首页 | 本学科首页   官方微博 | 高级检索  
相似文献
 共查询到19条相似文献,搜索用时 218 毫秒
1.
粉煤灰处理含氟废水的正交试验研究   总被引:6,自引:0,他引:6  
对粉煤灰处理含氟废水进行了正交试验研究。结果表明各因素对F-去除率的影响顺序为:pH>V/M>T>CF-,极差R分别为49.6、9.1、4.9和3.6;在pH=5、V/M=10、T=3h时,粉煤灰对于CF-<500 mg/L的废水具有较好的去除效果;粉煤灰吸附F-的行为符合Langmuir等温方程,方程为Ce/qe=0.251 8Ce+6.087 3。  相似文献   

2.
坡缕石对Zn^2+的吸附性能及吸附工艺条件优化研究   总被引:1,自引:2,他引:1  
从坡缕石粘土提纯人手,进行了坡缕石吸附Zn^2 的实验研究,结果表明坡缕石对水中Zn^2 的吸附性能主要受振荡速度、吸附时间、溶液pH值、吸附剂用量等因素影响,30℃时坡缕石对Zn^2 的等温吸附曲线同时符合Langmuir方程和BET方程。在本实验条件下,坡缕石对水中的Zn^2 (20mL,Zn^2 浓度均为50mg/L)的最佳吸附工艺条件为:振荡速度150r/min,吸附时间120min,吸附剂用量0.120g,溶液pH为6.2,此条件下去除率达到T95.5%。  相似文献   

3.
利用粉煤灰处理含铜废水的实验研究   总被引:8,自引:0,他引:8  
研究了粉煤灰去除废水中铜离子的速率、粉煤灰投加量对粉煤灰去除废水中铜离子的影响和粉煤灰对质量浓度不同的含铜离子废水的去除效果,进一步探讨了粉煤灰去除铜离子的机理,实验结果显示粉煤灰在去除废水中铜离子的过程中反应3 h后就达到了平衡,粉煤灰对Cu2 的去除率随粉煤灰投加量的增加而增加,但是就充分利用吸附剂粉煤灰的角度而言,并非其投加量越多去除量越大,粉煤灰吸附废水中的铜离子更符合Langmuir模型,而不是Freundlich模型;粉煤灰去除废水中的Cu2 主要是静电吸附、阳离子交换吸附和表面络合吸附作用,但是,当用碱性粉煤灰处理质量浓度较低的含Cu2 废水时,生成Cu(OH)2的沉淀作用可能占主要的地位.  相似文献   

4.
利用13X沸石分子筛净化含Pb~(2+)废水的实验研究   总被引:11,自引:0,他引:11  
马鸿文  肖万  陶红 《现代地质》2003,17(2):157-162
采用静态间歇法 ,实验研究了含Pb2 +废水的 pH值及吸附时间对 13X沸石分子筛吸附Pb2 +性能的影响 ,得出了最佳去除效果的优化条件为 :废水的 pH值接近中性 ,吸附时间 10min。通过吸附实验 ,确定了在Pb2 +初始浓度为 2 0mg/L的条件下 ,13X沸石对Pb2 +的吸附量为 2 1 4 2mg/g ,即每克沸石净化含Pb2 +废水的最大体积量约为 75 0mL。解析实验表明 ,加入沉淀剂 ,浓缩洗脱液中的Pb2 +即以PbS的形式生成沉淀 ,为回收金属铅提供了可能 ;13X沸石在循环使用 5次的条件下 ,对废水中Pb2 +的吸附率仍高达 98% ,重复使用性能良好。经处理后的净化水中Pb2 +的浓度小于 0 4mg/L ,显著低于国家废水排放标准GB8978 88的指标 ( 1 0mg/L)。 13X沸石对Pb2 +的主要吸附形式是离子交换和表面络合反应。  相似文献   

5.
用固相反应法和sol-gel法合成了不同类型的磷灰石(AP),并采用TEM、XRD、IR、BET比表面积法及静、动态吸附等方法研究了不同AP的比表面积、结晶度、晶胞参数、结晶尺寸、晶格缺陷度、Ca/P摩尔比和煅烧温度等与吸氟能力的关系,结果表明:结晶度高、晶粒大的AP有较小的吸氟量,属表面单分子层化学络合吸附机理;酸活化的AP有较大的吸氟量,属溶解-沉淀与沉淀物表面纳米尺寸效应吸附的复合去氟机理;具纳米尺寸的HAP在常温、常压、无二次污染、小于11mg/L的低含氟浓度废水中且不酸化情况下有较大吸氟量,属纳米尺寸效应吸附机理。  相似文献   

6.
天然锰钾矿处理含Cd^2+废水实验研究   总被引:5,自引:2,他引:5       下载免费PDF全文
利用天然锰钾矿处理实验室内配置的含Cd^2 废水,结果表明:天然锰钾矿对水溶液中Cd^2 的去除达平衡需2d以上;锰钾矿粒径越小对Cd^2 的去除量越大;溶液中例Cd^2 的浓度不太高时,去除量随溶液浓度的升高而增大;在酸性介质中去除量随pH值增大先降低后增大,pH值超过6.3时天然锰钾矿表面开始带负电荷,在弱碱性介质中去除量最大;不同电解质对去除量的的影响主要是由Cl^-与Cd^2 的络合造成的。实验浓度范围内能很好地用Langmuir吸附等温线拟合,对Cd^2 0的最大吸附量为5.54mg/g。锰钾矿处理含Cd^2 废水的过程中伴随有K^ 和Mn^2 溶出。处理Cd^2 后的锰钾矿渣,经超声并淋滤后仍有大部分的Cd^2 被固持,固持率可达去除量的79.82%。  相似文献   

7.
炉渣处理含磷废水的实验研究   总被引:9,自引:0,他引:9       下载免费PDF全文
以炉渣作为吸附剂,用静态吸附实验方法研究了炉渣对模拟含磷废水脱磷的一般规律,结果表明,炉渣是一种有效的吸附剂,对废水中的磷有较强的吸附去除性能。影响炉渣除磷的主要因素有吸附时间、炉渣用量、pH值和原水含磷浓度。在含磷浓度2~13mg/L、炉渣用量5g/L、中性、吸附时间为2h的实验条件下,磷的去除率可高达99%以上。  相似文献   

8.
采用电-Fenton法对含苯酚废水进行处理,以石墨为阴极、铁为阳极,并向阴极不断通入空气,电解过程产生的H2O2与阳极溶解的Fe^2+形成Fenton试剂,Fenton试剂在电解过程中产生大量活性羟基自由基,能够很好地氧化降解废水中的苯酚。实验结果表明:影响苯酚去除率的因素主次顺序为pH值、电解质浓度、电解电压、电解时间、进水苯酚浓度。单因素分析得出电-Fenton法处理苯酚模拟废水的最优反应条件:pH值控制在2左右,反应时间为60min,电解电压选10V,Na2SO4的浓度为30g/L,进水苯酚浓度为150mg/L。在最优条件下苯酚的去除率为82%。  相似文献   

9.
氟广泛分布于地下水且与人体健康相关,世界上许多国家和地区均存在高氟水。本文以江西省均村-高兴地区为例,结合区域水文地质调查成果开展地下水中氟水文地球化学特征研究,探讨研究区地下水中F-的分布特征与来源。对研究区4个地下水系统中的442个地下水样品的F-、Ca2+、HCO_3^-浓度及pH值、TDS等进行分析,研究认为各地下水系统地下水中的F-浓度与Ca2+浓度、HCO_3^-浓度、pH值、TDS正相关,含氟矿物的溶解是地下水中氟的主要来源,较强烈的地下水交替条件及弱酸性的地下水特征是导致地下水中氟浓度低的重要原因。  相似文献   

10.
药剂与粉煤灰联合处理再生造纸废水的实验研究   总被引:2,自引:1,他引:1  
通过混凝实验探讨了用PAC处理再生造纸废水的最佳混凝条件.在此基础上,选用PAM为助凝剂,通过正交实验,获得了较佳的水平条件:先加PAM,质量浓度为3 mg/L,后加PAC,质量浓度为0.2 g/L,反应9 min;处理后的出水经粉煤灰过滤,ρ(COD)可降至37.383 mg/L,ρ(BOD)为20.7 mg/L,浊度为0,pH为11.12,在空气中放置24 h后pH变为8.02.  相似文献   

11.
循环流化床燃烧产生的粉煤灰按不同比例与污水充分混合,其对污水中P的去除率可达90%以上;对COD的去除率为45%左右;对NH3-N的去除效果较差,最高不超过11%。由于粉煤灰含有大量钙,可以与粉煤灰中的磷酸盐形成沉淀,故采用循环流化床产生的粉煤灰可以有效处理含P较高的污水。文章研究了粉煤灰中重金属在污染水中释放规律,如Pb、Cd、Cu、Cr及Ni等,由于粉煤灰与污水浸泡后pH值呈碱性,且污水中含有大量有机物质,使反应体系呈还原状态。因此,粉煤灰中的重金属可以稳定存在,粉煤灰在污水中几乎不释放重金属,所以未加任何处理的粉煤灰在浸泡过程中不会对环境产生重金属污染。为此,粉煤灰可用于井下采空区回填,也可用于路基填充等。由于粉煤灰中少量碱性物质溶于水中,可使地下水pH值升高。  相似文献   

12.
水热条件下利用微波加热从粉煤灰合成沸石研究   总被引:14,自引:0,他引:14  
着重选用NaOH水溶液为反应前驱物, 通过改变反应温度、NaOH浓度与合成时间等参数, 在水热条件下利用微波加热直接对粉煤灰进行晶化, 合成得到了浊沸石、菱沸石、NaP1沸石3种沸石.粉煤灰转化为沸石率约15%~40%.研究表明: (1) 反应体系在15min左右即有合成沸石产生, 30min左右合成沸石转化率达到最佳; (2) 为保证沸石晶核生成和晶体的生长, 反应体系的溶液/粉煤灰比不应低于2.5; (3) 在溶液/粉煤灰比为2.5时, 应控制加热时间在30min左右.   相似文献   

13.
Abstract. Municipal solid waste combustion leads to concentration of various metals in the solid residue (fly ash) remaining after combustion. These metals pose serious environmental hazard and require proper handling and monitoring in order to control their harmful effects. Leachability of some metals from fly ash was examined in fly ash and Milli-Q water mixture (liquid-to-solid ratio, 100) under various temperature and pH conditions in the laboratory. The leaching experiments conducted for 24 hours showed that pH was generally more important than temperature in controlling the amount of metals leached out of the fly ash. However, at a given pH, rise in temperature led to different degree of (usually one to two fold) enhanced or reduced leaching of metals. Owing to amphoteric nature of oxides of Al, Cr, Pb and Zn, these metals often yielded typical pattern of increase and decrease in their concentrations with change in pH. The extent of leaching of Cr and Pb in our experiments suggests that decrease of pH to acidic range in the case of Pb and to neutral to acidic range for Cr over a long period of storage of fly ash at solid waste dumping site may facilitate leaching of these metals from fly ash, leading to contamination of groundwater to the level that exceeds beyond the level permitted by the environmental laws.  相似文献   

14.
In some regions of the world, the concentration of fluoride in groundwater is high. To reduce the amount of fluoride to acceptable drinking water standard, it is highly recommended to treat the water. Fluoride adsorption in aqueous solution by a hybrid resin was studied in this research because of its functional groups likeness with goethite. Kinetic data showed that F adsorption was rapid in the beginning and maximum uptake occurred in within 10 min and equilibrium reached within 100 min. The experimental results showed that fluoride adsorption was influenced by pH of solution and optimum operating pH was in the range of 3 to 5.5. Langmuir model was applicable to the present study and F ions were exchanged with hydroxide ions in nano-scaled structure on the surface of sorbent. This adsorbent with 61 % efficiency is suitable for the regions where F concentration is less than 4 mg/L.  相似文献   

15.
朱蕾  董娅玮  于学君  李琦  郭婷婷 《地下水》2007,29(4):102-104
石油废水中含有多种有机物,成分复杂,其治理是当今急需解决的问题.用自制的反应器以石墨为电极材料,应用脉冲电解方法,进行处理石油废水的实验.实验结果表明:在电解时间 30 min,电解电压 10 V,脉冲电源频率 3 750 Hz,占空比 50 %,pH=9,电极间距 2.5 cm,电极直径 1.0 cm,电解质浓度 0.2 % 的条件下进行电解,废水的处理效果可达到 89 % 以上.处理后的废水低于国家第二类污染物最高允许排放浓度的二级排放标准.脉冲电解法不但处理含油废水效果显著,而且设备简单,易于操作,为处理石油废水提供了一项新技术.  相似文献   

16.
The aim of this study was to investigate the geochemical characteristics of arsenic in the solid material samples of the Mae Moh Mine and also the Mae Moh power plants fly ash samples were systematically studied. Arsenic concentration in overburden, coal lignite and fly ash are variable (depending on source of solid samples). The results show that the strata of overburden, J seam of coal and fly ash are rich in arsenic and also relatively soluble from fly ash; it occurs as a surface precipitate on the ash particle. The experimental study on speciation in the strata also indicates that the arsenic speciation of Mae Moh solid samples are mainly arsenate, As (V), which are approaching exceed 80%. Arsenic content in the main of overburden is in the range of 14.3–888.8 mg/kg, which is larger than the arsenic background soil values. Solid materials polluted wastewater; the arsenic speciation was present predominantly as arsenate in the surface water of a series of Mae Moh solid materials basins.  相似文献   

17.
垃圾焚烧飞灰水泥固化体强度稳定性研究   总被引:1,自引:0,他引:1  
针对垃圾焚烧飞灰安全处置技术要求,采用水泥对其进行固化、稳定化处理,研究了不同水泥添加量、不同养护时间和渗沥液浸泡时间对固化体无侧限抗压强度及破坏特性的影响,并对垃圾渗沥液的侵蚀机制进行了分析。结果表明:当水泥添加量小于5%,养护时间小于3 d时,飞灰固化体在渗沥液浸泡下迅速解体,垃圾渗沥液的侵蚀对飞灰固化体的强度有较大的影响,浸泡后的固化体呈现出明显的应变软化特征,而未经浸泡的固化体的强度增长符合y=a[1-exp(-bt)]模式。随着水泥添加量及养护时间的增加,飞灰固化体无侧限抗压强度增加,破坏应变减小,而随着浸泡时间的增加,飞灰固化体的无侧限抗压强度先增大后减小,转折点大约在5~7 d,破坏应变近似呈线性增大。渗沥液对飞灰固化体的侵蚀主要是其成分抑制了固化体水化反应和破坏了水化产物。研究成果可为垃圾焚烧飞灰的安全处置技术提供理论依据和参数支持。  相似文献   

18.
Acid mine drainage was reacted with coal fly ash over a 24 h reaction time and species removal trends evaluated. The evolving process water chemistry was modeled by the geochemical code PHREEQC using WATEQ4 database. Mineralogical analysis of the resulting solid residues was done by X-ray diffraction analysis. Selective sequential extraction was used to evaluate the transfer of species from both acid mine drainage and fly ash to less labile mineral phases that precipitated out. The quantity of fly ash, volume of acid mine drainage in the reaction mixture and reaction time dictated whether the final solution at a given contact time will have a dominant acidic or basic character. Inorganic species removal was dependent on the pH regime generated at a specific reaction time. Sulphate concentration was controlled by precipitation of gypsum, barite, celestite and adsorption on iron-oxy-hydroxides at pH > 5.5. Increase of pH in solution with contact time caused the removal of the metal ions mainly by precipitation, co-precipitation and adsorption. PHREEQC predicted precipitation of iron, aluminium, manganese-bearing phases at pH 5.53–9.12. An amorphous fraction was observed to be the most important in retention of the major and minor species at pH > 6.32. The carbonate fraction was observed to be an important retention pathway at pH 4–5 mainly due to initial local pockets of high alkalinity on surfaces of fly ash particles. Boron was observed to have a strong retention in the carbonate fraction.  相似文献   

19.
The adsorption of fluoride ions on ground fired clay pot has been investigated. The maximum efficiency of the adsorbent for defluoridating 1–2 litres of water was found to be 200 mg fluoride kg−1 adsorbent. The investigation showed that 5–20 mg l−1 fluoride, from 1 litre of water, could be reduced to less than 1.5 mg l−1 using 120–240 g of the adsorbing medium. The effects of the dose of the medium, the pH, the contact time and the initial fluoride content were studied in relation to defluoridation efficiency. Comparison of fluoride removal capacity of the adsorbent was also made with those of fired brick, clay soil and red ash. The latter exhibited practically no adsorption. A packed column of the same ground clay pot was saturated with 285 mg fluoride kg−1 of adsorbent when 20 litres of water containing 10 mg l−1 F was allowed to pass through it. This column defluoridated 6 litres of tap water containing 10 ppm F to below 1.5 mg l−1.  相似文献   

设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号