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1.
外置式超滤膜生物反应器处理油田废水   总被引:6,自引:0,他引:6  
采用外置式超滤膜生物反应器处理油田废水,废水中的有机物被生物接触氧化池填料上形成生物膜的微生物降解,然后通过中空纤维超滤膜进行过滤,出水中油的质量浓度在1m g/L以下,悬浮物的质量浓度在3m g/L以下。考察了细菌的筛选、生物膜的培养驯化及压力、温度等对膜通量的影响。实验结果表明,筛选出的3株高效原油降解菌有很好的除油效果;生物膜经培养驯化成熟后,生物接触氧化池内细菌浓度为1×106个/mL;膜通量随压力和温度的适当提高而增加,适宜的操作压力为0.08M Pa,温度为20~28℃。分别用超滤水反冲洗、稀碱、稀酸、杀菌剂(如N aC lO溶液)和清水冲洗被污染的超滤膜,可使膜通量恢复到新膜的98%以上;在生物除油工序后增加沉淀池,膜污染可减少约7.77%。  相似文献   

2.
陶粒填料生物滴滤塔处理二甲苯废气   总被引:10,自引:1,他引:9  
以两种不同的陶粒作为生物滴滤床填料净化二甲苯废气,研究了喷淋液量、气体流量、进气负荷、喷淋液中氨氮浓度及填料层高度对净化效率的影响,并对两种填料的使用效果进行了对比。结果表明:二甲苯废气进气流量越小、进气负荷越低,净化效果越好;充足的氮源是高净化率的保证;对于较高浓度的废气,需要适当增加填料层高来达到净化要求;使用具有比表面积大的陶粒作为填料,可以使设备挂膜时间更短、能耗更低,净化效率更高。  相似文献   

3.
以膨润土为基质,添加表面活性剂和助表面活性剂,制备了多孔黏土异构材料(PCHs),采用SEM和BET技术进行了表征,并将其用于气态萘的吸附。考察了吸附效果的影响因素,并探讨了吸附机理。表征结果显示,PCHs具有较大的比表面积,孔径分布均匀,兼具微孔和中孔结构。实验结果表明:当吸附温度为30℃、初始萘质量浓度为560 mg/m3、相对湿度为0时,PCHs对萘的平衡吸附量达370 mg/g,远高于膨润土和有机膨润土;吸附为放热过程,温度越高平衡吸附量越低;平衡吸附量随初始萘质量浓度的增加呈非线性增长;水蒸气的存在导致萘的平衡吸附量减小;萘在PCHs上的吸附机理主要为表面物理吸附和有机质的分配作用。  相似文献   

4.
以含锌废催化剂为原料,经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌,再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比(硫酸与含锌废催化剂的质量比)对锌浸出率的影响,以及煅烧温度对纳米氧化锌质量的影响。实验结果表明:在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下,锌浸出率为92%;在最佳煅烧温度为400℃的条件下,氧化锌质量分数大于95%,比表面积大于50 m2/g;纳米氧化锌颗粒大小均匀,平均粒径小于50 nm。  相似文献   

5.
在自行设计的小型热态流化床反应器上,以金属镁渣作为脱硫剂,研究了镁渣粒径、反应温度、反应气体浓度对镁渣炉内脱硫性能的影响。研究结果表明,镁渣粒径越小,脱硫性能越好;在800~1 000℃范围内,镁渣的脱硫性能随着温度升高而升高;参与反应的SO2和O2浓度越大镁渣脱硫性能越好。实验中还发现水冷镁渣的脱硫性能明显优于自然冷却镁渣。实验所得结论为金属镁渣应用于流化床炉内脱硫提供了理论依据。  相似文献   

6.
采用颗粒活性炭掺杂生物质材料并在微波作用下制备了小麦秸秆(WH)微波生物炭和玉米秸秆(CB)微波生物炭,并用比表面积孔径分析仪、扫描电子显微镜和傅里叶变换红外光谱仪对其进行了表征,考察了微波生物炭对水中亚甲基蓝的吸附特性.实验结果表明:所制备的微波生物炭具有较大的比表面积和丰富的表面官能团,微波功率500 W制备的微波...  相似文献   

7.
田伟军 《化工环保》2014,34(1):64-66
以含锌废催化剂为原料,经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌,再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比(硫酸与含锌废催化剂的质量比)对锌浸出率的影响,以及煅烧温度对纳米氧化锌质量的影响。实验结果表明:在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下,锌浸出率为92%;在最佳煅烧温度为400 ℃的条件下,氧化锌质量分数大于95%,比表面积大于50 m2/g;纳米氧化锌颗粒大小均匀,平均粒径小于50 nm。  相似文献   

8.
针对某厂多介质过滤-超滤-反渗透(MMF-UF-RO)废水深度处理工艺发生污堵的问题, 采用在MMF装置前加入NaOH混凝沉淀的改进工艺代替加入聚合氯化铝(PAC)絮凝剂的原工艺.模拟原工艺水样的初始UF膜通量较低,过滤后UF膜通量下降35%左右;模拟改进工艺水样的初始UF膜通量较高,且UF膜通量基本无变化.改进工艺UF装置出水中除SiO_2外,其他物质的质量浓度远小于原工艺UF装置出水,可有效改善RO装置的进水水质.改进工艺的MMF和UF的运行稳定性均明显优于原工艺.  相似文献   

9.
本文在实测电厂灰水中悬浮物和COD的基础上。针对悬浮物对COD的影响。通过对灰水的过滤、澄清、混匀试验以及粉煤灰对COD的降解试验,探明了灰水中COD的超标原因并提出治理措施.  相似文献   

10.
玉米秸秆生物炭对苯胺的吸附   总被引:1,自引:0,他引:1       下载免费PDF全文
以玉米秸秆为原料制备生物炭吸附剂,研究了生物炭对水中苯胺的吸附性能。表征结果显示:制备的生物炭的比表面积为449.7 m2/g,体积平均粒径为103μm,主要以小粒径存在;制备的生物炭表面以碱性含氧官能团为主,含量为1.31 mmol/g。实验结果表明:在溶液p H 3、生物炭加入量10 g/L、吸附温度313 K、吸附时间3.0h的最佳反应条件下处理初始苯胺质量浓度为400 mg/L的苯胺溶液,苯胺去除率为94.0%,吸附量为37 mg/g;生物炭对苯胺的吸附过程符合拟二级动力学方程,吸附等温线满足Freundlich等温吸附方程;生物炭对苯胺的吸附是自发、吸热的过程;吸附过程中存在着水分子从生物炭表面的解吸。  相似文献   

11.
采用溶胶-凝胶法制备了纳米羟基磷灰石(n-HAP),使用FTIR、XRD、气体吸附仪等表征了n-HAP的物相及微观结构,并研究了n-HAP对模拟含Pb2+废水中Pb2+的吸附特性。实验结果表明:所制备的n-HAP粒径为24.39 nm,比表面积为53.50 m2/g,孔体积为0.32 cm3/g;n-HAP对Pb2+的去除率随吸附时间、吸附温度和溶液pH(小于6.5的实验范围)的增加而增大,随初始Pb2+质量浓度增大而减小;n-HAP对Pb2+的吸附较符合准二级吸附动力学方程,颗粒内扩散过程是吸附速率的控制步骤;Langmuir吸附等温方程比Freundlich吸附等温方程更适合描述n-HAP对Pb2+的吸附热力学行为,Pb2+在n-HAP上的吸附符合单分子层吸附形式。  相似文献   

12.
In this study, we have showed a facile route for fabrication of a novel microporous material based on chitosan (CS) and poly(vinyl alcohol) (PVA) biodegradable nanofibers that have high specific surface area, considerable porosity, and small diameter. Scanning electron microscopy, thermogravimetric analysis, differential scanning calorimetry, fourier transform infrared spectroscopy, Brunauer–Emmett–Teller surface area analysis, and CHNS/O elemental analyser were applied to characterize the fabricated CS/PVA composite nanofibers. Moreover, the influences of spinning conditions including concentration, voltage, electrospinning distance, and flow rate, on size distribution and pore diameter of the final product were systematically studied using 2k?1 factorial design experiments, and the response surface optimization was used for determining the best synthesis parameter. The results obtained from 2K?1 factorial design experiments showed that electrospinning parameters influenced the size distribution and pore diameter of the CS/PVA microporous material. Based on the response surface methodology, the CS/PVA product could be obtained with a high microporous diameter of 1.8 nm and a small diameter distribution of 15.0 nm under optimized conditions. The obtained results showed that the fabricated samples could be utilized in different applications.  相似文献   

13.
闫莎莎  张文泉 《化工环保》2012,40(4):436-441
以滕南煤田某煤矿风化煤矸石为研究对象,应用主成分分析法分析了煤矸石粒径对Pb,Cr,Cd溶出浓度的影响,应用回归分析法分析了浸溶时间与Pb,Cr,Cd溶出浓度的关系特征。实验结果表明:模拟湿地浸溶条件下,煤矸石中Pb,Cd,Cr溶出浓度均超出或接近Ⅲ类水体水质标准,对水环境存在污染风险;煤矸石粒径对Pb,Cd,Cr溶出浓度存在影响,粒径越小则Pb、Cr、Cd溶出浓度越大,粒径小于8.0 cm的煤矸石浸溶贡献较大。建立了表征Pb,Cr,Cd溶出浓度与浸溶时间对数(以10为底)关系的一元三次多项式回归方程,经检验均具有显著性。  相似文献   

14.
Colloids are present in groundwater aquifers and water-permeable engineered barrier systems and may facilitate the migration of radionuclides. A highly permeable mortar is foreseen to be used as backfill for the engineered barrier of the Swiss repository for low- and intermediate-level waste. The backfill is considered to be a chemical environment with some potential for colloid generation and, due to its high porosity, for colloid mobility. Colloid concentration measurements were carried out using an in-situ liquid particle counting system. The in-house developed counting system with three commercially available sensors allowed the detection of single particles and colloids at low concentrations in the size range 50-5000 nm. The counting system was tested using suspensions prepared from certified size standards. The concentrations of colloids with size range 50-1000 nm were measured in cement pore water, which was collected from a column filled with a highly permeable backfill mortar. The chemical composition of the pore water corresponded to a Ca(OH)2-controlled cement system. Colloid concentrations in the backfill pore water were found to be typically lower than approximately 0.1 ppm. The specific (geometric) surface areas of the colloid populations were in the range 240 m2 g(-1) to 770 m2 g(-1). The low colloid inventories observed in this study can be explained by the high ionic strength and Ca concentrations of the cement pore water. These conditions are favourable for colloid-colloid and colloid-backfill interactions and unfavourable for colloid-enhanced nuclide transport.  相似文献   

15.
Virgin activated carbon (VAC) was chemically activated by hydrochloric acid and aqueous ammonia to obtain different surface functionalities and nanopore distributions. The N-tailored AC (NAC) acquired by alkali treatment significantly enhanced the cadmium sorption capacity, while the Cl-tailored AC obtained by acidic modification decreased the sorption capacity compared with that of VAC. With increasing ammonia concentration in the basic treatment, the NAC surface area was increased with declining pore volume and diameter, which increased the adsorption capacity for Cd(II) removal. However, increasing HCl concentration in the acidic modification decreased the surface area, with increasing pore volume and diameter, which decreased the cadmium adsorption capacity. The basic treatment created more alkaline-rich sites such as nitrogen-containing functional groups, on the carbon surface, thereby improving cadmium removal efficiency. However, the acidic treatment generated a stronger acidic chemical structure and much more the formation of the acyl- and alkyl chloride groups that greatly inhibited the Cd(II) sorption capacity.  相似文献   

16.
In this study, a new type poly(vinyl alcohol)/peat composite bead is prepared and is shown suitable as a filter material for biofiltration. The optimal preparation condition is with the peat size of 16–35 mesh, the ratio of water to peat of 40g water/10 peat and the immersion time in the phosphate solution of 30min. The composite bead prepared by this process is a porous spherical particle with a density of 0.692 g/cm3. It contains phosphor and nitrogen nutrient are 2.91mg P/g dry solid and 3.25mg N/g dry solid, respectively. The diameter of composite bead is between 2.4 and 6.0mm and the average diameter is about 4.0mm. The equilibrium moisture content of the bead from adsorption and holding experiments are 50.5 and 66.8% on a wet basis, respectively, corresponding to the optimal filter material required and is sufficient to sustain biological activity as the bead adsorbs equilibrium moisture. The composite bead has higher moisture holding capacity and the compression strength than the pig manure compost filter material. The composite bead has buffer capacity and could maintain the filter bed at pH = 6.9–7.2 during the operation period. The percentage of removed ethyl acetate could stay at over 99% for 33 days operation while the composite bead adsorbed inorganic nitrate nutrient.  相似文献   

17.
以盐泥为原料,采用氯化铵浸取回收盐泥中的Mg2+,以浸取液和回收的氨反应制取氢氧化镁产品。考察了盐泥浆液固含量、浸取时间、物料比(氯化铵与盐泥中氢氧化镁的摩尔比)等工艺条件对Mg2+浸取率的影响,并以比表面积为考察指标进行正交实验,确定氢氧化镁的最佳制备条件。实验结果表明:在盐泥浆液固含量为248 g/L、浸取时间为100 min、物料比为2.3的条件下,Mg2+浸取率为75.0%;在n(MgCl2):n(NH4Cl)=0.5、氨水浓度3 mol/L、氨水滴加速率 0.8 mL/min、反应温度 90 ℃的最佳条件下,制备的氢氧化镁的比表面积为17.87 m2/g,粒径约为3 μm。该工艺简单可行,为盐泥的综合利用提供了新的思路。  相似文献   

18.
The present study focuses on the use of solid waste generated by the steel works in Brazil for manufacturing clay-based structural products. The waste sample was characterized regarding chemical composition, X-ray diffraction, particle size, morphology, specific surface and plastic properties. The waste was added in gradual proportions to a kaolinitic clay from zero up to 3 wt.%. Ceramic bodies were formed by vacuum extrusion and fired at 950 degrees C. The physical-mechanical properties (linear shrinkage, water absorption, apparent density and flexural strength) of the resulting clay/solid waste mixtures were determined. In addition, leaching tests were performed according Brazilian Standards as well as a preliminary analysis of gases evolved during the thermal process. It was found that the solid waste is formed by irregular particles, ranging in size from 1 to 500 microm. The test results indicate that solid wastes generated by steel works can be used as filler in construction materials, thereby increasing reuse in an environmentally safe manner.  相似文献   

19.
Recovery of nickel oxide from spent catalyst   总被引:3,自引:0,他引:3  
This study investigates the possibility of recovering nickel from the spent catalyst (NiO/Al2O3) resulting from the steam reforming process to produce water gas (H2/H2O) in many industries. In the extraction process, nickel is recovered as sulfate using sulfuric acid as a solvent. The considered parameters affecting nickel recovery were acid concentration, temperature and time of digestion solid:liquid ratio, particle size and stirring rate. Nickel was to be directly recovered as a sulfate salt by direct crystallization method. The conversion was 99% at 50% sulfuric acid concentration, solid: liquid ratio (1:12) by weight, particle size less than 500 micron for more than 5 h and 800 rpm at 100 degrees C.  相似文献   

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