Adsorbent for removal of benzothiophene from diesel oil and preparation method thereof
A technology of benzothiophene and adsorbent, applied in the field of adsorbent for removing benzothiophene from diesel oil and its preparation, can solve problems affecting the service life of the adsorbent, loss of cerium ions, etc., achieve good hydrothermal stability, reduce Drain, the effect that how to use is easy
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Embodiment 1
[0017] Weigh 10 g of sodium-type Y molecular sieve, 60 mL of Y(NO 3 ) 3 ·6H 2 O aqueous solution, stirred and mixed evenly in a batch kettle, soaked at 80°C for 20 hours, dried the solid in an oven at 100°C, raised the temperature to 450°C at a rate of 2°C / min in a muffle furnace, and maintained this temperature for 4 hours, a sodium-type Y molecular sieve adsorbent loaded with yttrium oxide (abbreviated as Y / Y molecular sieve adsorbent) was obtained, which was used as an adsorbent for removing benzothiophene from diesel.
[0018] Desulfurization: Weigh 0.1 g of Y / Y molecular sieve adsorbent, 6 mL of simulated diesel oil containing n-octane and benzothiophene, place the two in a batch kettle, and react for 1 hour at 50°C to simulate diesel oil The sulfur content of the diesel oil product is 60 mg / L, the sulfur content of the simulated diesel oil product after desulfurization is 0 mg / L, and the desulfurization rate is 100%.
Embodiment 2
[0022] 60 mL of 1 wt% Y(NO 3 ) 3 ·6H 2 O aqueous solution, at 50°C, impregnated for 10 hours, and the other conditions were the same as in Example 1, to obtain a sodium-type Y molecular sieve adsorbent loaded with yttrium oxide (abbreviated as Y / Y molecular sieve adsorbent), which was used as a method for removing benzothiophene from diesel oil. the adsorbent.
[0023] Desulfurization: Weigh 0.12 g of Y / Y molecular sieve adsorbent weight g and diesel volume mL in a ratio of 1:6 to 1:200, and place the two in an intermittent kettle, which is placed in an oil bath at 50 to 80°C , the desulfurization time is 0.5 to 4 hours; at 80 ° C, the reaction is 2 hours, and the rest of the conditions are the same as in Example 1. The sulfur content of the simulated diesel oil is 60 mg / L, after desulfurization, the sulfur content of the simulated diesel oil is 15 mg / L, and the desulfurization rate is 75%.
Embodiment 3
[0025] 60 mL of 10 wt% Y(NO 3 ) 3 ·6H 2 The aqueous solution of O was immersed at 50° C. for 5 hours, and other conditions were the same as in Example 1 to obtain a sodium-type Y molecular sieve adsorbent loaded with yttrium oxide, which was used as an adsorbent for removing benzothiophene in diesel oil.
[0026] Desulfurization: react for 0.5 hour, and all the other conditions are the same as in Example 1. The sulfur content of the simulated diesel oil is 60 mg / L. After desulfurization, the sulfur content of the simulated diesel oil is 6 mg / L, and the desulfurization rate is 90%.
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