Attapulgite clay-supported heteropoly acid phase-transfer catalyst for oxidative desulfurization of fuel
A phase transfer catalyst, attapulgite clay technology, applied in physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, catalyst activation/preparation, etc., can solve the problems of low desulfurization rate and high cost, and achieve Low cost, cost reduction, and effect of improving catalytic desulfurization effect
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Embodiment 1
[0025] Add 20g of sodium tungstate and 1g of sodium dihydrogen phosphate into a reactor filled with 100mL of distilled water, and stir at 60°C for 3h. Then add 30 g of 2 mol / L hydrochloric acid to treat the attapulgite clay, continue to stir for 1 hour, then add dropwise 100 mL of an aqueous solution in which 15 g of cetyltrimethylammonium bromide is dissolved, and stir vigorously for 6 hours. After the reaction, the product was washed with distilled water, then dried at 70° C. to constant weight, crushed, and passed through a 200-mesh sieve. The product in this embodiment has a desulfurization rate of more than 90% for fuel oil, the sulfur content can be reduced to below 100ppm, and the oxidation efficiency of hydrogen peroxide is obviously higher than that of small molecule organic acids.
Embodiment 2
[0027] Add 15g of sodium tungstate, 1.2g of sodium molybdate and 1g of sodium dihydrogen phosphate into a reactor filled with 100mL of distilled water, and stir at 70°C for 2h. Then add 40 g of attapulgite clay heat-treated at 400 degrees, continue to stir for 1 hour, then add dropwise 100 mL of an aqueous solution in which 10 g of tetradecyltrimethylammonium bromide is dissolved, and stir vigorously for 6 hours. After the reaction, the product was washed with distilled water, then dried at 70° C. to constant weight, crushed, and passed through a 200-mesh sieve. The product in this embodiment has a desulfurization rate of more than 92% for fuel oil, the sulfur content can be reduced to below 90ppm, and the oxidation efficiency of hydrogen peroxide is obviously higher than that of small molecule organic acids.
Embodiment 3
[0029] Add 20g sodium tungstate, 1.5g sodium molybdate, 1.5g ammonium metavanadate and 1g sodium dihydrogen phosphate into a reactor filled with 100mL dihydrogen phosphate, stir and react at 80°C for 2h, then add 50g iron ion exchange attapulgite clay, The stirring reaction was continued for 1h. Then, 100 mL of an ethanol solution in which 20 g of dioctadecyldimethylammonium bromide was dissolved was added dropwise, and the reaction was vigorously stirred for 6 h. After the reaction, the product was washed with an alcohol-water solution, then dried at 70° C. to constant weight, crushed, and passed through a 200-mesh sieve. The product in this embodiment has a desulfurization rate of more than 95% for fuel oil, the sulfur content can be reduced to below 80ppm, and the oxidation efficiency of hydrogen peroxide is obviously higher than that of small molecule organic acids.
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