Method for preparing active carbon materials SO#-[2] absorbent by medicament activation method
A technology for preparing activated carbon and adsorbents, which is applied in chemical instruments and methods, separation methods, and other chemical processes. It can solve the problems of large carbon loss, high cost, and limited modification of chemical properties, and achieve broad application prospects and low prices. , the effect of a wide range of sources
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Embodiment 1
[0013] The 4-10 mesh granules obtained after semi-coke sieving are mixed with the medicament mixed aqueous solution at a volume ratio of 1:0.83 and then added to the autoclave, wherein the medicament mixed aqueous solution is 3%, 5% and 6% hydrogen peroxide aqueous solution respectively. Under the highest temperature of 270°C and the highest pressure of 43atm, the hydrothermal chemical reaction was carried out for 2 hours, and then it was taken out after natural cooling, and then its specific surface area, pore volume and desulfurization activity were measured. Experimental conditions for adsorbent activity and sulfur capacity test: temperature: 85°C; space velocity: 900-1000h -1 ;SO 2 Concentration: 1700-2100ppm; O 2 : ~5%; H 2 O(g): 6-10%. The results are shown in Table 1.
[0014] Table 1. Different H 2 o 2 Activated carbon-based material SO after hydrothermochemical modification at high concentration 2 The change of specific surface area and pore volume of adsorbent...
Embodiment 2
[0022] Mix the 4-10 mesh granules obtained after sieving the semi-coke with the medicament mixed water solution at a volume ratio of 1:0.83, and then add it to the autoclave, wherein the medicament mixed water solution is 5% KOH, KMnO 4 、HNO 3 and H 2 SO 4 solution. Under the highest temperature of 270°C and the highest pressure of 43atm, the hydrothermal chemical reaction was carried out for 2 hours, and then it was taken out after natural cooling, and then its specific surface area, pore volume and desulfurization activity were measured. Experimental conditions for adsorbent activity and sulfur capacity test: temperature: 85°C; space velocity: 900-1000h -1 ;SO 2 Concentration: 1700-2100ppm; O 2 : ~5%; H 2 O(g): 6-10%. The results are shown in Table 2.
[0023] Table 2. Activated carbon-based material SO after hydrothermochemical modification under different agents 2 The change of specific surface area and pore volume of adsorbent and its influence on breakthrough ti...
Embodiment 3
[0030]Mix the 4-10 mesh particles obtained after semi-coke sieving with 6% hydrogen peroxide aqueous solution at a volume ratio of 1:0.83, and then add it to the high-pressure reactor. Under 43atm for 2 hours of hydrothermal chemical reaction, take it out after natural cooling, and then measure its specific surface area, pore volume and desulfurization activity. Experimental conditions for adsorbent activity and sulfur capacity test: temperature: 85°C; space velocity: 900-1000h -1 ;SO 2 Concentration: 1700-2100ppm; O 2 : ~5%; H 2 O(g): 6-10%. The results are shown in Table 3.
[0031] Table 3. Activated carbon-based material SO after hydrothermochemical modification under different pressures 2 The change of specific surface area and pore volume of adsorbent and its influence on breakthrough time and sulfur capacity
[0032] Sample Raw coke 8atm 12atm 24atm 43atm
[0033] Specific surface area m 2 / g 49.19 468 689 906 234
[0034] Pore volume ml / g 0.0351 0.2364 0.204...
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