Preparation method of fly ash-based adsorption material for biogas purification
An adsorption material and fly ash technology, applied in the field of preparation of fly ash-based adsorption materials, can solve the problems of solvent foaming and degradation, stability to be improved, poor selectivity of absorbents, etc., so as to improve pore volume and improve biogas purification Efficient and efficient synergistic removal
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Embodiment 1
[0024] Biomass incineration fly ash is used as raw material, and the fly ash with a particle size of less than 0.2 mm is screened after dry ball milling by a ball mill, and 10 g of the screened fly ash is placed in a vertical tube furnace, and a concentration of 20 wt % is introduced at 900 ° C. Urea solution, the solution flow rate is 200mL / h, activated for 3 hours, and cooled to room temperature under a helium atmosphere, then ultrasonically immersed in a magnesium chloride solution with a concentration of 1wt% for 3 hours, and finally heated at a temperature of 80 °C and a pressure of 0.10Mpa. Rotary drying is carried out under the condition of rotating speed of 80 r / min, and a fly ash-based adsorption material loaded with 0.5 wt% magnesium chloride is obtained. Use of adsorbent materials for biogas (CO 2 30%, H 2 S is 2%, the rest is CH 4 ) purification, can achieve H 2 S removal rate was 84%, CO 2 The removal rate was 87%, H 2 S / CH 4 and CO 2 / CH 4 The separation ...
Embodiment 2
[0026] 10g of the fly ash screened in Example 1 was placed in a vertical tube furnace, and a hydrazine hydrate solution with a concentration of 15wt% was introduced at 800°C with a solution flow rate of 200mL / h, activated for 2 hours, and heated in a nitrogen atmosphere. Cool to room temperature, then ultrasonically immerse in a barium chloride solution with a concentration of 2wt% for 1 hour, and finally spin dry at a temperature of 80°C, a pressure of 0.10Mpa, and a speed of 80r / min to obtain a load of 2wt% sodium chloride fly ash-based adsorbent materials. Use of adsorbent materials for biogas (CO 2 30%, H 2 S is 2%, the rest is CH 4 ) purification, can achieve H 2 S removal rate is 88%, CO 2 The removal rate is 90%, H 2 S / CH 4 and CO 2 / CH 4 The separation coefficients were 12.57 and 12.86, respectively.
Embodiment 3
[0031] Using waste incineration fly ash as raw material, dry fly ash with particle size less than or equal to 0.15mm is screened by ball mill, and 10g of screened fly ash is placed in a vertical tube furnace, and the concentration of 10wt% is introduced at 600°C. Ammonia solution, the solution flow rate is 100mL / h, activated for 1 hour, and cooled to room temperature under nitrogen atmosphere, then ultrasonically immersed in a sodium chloride solution with a concentration of 3wt% for 2 hours, and finally heated at a temperature of 70°C and a pressure of 0.07Mpa , under the condition of rotating speed of 60r / min, the fly ash-based adsorption material loaded with 1.5wt% sodium chloride was obtained. Use of adsorbent materials for biogas (CO 2 30%, H 2 S is 2%, the rest is CH 4 ) purification, can achieve H 2 S removal rate was 84%, CO 2 The removal rate was 86%, H 2 S / CH 4 and CO 2 / CH 4 The separation coefficients were 11.20 and 11.47, respectively.
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