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焦油渣基活性炭的制备及其对生化废水COD的脱除性能OA

Preparation of tar residue-based activated carbon and its performance for COD removal in biochemical wastewater

中文摘要英文摘要

危废焦油渣缺乏有效的处理手段,长期堆放造成了大气和地下水的严重污染,处理费用高昂制约了煤化工企业的规模化发展.为了开发焦油渣高效环保资源化消纳利用技术,将焦油渣干渣、改性沥青和KOH按照100∶10∶5质量比混合成型,制备焦油渣基活性炭,在水平刚玉管式炉中考察了活化温度、活化时间和升温速率对活性炭产物表面吸附性能及孔隙发育的影响规律.采用FTIR、N2吸-脱附仪、扫描电镜、XPS等手段对成型活性炭的表观形貌和表面化学性质进行了全面分析,并将活性炭产品用于生化废水进行COD脱除效果的检验.结果表明:焦油渣经过260℃和1 h热处理可形成干渣,干渣原料体系以5℃/min速率升温至550℃恒温30 min炭化后,最优活化工艺参数为:水蒸气流量2 mL/(h·g),活化温度900℃,活化时间1.5 h,升温速率5℃/min.在最优活化条件下焦油渣干渣制备的成型活性炭表面炭质组分稀松,孔隙鲜明,富含羰基、羟基、酯基、羧基等含氧官能团,比表面积达到 1 045.10 m2/g,碘吸附值为 939 mg/g,亚甲蓝吸附值为125 mg/g,灰分为8.46%,抗压强度为90%,均达到了GB/T 7701.4-2008《煤质颗粒活性炭 第2部分:净化水用煤质颗粒活性炭》的要求,总孔体积为0.654 cm3/g,中孔占比63.57%,平均孔径为3.94 nm,孔径分布较为集中,在处理时间为60 min和固液比(1 L生化废水中活性炭的添加量)为0.6 g/L的条件下,焦油渣基活性炭可将生化废水的COD从312 mg/L降至35 mg/L,水质清澈透明无味,达到水污染物综合排放标准(DB11/307-2013)B类水质的要求.

As a hazardous waste,tar residue lacks effective utilization methods,and its long-term stacking causes severe air and groundwater pollution.The high treatment costs also con-strain the large-scale development of coal chemical enterprises.To develop its efficient and environ-mentally friendly technology,a study on the preparation of tar residue-based activated carbon was car-ried out using dry tar residue,modified asphalt and KOH activator in a mass ratio of 100∶10∶5.The effects of activation temperature,activation time,and heating rate on the surface adsorption perfor-mance and pore development of activated carbon products were investigated in a horizontal tube alun-dum furnace.The morphology and surface chemical properties of the activated carbon were compre-hensively analyzed using infrared spectroscopy,N2 adsorption-desorption,scanning electron micros-copy(SEM)and X-ray photoelectron spectroscopy(XPS).The activated carbon product was tested for COD removal efficiency in biochemical wastewater.The results show that the tar residue forms a dry residue after heat treatment at 260℃for 1 h.For the dry residue carbonized by rising from room temperature to 550℃at a heating rate of 5℃/min for 30 min,the optimal steam activation process parameters are:steam flow rate 2 mL/(h·g),activation temperature 900℃,activation time 1.5 h and heating rate 5℃/min.The surface carbon component of the tar residue-based activated carbon is loose with distinct pores and abundant oxygen functional groups such as carbonyl,hydroxyl,ester and carboxyl.The specific surface area is 1 045.10 m2/g,iodine value is 939 mg/g,methylene blue value is 125 mg/g,ash content is 8.46%and compressive strength is 90%,all of which reach the national standard requirements of"Granular activated carbon from coal for the treatment of water"(GB/T 7701.4-1997).The total pore volume is 0.654 cm3/g and the average pore size is 3.94 nm with 63.57%of the concentrated mesopore distribution.The COD in biochemical waste water treated by the the tar residue-based activated carbon for 60 min with a solid-to-liquid ratio of 0.6 g/L is reduced from 312 mg/L to 35 mg/L.The transparent and odorless water meets the class B water quality requirements of the Chinese standard"Integrated Discharge Standard of Water Pollutants"(DB11/307-2013).

乔元;徐春明;吕昭;赵鹏

中国石油大学(北京)化学工程与环境学院,102249 北京||国能榆林化工有限公司,719000 陕西榆林中国石油大学(北京)化学工程与环境学院,102249 北京国能哈密能源化工有限公司,839000 新疆哈密煤炭科学技术研究院有限公司,100013 北京||国家能源煤炭高效利用与节能减排技术装备重点实验室,100013 北京

化学化工

焦油渣活性炭活化孔结构危废

coal tar residueactivated carbonactivationpore structurehazardous waste

《煤炭转化》 2026 (2)

81-91,11

国家重点研发计划资助项目(2023YFC3904302-02)和煤科院科技发展基金重点项目(2024ZDI-05)

10.19726/j.cnki.ebcc.202602008

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