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1.
Carbon–silica materials with hierarchical pores consisting of micropores and mesopores were prepared by introducing nanocarbon microspheres derived from biomass sugar into silica gel channels in a hydrothermal environment.The physicochemical properties of the materials were characterized by nitrogen physical adsorption(BET),scanning electron microscopy(SEM),and thermogravimetric(TG),and the adsorption properties of various organic waste gases were investigated.The results showed that microporous carbon materials were introduced successfully into the silica gel channels,thus showing the high adsorption capacity of activated carbon in high humidity organic waste gas,and the high stability and mechanical strength of the silica gel.The dynamic adsorption behavior confirmed that the carbon–silica material had excellent adsorption capacity for different volatile organic compounds(VOCs).Furthermore,the carbon–silica material exhibited excellent desorption characteristics:adsorbed toluene was completely desorbed at 150℃,thereby showing superior regeneration characteristics.Both features were attributed to the formation of hierarchical pores.  相似文献   
2.
Two chromium removal experiments were performed in bioreactors with and without a magnetic field under the same conditions.The release of the chromium present in the biomass was tested in two experiments one with the initial pH of the medium and one with pH 4.0.The objective was to remove Cr(Ⅵ) and total Cr from the effluent,this was carried out by placing biological treatments of synthetic effluent contaminated with 100 mg/L of Cr(Ⅵ) in a bioreactor with neodymium magnets that applied a magnetic field(intensity85.4 mT) to the mixed culture.The removal of Cr(Ⅵ) was approximately 100.0% for the bioreactor with a magnetic field and 93,3% for the bioreactor without a magnetic field for9 hr of recirculation of the synthetic effluent by the bioreactor.The removal of total Cr was61.6% and 48.4%,with and without a magnetic field,respectively;for 24 hr.The desorption of Cr(VI) in the synthetic effluent was 0.05 mg/L,which is below the limit established by Brazilian legislation(0.1 mg/L) for the discharge of effluent containing Cr(Ⅵ) into bodies of water.The results obtained for the removal of chromium in synthetic effluent suggested that there was no significant influence on the viable cell count of the mixed culture.The desorption of Cr(Ⅵ) in synthetic effluent after bioadsorption of chromium by the mixed culture in the process of removal of chromium in bioreactors with and without a magnetic field was not significant in either of the experiments with different initial pHs.  相似文献   
3.
综述了预富集技术在无机痕量分析中的应用,概述了国内外最新进展,介绍了主要技术及方法的特点,大量文献表明预富集技术用于痕量分析取得满意的效果,降低了检测限,提高了灵敏度。  相似文献   
4.
在雾稳定的条件下,研究了雾滴穿过SO_2烟羽沉降到地面的过程中吸收、析解以及酸化等过程。结果表明,雾对烟羽中SO_2的清除具有某些奇特的现象。即仅在离源较远的区域才表现出有限的清除作用:而在近源区,主要以析解为主,使源附近地面SO_2浓度增加,高架源成了低架源。雾滴在地面附近的这种析解作用,是造成雾天污染物浓度高的重要原因之一。  相似文献   
5.
曲霉对水中重金属的吸附去除   总被引:15,自引:0,他引:15  
利用2种曲霉A.sojae M146和A.oryzae M149的菌体,作为吸附剂对水中Pb^2+和Cd^2 进行去除实验。结果表明,曲霉菌体的最佳培养时间为72h,吸附的最佳pH为5.5、温度为30℃、时间为1h。在最佳实验条件下,A.sojae M146对Pb^2 和Cd^2 的吸附率,分别为69.76%和72.28%;A.oryzae M149对Pb^2 和Cd^2 的吸附率,分别为60.64%和81.34%。使用稀碱溶液对曲霉菌体进行浸泡预处理后,可提高对重金属的吸附去除效果;而使用稀释、乙醇水溶液以及蒸馏水对菌体浸泡后,明显降低了重金属的去除效果。Na2CO3和EDTA溶液,可以有效地将重金属从曲霉体上解吸下来,从而达到重复利用菌体作为吸附剂的目的。  相似文献   
6.
采用哌嗪等二元胺和二乙醇胺为吸收剂,对模拟烟气进行SO2的吸收解吸实验研究,筛选出性能优异的吸收剂,并考察添加剂H2 S O 4对其性能的影响。实验表明:可再生胺类吸收剂脱硫率可接近100%,二元胺吸收剂较醇胺的SO 2吸收量大、pH值随时间变化慢、首次解吸率高;羟乙基支链对胺类吸收剂的抗氧化能力、SO2吸收量和首次解吸率均有影响,环状二元胺比链状二元胺的抗氧化能力好、首次解吸率高;在N-(2-羟乙基)哌嗪溶液中添加硫酸构成N-(2-羟乙基)哌嗪/H 2S O 4脱硫体系后,脱硫率未受影响、SO2吸收量变小、首次解吸率显著提高,具有更好的循环使用性能。  相似文献   
7.
We determined the maximum amounts of added phenanthrene, chrysene, and 2,5-dichlorobiphenyl sorbed onto high-energy adsorption sites in a sediment on bi-solute experiments. The bi-solute pairs were phenanthrene/chrysene and phenanthrene/2,5-dichlorobiphenyl. On the bi-solute sorption experiments, one solute was introduced and equilibrated with sediment prior to addition of the second solute. The values for the maximum amounts adsorbed onto high-energy sites revealed that, after equilibration of the first solute, still some high-energy sites could be occupied by the second solute. Phenanthrene, chrysene, and 2,5-dichlorobiphenyl seem to share about 30% of the accessible high-energy adsorption sites in the sediment employed.  相似文献   
8.
Previous work has shown that arsenic can accumulate in drinking water distribution system (DWDS) solids (Lytle et~al., 2004) when arsenic is present in the water. The release of arsenic back into the water through particulate transport and/or chemical release (e.g. desorption, dissolution) could result in elevated arsenic levels at the consumers' tap. The primary objective of this work was to examine the impact of pH and orthophosphate on the chemical release (i.e. desorption) of arsenic from nine DWDS solids collected from utilities located in the Midwest. Arsenic release comparisons were based on the examination of arsenic and other water quality parameters in leach water after contact with the solids over the course of 168~hours. Results showed that arsenic was released from solids and suggested that arsenic release was a result of desorption rather than dissolution. Arsenic release generally increased with increasing initial arsenic concentration in the solid and increasing pH levels (in the test range of 7 to 9). Finally, orthophosphate (3 and 5 mg PO4/L) increased arsenic release at all pH values examined. Based on the study results, utilities with measurable levels of arsenic present in their water should be aware that some water quality changes can cause arsenic release in the DWDS potentially resulting in elevated levels at the consumer's tap.  相似文献   
9.
水溶性巯基壳聚糖对污染土壤吸附态汞的解吸作用研究   总被引:1,自引:0,他引:1  
用两种巯基化试剂半胱氨酸(Cys)和硫代乙醇酸(Thi)与壳聚糖(CTS)反应,制备了两种水溶性巯基壳聚糖,即Cys-CTS和Thi-CTS,对比研究了这两种巯基壳聚糖与CTS对被染毒土壤中吸附态汞的提取能力.结果表明,Thi-CTS在pH=3、质量浓度为0.5g/L、用量为20 mL的条件下.对汞的提取率为59.44%,相同条件下CTS和cys-CTS对汞的最高提取率只有31.81%和10.15%.  相似文献   
10.
给水管壁生物膜会吸附水中的重金属元素积累在管壁生物膜中,在受到扰动时释放回到水体,危害饮用水水质安全。试验以上海管网末梢水为实验对象,研究了PVC、铸铁和紫铜等三种管材上生物膜对铅、镉的解吸特性。结果表明,PVC、铸铁和紫铜附着生物膜对铅的解吸容量qe分别为:5.92211μmol·m^-2、128.3051μmol·m^-2和21.1808,解吸速率常数k分别为:0.001060 m^2·μmol^-1·min^-1、0.000041 m^2·μmol^-1·min^-1和0.000503 m^2·μmol^-1·min^-1,对于镉元素三种材质的解吸容量qe分别为:14.71519μmol·m^-2、18.50481μmol·m^-2和2.25225μmol·m^-2;解吸速率常数k分别为:0.000102 m^2·μmol^-1·min^-1、0.001070 m^2·μmol^-1·min^-1和0.000103 m^2·μmol^-1·min^-1。  相似文献   
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