High-temperature calcium-based coal ash absorbent for CO2 and preparation method of high-temperature calcium-based coal ash absorbent
A technology of fly ash and absorbent, which is applied in the field of CO2 separation and capture, can solve problems such as the decline of absorption performance, and achieve the effects of improving stability, reducing costs, and high CO2 absorption performance
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Embodiment 1
[0026] a CO 2 The high-temperature calcium-based fly ash absorbent is composed of calcium oxide and fly ash, the mass percentage of calcium oxide in the absorbent is 50%, and the fly ash is 50%.
[0027] The CO 2 The preparation method of high-temperature calcium-based fly ash absorbent, the steps are as follows:
[0028] 1) Pass the fly ash through a 150 μm standard sieve, soak the collected fly ash in deionized water for 2 hours, wash with deionized water for 4 times after suction filtration, and dry at 80°C for use;
[0029] 2) Calcining calcium oxide at 850°C for 3 hours to ensure that the calcium-based material is completely calcined;
[0030] 3) Weigh the calcined calcium oxide and the dried fly ash according to the mass ratio and mix them evenly, slowly add the mixed solution of water and 2-propanol under stirring condition, and the water and 2-propanol in the mixed solution The volume ratio is 3:1, hydration reaction at 85°C for 2 hours, and then evaporated and dried ...
Embodiment 2
[0034] a CO 2 The high-temperature calcium-based fly ash absorbent is composed of calcium oxide and fly ash, the mass percentage of calcium oxide in the absorbent is 75%, and the fly ash is 25%. The CO 2 The preparation method of the high-temperature calcium-based fly ash absorbent is the same as in Example 1.
[0035] Experiments show that: in the high temperature range of 400-650 ℃, the CO of the absorbent 2 The absorption capacity reached 256mg / g; when the cycle reaction was carried out 14 times, its CO 2 The decline trend of absorption capacity began to stabilize, and there was no continuous downward trend in the follow-up, and the sintering of absorbent particles was significantly improved after multiple cycles.
Embodiment 3
[0037] a CO 2 The high-temperature calcium-based fly ash absorbent is composed of calcium hydroxide and fly ash, the mass percentage of calcium hydroxide in the absorbent is 50%, and the fly ash is 50%. The CO 2 The preparation method of the high-temperature calcium-based fly ash absorbent is the same as in Example 1.
[0038] Experiments show that: in the high temperature range of 400-650 ℃, the CO of the absorbent 2 The absorption capacity reached 222mg / g; when the cycle reaction was carried out 17 times, its CO 2 The decline trend of absorption capacity began to stabilize, and there was no continuous decline trend afterwards; the sintering of absorbent particles was improved.
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