemical instruments and methods, physical/chemical process catalysts, ether preparation, etc., can solve problems such as catalyst separation and post-processing difficulties, equipment corrosion and scaling, environmental pollution, etc.
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Embodiment 1
[0023] (1) Weigh Mg(NO 3 ) 2 , Al(NO 3 ) 3 and Zn(NO 3 ) 2 A total of 100 g, wherein the Mg / Al molar ratio is 3, and the zinc mass fraction accounts for 10% of the total mixture; the mixture is dissolved in 200 ml of deionized water to obtain solution A;
[0024] Take the molar ratio of NaOH and Na of 1:1 2 CO 3 , dissolved in deionized water, with 200 ml of saturated lye B.
[0025] Mix solution A and saturated lye solution B by the double-drop method, control the temperature at 60 °C, stir vigorously, keep pH 9-10, after the dropwise addition, statically crystallize at 80 °C for 12 hours, filter the precipitate, wash and dry to obtain zinc and magnesium Aluminum hydrotalcite.
[0026] (2) The zinc-magnesium-aluminum hydrotalcite was calcined at 600°C for 7 hours.
[0027] (3) Step (2) The calcined product is placed in a fixed bed reactor, and the mass space velocity is 3h -1 Water was poured into it and treated at 500° C. for 3 hours to obtain a hydrothermal treatm...
Embodiment 2
[0030] (1) Step (1) is the same as in Example 1.
[0031] (2) The zinc-magnesium-aluminum hydrotalcite obtained in step (1) was calcined at 500° C. for 8 hours.
[0032] (3) Step (2) The calcined product is placed in a fixed bed reactor, and the mass space velocity is 3h -1 Water was poured into it and treated at 500° C. for 3 hours to obtain a hydrothermal treatment product.
[0033] (4) The hydrothermal treatment product was immersed in a saturated potassium fluoride solution for 3 hours, and the temperature was controlled at 75°C; filtered, dried at 100°C, and activated at 280°C for 2 hours to obtain a catalyst. The content of potassium fluoride is 31%.
Embodiment 3
[0035] Methanol, propylene oxide and the catalyst prepared in Example 1 were added to a 200 ml autoclave, and the amount of the catalyst was 1 wt % of the reactant. The reaction was cooled to room temperature, filtered, and the filtrate was distilled to give the product. The molar ratio of methanol and propylene oxide was 3:1, the amount of catalyst was 1 wt % of the reactant, and the total amount of the reactant and the catalyst was 30 g.
[0036] The product was detected by GCMS as propylene glycol methyl ether. The PO conversion rate of the whole reaction was 98.2%, the ratio of primary and secondary ethers was 96.5:3.5, and the yield was 87.2%.
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