磷酸低温活化蔗渣基中孔生物炭及其影响因素

以甘蔗渣为原料,磷酸为活化剂,采用低温活化法制备蔗渣基中孔生物质炭.采用L9(34)4因素3水平正交实验,探讨制备蔗渣基中孔生物质炭的实验方案与工艺条件;分析了浸渍比、烘干时间、活化温度、活化时间在3个不同水平下,对蔗渣基生物质炭碘吸附值、亚甲基蓝吸附值的影响.结果表明,对蔗渣基生物质炭孔结构和得率影响最大的因素是活化温度,影响最小的因素是烘干时间;实验范围内,提高活化温度有利于材料中孔结构的形成;最佳条件下制备的蔗渣基生物质炭其低温氮气等温吸附线有明显的回滞环,BET比表面积和总孔容分别为939 m2/g和1.35 mL/g,中孔占总孔容比例为89％,亚甲基蓝吸附值高达240 mg/g,远高于木质净水用活性炭国家一级标准(135 mg/g),属于典型的中孔炭.     

废活性炭微波再生新工艺的研究

提出用微波加热-二氧化碳活化法再生乙酸乙烯合成用触媒载体废活性炭工艺.采用条件实验法研究了活化时间、二氧化碳流量和微波功率对活性炭碘吸附值,亚甲基蓝吸附值和再生得率的影响,得到微波辐射加热二氧化碳活化再生乙酸乙烯用触媒载体废活性炭的最佳工艺条件为活化时间25 min,二氧化碳流量0.2 L/min,微波功率700 W.在此条件下制得的活性炭碘吸附值为1158.02 mg/g、亚甲基蓝吸附值为240 mg/g、得率为74.19%.并对活性炭进行了比表面积的测定和孔结构的分析,活性炭的比表面积为1308.13 m2/g,总孔容为0.76 mL/g.     

核桃壳炭化吸附废水中Cr(Ⅵ)的性能研究

采用氯化锌活化法制备生物质废物硬壳活性炭,工艺条件为:核桃壳与氯化锌溶液质量比为1∶1.5、氯化锌溶液质量分数50%、炭化温度300℃、炭化时间90 min、活化温度600℃、活化时间60 min。对产品比表面积、孔径和表征进行了分析,并探讨了该核桃壳活性炭吸附废水中六价铬的pH值、废水初始浓度、吸附时间、振动转速等影响因素。结果表明:制得的活性炭碘吸附值为1 038.33 mg/g,比表面积为645.36 m2/g,平均孔半径为1.37 nm。当活性炭用量为0.1 g,废水pH=3,吸附接触时间为1 h,取100 mL浓度为50 mg/L的含Cr6+废水时,处理吸附量可达48.57 mg/g。活性炭最大饱和吸附值为80.24 mg/g。吸附符合Langmuir等温模式,吸附等温方程式为Ce/Qe=0.0083+0.0121Ce。     

棉秆基活性炭的制备及其对2,4-二硝基苯酚的吸附

以棉秆为原料,以KOH为活化剂,制备了高比表面棉秆基生物质活性炭。分析了制得的活性炭的元素组成、表面官能团、吸附能力等物化性能,探讨了浸渍比,活化温度,活化时间等工艺参数对制备活性炭得率、表面官能团、碘值、亚甲基蓝值等性能的影响,并通过静态吸附实验比较了不同条件下制备活性炭对2,4-二硝基苯酚的吸附性能,探讨了典型炭样品对2,4-二硝基苯酚的等温吸附特性。结果表明,KOH活化棉秆基生物质活性炭的表面物化性质随浸渍比、活化温度等工艺参数变化而变化,活化适宜条件为浸渍比1：3、活化温度800℃、活化时间90 min,在此条件下制得的炭样的碘值为1 251 mg/g,亚甲基蓝吸附值为478 mg/g,分别是国家一级品标准的1.25倍与3.54倍;对2,4-二硝基苯酚的Langmuir最大吸附量为747 mg/g,与Freundlich模型相比,Langmuir模型能较好地描述2,4-二硝基苯酚在炭样上的吸附行为,表明制备活性炭样品表面吸附位的能量分布较为均一。     

废活性炭微波再生新工艺的研究

提出用微波加热一二氧化碳活化法再生乙酸乙烯合成用触媒载体废活性炭工艺。采用条件实验法研究了活化时间、二氧化碳流量和微波功率对活性炭碘吸附值，亚甲基蓝吸附值和再生得率的影响，得到微波辐射加热二氧化碳活化再生乙酸乙烯用触媒载体废活性炭的最佳工艺条件为活化时间25min，二氧化碳流量0．2L／min，微波功率700w。在此条件下制得的活性炭碘吸附值为1158．02mg／g、亚甲基蓝吸附值为240mv,／g、得率为74．19％。并对活性炭进行了比表面积的测定和孔结构的分析，活性炭的比表面积为1308．13m^2／g，总孔容为0．76mL／g。     

生物质活性炭的制备及其染料废水中的应用

以城市污水厂活性污泥为原料,用3 mol/L ZnCl2溶液活化,通入水蒸气作活化气制备活性炭吸附剂.实验结果表明,温度为600℃条件下,活化时间为1 h,制得的活性炭其碘吸附值为374.10 mg/g,比表面积为381.62 m2/g,孔容积为0.25 cm3/g,微孔容积为0.11cm3/g.并进一步将生物质活性炭应用于染料废水的处理,考察了吸附时间、活性炭投加量和pH对色度及TOC的脱除效果的影响.室温下,酸性大红GR染料废水初始浓度为300 mg/L,污泥活性炭的最佳投加量为2%(质量分数),吸附15min,废水色度脱除率可达99.6%,TOC去除率可达99.7%,利用等温吸附实验作吸附等温线,吸附等温线可以用Freundlich或Langmuir方程描述.     

磷酸活化植物基活性炭对水溶液中铅的吸附

以棉秆与互花米草为原料,采用磷酸活化法制备了低成本的植物基活性炭,通过静态实验研究了其对重金属铅的吸附性能。结果表明,在活化温度为500℃、活化时间为2 h条件下,制备的棉秆和互花米草活性炭比表面积为1 570m2/g和856 m2/g,含氧酸官能团含量分别为1.43 mmol/g和1.27 mmol/g。在25℃下,两种活性炭对重金属铅的Langmuir最大吸附量分别为119 mg/g和111 mg/g,吸附最佳pH为4.3,吸附平衡符合Freundlich方程,离子交换在吸附过程中发挥了重要作用。     

剩余污泥制备活性炭及其应用研究

以城市污水处理厂二沉池排出的剩余污泥为原料,采用不同活化方法制备活性炭,同时对比活化效果,研究了制备工艺条件对污泥活性炭吸附性能及产率的影响。结合比表面积、孔径分布和扫描电镜表征分析,对制备的污泥活性炭的性能进行评价,并探讨了污泥活性炭作为水处理吸附剂的去除效果。结果表明,以ZnCl₂为活化剂制备的活性炭性能较好,其最佳制备条件为：活化温度550℃,活化时间45 min,ZnCl₂浓度40％,固液比1∶2。制得的污泥活性炭的碘吸附值为496 mg/g,产率为51.8％,比表面积为301.4 m²/g,孔体积为0.37 mL/g,微孔体积为0.08 mL/g,平均孔径为5.78 nm。将该产品用于处理城市污水,投加量为0.8％,吸附平衡时间约为60 min时,对COD的去除率为81％,吸附容量为42.53 mg/g。     

长柄扁桃核壳活性炭的制备及表征

以长柄扁桃核壳为原料采用磷酸活化法制备活性炭,分别研究了温度、时间、浸渍比和磷酸浓度对活性炭吸附性能的影响;进而采用氮气吸附曲线和SEM对最佳工艺条件下的活性炭进行了表征。结果表明,长柄扁桃核壳是一种优质的活性炭原料;当温度为400℃,活化时间2 h,浸渍比2：1,磷酸浓度60%时,得到产率为46.46%,碘吸附值和亚甲基蓝吸附值分别为1 073 mg/g、255 mg/g,比表面积高达1 740 m²/g,中孔率为73.12%的孔隙发达的高中孔率活性炭。     

微波法污水厂污泥制备活性炭的研究

研究了以污水厂污泥为原料、微波辐照下磷酸活化法制备污泥活性炭的工艺条件,探讨了微波功率、辐照时间以及磷酸浓度对活性炭碘值的影响.结果表明,微波功率480 W、辐照时间315 s、磷酸浓度40%～45%的条件下,制备的污泥活性炭碘值为301 mg/g,总孔孔容是0.37 mL/g,平均孔径8.8 nm,比表面积168 m2/g.将该污泥活性炭用于处理TNT红水,吸附效果良好.     

Characterization of activated carbons prepared from sugarcane bagasse by ZnCl2 activation.

Activated carbons were prepared from the agricultural waste of sugarcane bagasse by the chemical activation with zinc chloride (ZnCl2) at the activation temperature of 500 degrees C with soaking time of 0.5 hour. The influence of activation parameters on the final carbon products was examined by varying the impregnation ratio (i.e., mass ratio of added ZnCl2 to bagasse) and bagasse size. The physical properties of carbon products were characterized by nitrogen adsorption/desorption isotherms (at 77 K) and helium displacement method. The surface area and pore volume of carbons were thus obtained by the BET equation and t-plot method. Also, the particle density and porosity of carbons were estimated by the total pore volume and true density. The increases of the values of surface area and pore volume are approximately proportional to the impregnation ratio. The microporous carbon product with the BET surface area of 905 m2/g and total pore volume of 0.44 cm3/g was obtained in the present study. Further, the adsorption isotherms of two acid dyes from aqueous solutions onto the carbon products were performed at 30 degrees C. The results show that the adsorption isotherms of acid dyes with high molecular weight or large molecular size on the microporous adsorbents of activated carbons are plateau forms, indicating multilayer adsorptions, which may be attributed to the steric hindrance of the adsorbate molecules.     

Optimization of preparation process of activated carbon from chestnut burs assisted by microwave and pore structural characterization analysis

In this study, activated carbon was prepared from Chinese chestnut burs assisted by microwave irradiation with potassium hydroxide (KOH) as activator, and the process conditions were optimized employing Box-Behnken design (BBD) and response surface methodology (RSM). The optimized variables were irradiation time, impregnation time, and mass ratio of alkali-to-carbon, and the iodine adsorption value was used to evaluate the adsorption property of activated carbon. The optimal preparation conditions were determined as follows: irradiation time 17 min, impregnation time 240 min, and mass ratio of alkali-to-char 1.5:1. Meanwhile, the relatively high iodine adsorption value (1141.4 mg/g) was also obtained. Furthermore, the pore structural characterization of activated carbon was analyzed. The analyzed results showed a larger Brunauer-Emmett-Teller (BET) specific surface area (1254.5 m²/g) and a higher microporosity ratio (87.2%), a bigger total pore volume (0.6565 m³/g), but a smaller average pore size (2.093 nm), which demonstrated the obtained activated carbon possessed strong adsorption capacity and well-developed microporous structure. This research could not only establish the foundation of utilizing chestnut burs to prepare activated carbon, but also provide the basis for exploitation of Chinese chestnut by-products.

Implications: Because Chinese chestnut burs are the by-products and usually discarded upon harvesting subsequently, the utilization of chestnut burs as a potential source of activated carbon is of great profit to the chestnut processing industries.     

浸渍-碱性微波法载磁活性炭粉对壬基酚的吸附

利用浸渍-碱性微波法制备载磁粉末活性炭,通过等温吸附实验和动力学吸附实验,研究对比了其与原料活性炭、浸渍载铁活性炭对壬基酚的吸附性能。采用氮气吸附仪、FTIR、XRD、国标(GB/T12496.19-1999)邻菲啰啉分光度法及VSM,分别对3种样品进行了物相结构、表面官能团、铁含量及磁性能的分析,并探讨了吸附机理。结果表明,浸渍-碱性微波法载磁活性炭的总孔容及孔隙率均有较大提高;其吸附等温线符合Freundich方程,吸附动力学过程符合准二级动力学方程与孔道内扩散模型,相关系数R2均大于0.900。原活性炭经一定浓度的铁盐溶液浸渍后,铁含量由2%提高到8%。在碱性、N2气氛条件下微波后,铁系物主要存在形式为零价铁和Fe3O4,制得的载磁活性炭饱和磁化强度为1.12 emu/g。     

Adsorption of acid dye onto activated carbons prepared from agricultural waste bagasse by ZnCl2 activation

A series of activated carbons were prepared from agricultural waste sugarcane bagasse by chemical activation with zinc chloride (ZnCl2) as an activating agent at 500 degrees C and 0.5 h soaking time. The Langmuir surface area and total pore volume were used to estimate the average pore diameter of the carbon products. The values of the surface area and pore volume increased linearly with increase in the impregnation ratio (IR) up to 100 wt%. The adsorption capacities of the derived adsorbents for Acid Orange 10 were measured at 20 degrees C and 40 degrees C to gain further insights into the acidic surface oxides of the adsorbent from the results of Fourier transform infrared (FTIR) spectroscopy analysis and pH measurement. Adsorption isotherms of the acid dye on adsorbents prepared were determined and correlated with common isotherm equations. It was found that the Langmuir model appears to fit the isotherm data better than the Freundlich model. The physical properties of these adsorbents were consistent with the parameters obtained from the isotherm equations.     

活性炭和沸石对氨氮的吸附特性及生物再生

采用活性炭和沸石作为吸附材料,分别考察了这两种吸附材料对水体中氨氮的吸附特性及其生物再生性能。实验结果表明,活性炭和沸石对水体中氨氮的等温吸附符合Freundlich等温式,其拟合度分别为0.9783和0.9303;静态吸附结果表明活性炭和沸石均具有较好的氨氮吸附性能,24 h内沸石对氨氮的吸附能力为1.27 mg/g,高于活性炭的0.53 mg/g;动态吸附中沸石达到吸附饱和的时间为96 h,较活性炭达到吸附饱和的时间长,沸石显示出作为氨氮吸附剂的优越性;活性炭和沸石经过96 h的生物再生后吸附性能获得一定程度的再生,出水中氨氮浓度比未进行生物再生前分别降低17.31 mg/L和8.32 mg/L,且都在表面形成了稳定的生物膜。     

微波活化制备加拿大一枝黄花活性炭及对Cd（Ⅱ）的吸附

以入侵植物加拿大一枝黄花为原料,在400℃氮气保护下,直接碳化90 min后,以KOH为活化剂,微波活化的方法制备了高比表面积微孔活性炭SCAC。结果显示活性炭SCAC的表面面积为1 888 m2/g,总孔容量为0.804 cm3/g,微孔容量为0.741 cm3/g,平均孔径0.567 nm,微孔平均孔径0.488 nm。通过静态吸附实验研究了活性炭添加量、溶液初始浓度、初始pH及吸附时间对SCAC吸附Cd(Ⅱ)的影响,通过动力学方程拟合探讨了活性炭对Cd(Ⅱ)的吸附机理。结果表明,吸附平衡时间、最佳pH及活性炭添加量分别为120 min、pH>7.5及0.05 g/50 mL,活性炭SCAC吸附动力学过程符合准二级方程模型。     

UTILIZATION OF AGRICULTURAL WASTE CORN COB FOR THE PREPARATION OF CARBON ADSORBENT

In the present study, a series of activated carbons were prepared from agricultural waste corn cob by chemical and physical activations with potassium hydroxide (KOH)/potassium carbonate (K₂CO₃) and carbon dioxide (CO₂). The effect of process variables such as impregnation ratio, impregnation time, activation temperature and soaking time of CO₂ was studied in order to relate these preparation parameters with the physical properties of final carbon products. The resulting activated carbons were characterized by nitrogen adsorption[ch-[chdesorption isotherms at 77 K. The surface areas and pore volumes of carbons were estimated by the BET equation, the Langmuir equation and the t-plot method. Under the experimental conditions investigated, the main parameters in the activation of corn cob were found to be the impregnation ratio and activation temperature. The soaking time of CO₂ is another important variable, which had a strong effect on the pore volume development. The BET surface area and total pore volume were as large as about 2000 m²/g and about 1.0 cm³/g, respectively. This study showed that the activation of agricultural waste corn cob with KOH/K₂CO₃ and CO₂ was suitable for the preparation of large-surface-area activated carbons.     

改性污泥活性炭对水中镉离子的吸附性能

以城市污水处理厂的剩余污泥为原料,氯化锌为活化剂制备污泥活性炭,对一部分污泥活性炭用6.0 mol/L的硝酸进行改性,并研究了未改性和改性的污泥活性炭对Cd2＋的吸附行为的影响。结果表明,在pH为5.0、Cd2＋初始浓度为100 mg/L、吸附剂投加量为2.0 g/L、反应温度为25℃时,未改性的污泥活性炭吸附容量为8.45 mg/g,硝酸改性的污泥活性炭吸附容量达到了23.35 mg/g。改性和未改性的污泥活性炭对Cd2＋都有较好的吸附容量,硝酸改性大幅度提高了污泥活性炭对Cd2＋的吸附性能。常温下改性污泥活性炭对Cd2＋的吸附符合Langmuir吸附等温式。     

Utilization of agricultural waste corn cob for the preparation of carbon adsorbent

In the present study, a series of activated carbons were prepared from agricultural waste corn cob by chemical and physical activations with potassium hydroxide (KOH)/potassium carbonate (K2CO3) and carbon dioxide (CO2). The effect of process variables such as impregnation ratio, impregnation time, activation temperature and soaking time of CO2 was studied in order to relate these preparation parameters with the physical properties of final carbon products. The resulting activated carbons were characterized by nitrogen adsorption-desorption isotherms at 77 K. The surface areas and pore volumes of carbons were estimated by the BET equation, the Langmuir equation and the t-plot method. Under the experimental conditions investigated, the main parameters in the activation of corn cob were found to be the impregnation ratio and activation temperature. The soaking time of CO2 is another important variable, which had a strong effect on the pore volume development. The BET surface area and total pore volume were as large as about 2000 m2/g and about 1.0 cm3/g, respectively. This study showed that the activation of agricultural waste corn cob with KOH/K2CO3 and CO2 was suitable for the preparation of large-surface-area activated carbons.