MOFs based carbon dioxide adsorbent, preparation method and application thereof
A carbon dioxide and adsorbent technology, applied in the field of MOFs-based carbon dioxide adsorbent and its preparation, can solve the problems of weak adsorption and separation ability, and achieve the effect of strong adsorption ability, overcoming volatile and non-volatile
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Embodiment 1
[0046] Dissolve 1g of tetraethylenepentamine in 100ml of absolute ethanol, stir for 0.5h, add 1g of MOF-74, stir for 4h, put the sample in an oven, dry at 80°C to remove ethanol, and then dry at 105°C, denoted as M1. In the obtained sample, the content of organic amine was 50 wt%. The adsorption data was measured by using a fixed bed, the adsorption temperature was 70°C, and the simulated gas flow rate was 50ml / min. The results are shown in Table 1.
Embodiment 2
[0048] Dissolve 1g of tetraethylenepentamine in 100ml of absolute ethanol, stir for 0.5h, add 1g of ZIF-8, stir for 4h, put the sample in an oven, dry at 80°C to remove ethanol, and then dry at 105°C, denoted as M2 . In the obtained sample, the content of organic amine was 50 wt%. The test conditions are the same as in Example 1, and the results are shown in Table 1.
Embodiment 3
[0050] Dissolve 1g of tetraethylenepentamine in 100ml of absolute ethanol, stir for 0.5h, add 1g of MIL-101, stir for 4h, put the sample in an oven, dry at 80°C to remove ethanol, and then dry at 105°C, record as M3. In the obtained sample, the content of organic amine was 50 wt%. The adsorption capacity data was determined by using a fixed bed, and the results are shown in Table 1. When the adsorption temperature was adjusted to 20, 30, 40, 50, 60, 70, and 80°C, and the simulated gas flow rate was 50ml / min, the adsorption results of M3 are shown in Table 2. Adjust the adsorption temperature to 50°C, the simulated gas flow rate to 50ml / min; the desorption temperature to 150°C, the nitrogen purge flow rate to 50ml / min, and the desorption time to 30min. The cycle adsorption results of M3 are shown in Table 3.
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