首页|K2CO3活化低阶煤和污泥共水热炭制备多孔炭及其对CO2和SO2吸附性能

K2CO3活化低阶煤和污泥共水热炭制备多孔炭及其对CO2和SO2吸附性能

Preparation of porous carbon by K2CO3 activation of co-hydrochar of low-rank coal and sewage sludge and its adsorption performance for CO2 and SO2

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我国低阶煤储量大,低阶煤材料化利用是当前国家重大需求.另外,我国城市污泥排放量逐年增加,高含水率污泥资源化利用至关重要.低阶煤和污泥水热碳化可有效资源化利用原料内的硫氮元素,制备硫氮掺杂水热炭.水热炭孔隙较不丰富,对其进行活化造孔可丰富其孔隙结构,制备得到硫氮掺杂多孔炭.选用较为温和K2CO3作为活化剂,探究K2CO3活化不同次烟煤与污泥水热炭制备多孔炭材料的性质,并研究多孔炭对CO2 和SO2 的吸附性能.结果表明,次烟煤和污泥水热炭经K2CO3活化改性后,硫氮元素含量相较于原来的水热炭均有所减少,多孔炭的比表面积由原水热炭的23.92 m2/g增至 331.77 m2/g,孔体积由原水热炭的 0.07 cm3/g增至 0.23 cm3/g.制备的多孔炭对CO2和SO2具有一定的吸附效果,次烟煤与污泥质量比为 7∶3,水热碳化温度为 160℃时,经 700℃K2CO3活化所制备的多孔炭在25℃下,对CO2吸附量为 1.56 mmol/g;次烟煤与污泥质量比为 1∶1,水热碳化温度为160℃时,所制备的水热炭经活化后,其在吸附温度为 120℃时,对SO2的吸附量为52.2 mg/g,且随着水热碳化温度升高,其吸附量有所下降,共水热炭相比于单一水热炭对CO2和SO2的吸附性能更好.研究结果可为低阶煤和污泥清洁高效利用和低成本CO2、SO2吸附剂开发提供理论依据.
China has abundant reserves of low rank coal,and the material utilization of low rank coal is a major demand for the country.With the discharge of urban sewage sludge is rising,and the demand for resource utilization of high moisture sewage sludge is crucial.Hy-drothermal carbonization of low-rank coal and sewage sludge can utilize the sulfur and nitrogen elements in raw materials effectively and prepare sulfur and nitrogen doped hydrochar.Hydrochar had relatively less abundant pores,and activation by activator can enrich its pore structure and prepare sulfur nitrogen co-doped porous carbon.In this paper,relatively mild K2CO3 was chosen as an activator for por-ous carbon preparation from co-hydrochars of sub-bituminous coal and sewage sludge,and the adsorption performance of porous carbon on CO2 and SO2was also studied.The results showed that compared with those of the original hydrochars,the sulfur and nitrogen contents re-duced after the activation modification by K2CO3,and the specific surface area of the porous carbon was increased from 23.92 m2/g to 331.77 m2/g,and the pore volume was increased from 0.07 cm3/g to 0.23 cm3/g.The prepared porous carbon had certain adsorption effect on CO2 and SO2.For the hydrochar obtained from co-hydrothermal carbonizaiton at the condition that the mass ratio of sub-bitumi-nous coal to sewage sludge was 7∶3,and the hydrothermal carbonization temperature was 160℃,activated by K2CO3at 700℃,the por-ous carbon has a CO2 adsorption capacity of 1.56 mmol/g at 25℃;when the mass ratio of sub-bituminous coal to sewage sludge was 1∶1 and the hydrothermal carbonization temperature was 160℃,the activated hydrochar prepared had an adsorption capacity of 52.2 mg/g for SO2 at an adsorption temperature of 120℃.The adsorption amount decreased with the increase of the hydrothermal carbonization tem-perature,and the adsorption performance of the porous carbon from co-hydrochar was better than that from the separate hydrochar for CO2 and SO2.The results may provide a theoretical basis for the clean and efficient utilization of low-rank coal and sewage sludge,as well as for the preparation of low-cost and efficient CO2 and SO2 adsorbent.

low-rank coalsewage sludgehydrothermal carbonizationhydrochar modificationadsorption performance

宋瑞珍、陈云霄、杨晓阳、王嘉伟、王宝凤、赵瑞东

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山西大学 资源与环境工程研究所,山西 太原 030006

CO2减排与资源化利用教育部工程研究中心,山西 太原 030006

中国科学院青岛生物能源与过程研究所 中国科学院生物燃料重点实验室,山东 青岛 266101

低阶煤 污泥 水热碳化 水热炭改性 吸附性能

国家自然科学基金资助项目山西省区域合作资助项目襄垣县固废综合利用科技攻关资助项目

221782042021040411010292023-2

2024

洁净煤技术
煤炭科学研究总院 煤炭工业洁净煤工程技术研究中心

洁净煤技术

CSTPCD北大核心
影响因子:0.893
ISSN:1006-6772
年,卷(期):2024.30(7)
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