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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

Active Publication Date: 2021-07-23
NORTH CHINA ELECTRIC POWER UNIV (BAODING) +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the poor selectivity of the absorbent (water), high power consumption, and huge equipment, the high-pressure water washing method has been less used in recent years; the physical absorption method is mainly low-temperature methanol method and propylene carbonate method, and the absorption effect is better, but High investment cost and large loss of absorbent; chemical absorption method mainly uses ethanolamine, diethanolamine, N-methyldiethanolamine and other alcoholamine solvents as absorbents, which are prone to solvent foaming and degradation, and are highly corrosive and selective Insufficiency such as low performance; membrane separation to remove CO 2 and H 2 S technology has the advantages of environmental friendliness and safe operation, but due to factors such as complex membrane production process, high cost, and stability to be improved, industrial application has not yet been realized.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention belongs to the field of solid waste disposal and biogas purification, and particularly relates to a preparation method of a fly ash-based adsorption material for biogas purification. The method comprises the following steps: by taking incineration fly ash as a raw material, crushing and sieving by adopting a ball mill, putting the fly ash into a vertical tube furnace, introducing a nitrogen-rich aqueous solution at 600-900 DEG C, activating for 1-3 hours, cooling, loading alkali / alkaline earth metal chlorate by adopting an excessive impregnation method, and carrying out rotary evaporation drying, thereby obtaining the fly ash-based adsorption material. The prepared adsorption material not only has a good synergistic removal effect on impurity gases such as CO2 and H2S in the biogas, but also has the characteristics of low raw material price, simple preparation process and the like, and resource utilization of the fly ash and efficient purification of the biogas are realized.

Description

technical field [0001] The invention belongs to the fields of solid waste disposal and biogas purification and purification, and in particular relates to a preparation method of a fly ash-based adsorption material used for biogas purification. Background technique [0002] Biogas is a combustible gas produced by microbial fermentation of organic matter under anaerobic conditions, and its main components include CH 4 (50%~80%) and CO 2 (20% ~ 40%), also contains a small amount of H 2 S (0.5% ~ 3%), O 2 , CO, N 2 Wait. CO 2 The existence of will greatly reduce the calorific value and energy density of biogas, and increase the ignition temperature; while H 2 S is a highly toxic gas, which not only corrodes pipes, metal instruments, etc. during transportation and storage, but also produces SO after combustion. 2 Will cause environmental pollution. Therefore, the removal of CO from biogas 2 and H 2 S and other impurity gases are the key steps to realize the safe and eff...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/16B01J20/28B01J20/30C10L3/10
CPCB01J20/16B01J20/046B01J20/28054C10L3/103C10L3/104C10L2290/542
Inventor 李凯谢金恒马善为陈忠源崔亚茹胡斌陆强
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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