Absorbent for absorbing and separating polyaromatic hydrocarbon in diesel and preparation method thereof
A technology for adsorption and separation of polycyclic aromatic hydrocarbons, applied in chemical instruments and methods, refined hydrocarbon oil, petroleum industry, etc., can solve the problem of small saturated adsorption capacity of adsorbents, poor selectivity of aromatic hydrocarbon adsorbents, unsuitable for adsorption and separation of polycyclic aromatic hydrocarbons, etc. problem, to achieve the effect of reducing polycyclic aromatic hydrocarbons and high selectivity
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Embodiment 1
[0039] (1) First, 1000g of dilute water glass solution with a concentration of 16.8% (mass fraction of sodium silicate) was kept at 50°C for half an hour, and slowly added 340g of dilute sulfuric acid solution with a mass fraction of 12% to adjust the pH value to 6.5-7.0 , aged at 50°C for 3 hours after forming a sol, filtered and washed, dried at 100-120°C for 12 hours, and then calcined at 550°C for 4 hours to obtain carrier silica gel.
[0040] (2) Modulation of silica gel pore size: Weigh 6.88g of sodium hydroxide (Sinopharm Chemical Reagent Co., Ltd., analytically pure, 96wt%) and dissolve it in 500ml of deionized water, take 500ml of sodium hydroxide solution, stir evenly at 60°C, slowly Add 100g of the carrier silica gel in step (1), stir at 60°C for 6 hours, filter and wash to pH = 7-8, dry at 100-120°C for 12 hours, and roast at 550°C for 4 hours to obtain the modified Silica gel.
[0041] (3) Metal modification: 4.19g copper nitrate metal salt (Cu(NO 3 ) 2 ·3H 2 ...
Embodiment 2
[0044] (1) The synthesis of the carrier silica gel is the same as in Example 1.
[0045] (2) Modulation of silica gel pore size: Weigh 16.5g of concentrated sulfuric acid (98%, analytically pure, 96wt%) and dilute to 500ml with deionized water, take 500ml of sulfuric acid solution, stir evenly at 60°C, slowly add 100g of step (1) Carrier silica gel, the modification conditions are the same as in Example 1,,.
[0046] (3) Metal modification is the same as in Example 1.
[0047] (4) The performance evaluation of the adsorbent is the same as in Example 1, and the evaluation of the adsorbent is shown in Table 2.
Embodiment 3
[0049] (1) The synthesis of the carrier silica gel is the same as in Example 1.
[0050] (2) Modulation of silica gel pore size: take 500 ml of deionized water, stir evenly at 60° C., slowly add 100 g of the carrier silica gel in step (1), and the modification conditions are the same as in Example 1.
[0051] (3) Metal modification is the same as in Example 1.
[0052] (4) The performance evaluation of the adsorbent is the same as in Example 1, and the evaluation of the adsorbent is shown in Table 2.
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Abstract
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