吸附邻氯酚的超高交联树脂微波辅助再生研究

以NDA-150超高交联树脂为吸附剂,邻氯酚为吸附质,氢氧化钠稀溶液为脱附剂,采用微波间歇辐照的方法,对吸附氯酚树脂的再生过程进行了研究.系统分析了微波功率、辐照时间、碱液浓度对脱附效果的影响,并确定了最佳脱附条件.结果表明,微波辐照再生速度非常快.与传统热脱附不同,微波再生过程中脱附效率并不随碱浓度的增加而升高,微波辐照功率和辐照时间对脱附效果影响明显.树脂经多批次微波辐照,吸附性能和化学结构保持稳定.     

吸附邻氯酚的超高交联树脂微波辅助再生研究

以NDA-150超高交联树脂为吸附剂，邻氯酚为吸附质，氢氧化钠稀溶液为脱附剂，采用微波间歇辐照的方法，对吸附氯酚树脂的再生过程进行了研究。系统分析了微波功率、辐照时间、碱液浓度对脱附效果的影响，并确定了最佳脱附条件。结果表明，微波辐照再生速度非常快。与传统热脱附不同，微波再生过程中脱附效率并不随碱浓度的增加而升高，微波辐照功率和辐照时间对脱附效果影响明显。树脂经多批次微波辐照，吸附性能和化学结构保持稳定。     

吸附树脂组合工艺对微污染水的净化处理效果研究

利用江苏省盐城市串场河水作为源水,在常规处理工艺对源水进行前处理的基础上,结合树脂吸附处理工艺探讨了新型吸附树脂对水源水的处理效果和树脂吸附剂的再生效果.结果表明,新型吸附树脂按照ZH-02、ZH-03和ZH-00的顺序进行组合,对经沉淀砂滤预处理后的饮用水源水中微污染有机化合物具有较好的去除效果,处理2 000 BV后需对树脂进行再生,用2～2.5 BV的醇碱在常温下脱附,元素分析结果表明脱附效果较好,对水源水进行深度处理的原料成本大约为3.9元/t.     

树脂吸附法处理邻甲苯胺生产废水的研究

在最佳工艺条件下,采用NDA-804树脂对邻甲苯胺生产废水进行吸附-脱附实验。原废水经吸附处理后,邻甲苯胺去除率和CODcr去除率均大于99％．树脂脱附率接近100％。高浓度脱附液可以回收邻甲苯胺,达到了废水治理与资源化的效果。     

微波加热脱附回收Y分子筛吸附的酮类有机分子

微波再生技术被广泛认为是一种高效节能的绿色再生技术。采用3种不同Si/Al比的分子筛Na Y(Si/Al=3.8)、USY-1(Si/Al=4.1)、USY-2(Si/Al=7.6)作为吸附剂,3种分子结构不同的酮类物质环己酮、丁酮、丙酮作为吸附质,解决目前吸附酮类物质难再生的问题,开发一种新型有效可行的分子筛-酮类物质微波加热再生技术。通过实验结果分析,微波法对酮类有机物具有较高的脱附速率,可在较短的十几分钟内快速完成脱附,脱附率可达90%以上,残留量较少;Y分子筛表面无明显缩聚反应中毒现象;且经多次吸附/脱附循环再生后晶相结构保持稳定,可多次循环使用;脱附后有机物可直接液态回收再利用。     

盐酸脱附Pb(Ⅱ)负载氨基膦酸树脂的基本性能

氨基膦酸树脂是一种常用的广谱性重金属螯合树脂,对水中的Pb(Ⅱ)具有很好的选择性分离去除能力,但吸附Pb(Ⅱ)后的树脂再生较为困难。系统研究了盐酸脱附Pb(Ⅱ)-负载氨基膦酸树脂D860的基本性能,优化了基本脱附参数。实验表明,采用盐酸作为脱附剂具有较为良好的脱附效果,10%吸附量树脂脱附反应平衡较快仅需10 min,脱附本身受Pb(Ⅱ)在盐酸溶液中的溶解度影响显著。脱附流速从1 BV/h升高到5 BV/h,脱附效果受到的影响很小。升高温度可以提高PbCl2溶解度,进而提高脱附效率。固定床脱附采用1.0 mol/L盐酸,在1 BV/h和303 K条件下,仅需7 BV脱附剂即可实现较高的脱附效率。     

D201树脂的SO_4~(2-)吸附及脱附性能

采用离子交换树脂吸附去除炼化废水中的SO_4~(2-),以静态吸附法对比凝胶型树脂和大孔型树脂的性能,并进一步探究最优树脂的SO_4~(2-)吸附和脱附再生性能。结果表明,大孔型树脂较凝胶型树脂在复杂水质情况下性能更稳定,最优树脂为D201树脂,有较稳定的饱和吸附容量和较好的吸附脱附性能。     

树脂吸附法处理硫化促进剂CA生产废水的研究

采用特种吸附树脂处理促进剂CA生产废水 ,系统地研究了废水的pH值、吸附温度及吸附流量等因素对树脂吸附性能的影响 ,以及以稀硫酸为脱附剂 ,其配比、流量、温度等对树脂脱附性能的影响。实验结果表明 ,特种吸附树脂对该废水具有良好的吸附 脱附效果 ,废水经吸附处理后 ,CODCr浓度由 2 0 0 0 0mg/L左右降至 30 0mg/L以下 ,CODCr去除率达98%以上。该工艺简单 ,运行稳定 ,操作简便 ,可望实现工业化。     

树脂吸附法处理氯霉素中间体DL-氨基物合成废水

研究了树脂吸附法处理氯霉素生产中产生的DL 1 对硝基苯基 2 氨基 1 ,3 丙二醇 (DL 氨基物 )碱解废水的工艺。结果表明 ,NG 1 0 0超高交联吸附树脂对废水中DL 氨基物具有较好的吸附性能。在试验条件下 ,废水CODCr为 72 0 0mg/L ,DL 氨基物含量为 2 86 5mg/L ,批处理 1 7BV时 ,平均出水CODCr降至 89 3mg/L ,CODCr去除率 >98% ;出水中DL 氨基物未检出 ,去除率近 1 0 0 %。树脂经稀酸脱附处理后 ,再生性能良好 ,高浓脱附液可直接回用于氯霉素生产酸性水解工艺中 ,使回收物得到有效利用     

树脂吸附法处理硫化促进剂CA生产废水的研究

采用特种吸附树脂处理促进剂CA生产废水，系统地研究了废水的pH值、吸附温度及吸附流量等因素对树脂吸附性能的影响，以及以稀硫酸为脱附剂，其配比、流量、温度等对树脂脱附性能的影响。实验结果表明，特种吸附树脂对该废水具有良好的吸附，脱附效果，废水经吸附处理后，CODCr浓度由20000mg／L左右降至300mg／L以下，CODCr去除率达98％以上。该工艺简单，运行稳定，操作简便，可望实现工业化。     

微波解吸柠檬酸盐溶液中SO2实验研究

结合微波具有的热效应、非热效应特性,利用经改装的微波反应装置,研究了微波场下柠檬酸浓度、微波作用时间、微波功率、SO2初始浓度和搅拌速率对解吸柠檬酸盐溶液中SO2的影响,得出了影响SO2解吸率的基本规律和最佳解吸条件,并进行了分析.     

微波解吸柠檬酸盐溶液中SO2实验研究

结合微波具有的热效应、非热效应特性，利用经改装的微波反应装置，研究了微波场下柠檬酸浓度、微波作用时间、微波功率、SO2初始浓度和搅拌速率对解吸柠檬酸盐溶液中SO2的影响，得出了影响SO2解吸率的基本规律和最佳解吸条件，并进行了分析。     

弱碱性树脂吸附-解吸苦味酸

考察了水中苦味酸在弱碱性离子交换树脂D301R上的吸附与解吸。研究了吸附热力学、动力学特性及吸附机理。结果表明,树脂在pH=2.7～10.2时,吸附能力最好。等温平衡吸附遵循Freundlich模型。吸附过程为吸热、熵增的自发过程。吸附动力学符合Lagergren准二级速率方程,颗粒内扩散为吸附速率的主要控制步骤,吸附速率常数为7.23×10-5～1.20×10-4g/(mg.min),吸附活化能为19.4 kJ/mol。树脂上吸附的苦味酸可用HNO3+丙酮混合液定量洗脱,洗脱率达99%。静态吸附和脱附的比较结果证实了吸附过程中存在不可逆化学吸附。树脂对苦味酸的吸附主要是通过静电吸附、酸碱络合吸附、氢键吸附等协同作用来完成的。     

Kinetic characterizing of soil trace metal availability using Soil/EDTA/Chelex mixture

The kinetic aspects are not usually tackled when mimicking the soil trace metal mobilization. In this work, a simple procedure is developed for measuring the kinetics of Pb, Cu and Cd transfer from the soil solid phase towards a resin sink. A ternary system of Soil/EDTA/Chelex was employed for mimicking the metal transfer from two agricultural soil samples into the Chelex. Two different kinetic regimes (P₁ and P₂) were observed. The kinetic profile of Pb was distinctly different from those of Cd and Cu. Basing on kinetic principles, two kinetic models were proposed for estimating the apparent rate constants of leaching and removal processes in, respectively, two binary mixtures of soil/EDTA and EDTA extracts/Chelex. Contrary to Pb, solid phase pools of Cd and Cu exchanged with the solution on short time scales. The kinetic rate of desorption occurred in following order: Pb < Cu ? Cd. Comparing the kinetics of binary systems, the desorption process was hypothesized to control the metal transfer. The parameters related to the desorption process were extended to the kinetic regimes of Soil/EDTA/Chelex and revealed that the soil to Chelex transfer of Pb is under kinetics control whereas the bulk concentration (affected by the size of particulate reservoir) is likely to control the Cd transfer. Cu presents an intermediate case.     

The distribution, solid-phase speciation, and desorption/dissolution of As in waste iron-based drinking water treatment residuals

Arsenic concentrations and solid-phase speciation were assessed as a function of depth through Fe-media beds for two commercially available products (Granular Ferric Hydroxide-GFH and Bayoxide E33-E33) from pilot-scale water treatment field tests. These results were compared with data from solution (de-ionized water-DI-H2O) concentrations of As equilibrated with Fe-media in an anoxic environment at 4 degrees C. The materials had a high capacity for As (GFH media 9620 mg kg(-1) As, E33 Media 5246 mg kg(-1)). Arsenic concentrations decreased with bed depth. For E33, X-ray absorption near-edge spectroscopy results showed that As(V) was the dominant solid-phase species. For GFH, As(III) was detected and the proportion (relative to As(V)) of As(III) increased with bed depth. Arsenic concentrations in DI-H2O equilibrated with the media were low (35 microg l(-1)) over a period of 50 d. Arsenic concentrations in the equilibrated solutions also decreased with depth. Results from tests on soluble As speciation show that As in solution is in the form of As(V). Kinetic desorption experiments carried out at different pH values (3, 5, 7, 8, and 9) show that the media exhibit some acid/base neutralization capacity and tend to bind As sufficiently. Concentrations of As in the pH desorption experiments were in the same order of magnitude as the toxicity characteristic leaching procedure extractions (tens of microgl(-1)) except at low pH values. For the GFH media tested at a pH of three, As increases in solution and is mainly associated with colloidal (operationally defined as between 0.1 and 1.0 microm) iron.     

Leaching kinetics of water soluble organic carbon (WSOC) from upland soil.

The kinetics of the leaching process of Water Soluble Organic Carbon (WSOC) from an upland soil were studied in a column leaching experiment. The pattern of the leaching curve indicated multiphasic release kinetics. A conceptual model was proposed to divide capillary and gravitational pores. The translocation of organic carbon in soil during leaching occurs in four sequential steps. 1) degradation of insoluble organic carbon to form WSOC; 2) desorption into capillary pore water; 3) diffusion towards gravitation pore water; and 4) leaching by convection flow. The overall kinetics of the leaching process can be depicted using an equation with three additive terms for degradation, desorption/diffusion, and convection, respectively.     

Microwave pretreatment for enhancement of phosphorus release from dairy manure

Both the advanced oxidation process (AOP) using a combination of hydrogen peroxide addition and microwave heating (H2O2/microwave), and the microwave heating process were used for solubilization of phosphorus from liquid dairy manure. About 80% of total phosphate was released into the solution at a microwave heating time of 5 min at 170 degrees C. With an addition of H2O2, more than 81% of total phosphate could be released over a reaction period of 49 h at ambient temperature. The AOP process could achieve up to 85% of total phosphate release at 120 degrees C. The results indicated that both the microwave, and the AOP processes could effectively release phosphate from liquid dairy manure. These processes could serve as pretreatments for phosphorus recovery from animal wastes, and could be combined with the struvite crystallization process to provide a new approach in treating animal wastes.     

旋转填料床/柠檬酸盐法吸收-解吸SO2

提出采用旋转填料床结合柠檬酸盐法脱除烟气中SO2的方法,考察了旋转填料床转子转速、液气比、初始柠檬酸根浓度和初始pH值等因素对脱硫效率的影响。结果表明,采用超重力法超重机转子转速为1 000 r/min、液气比为7L/m3、初始柠檬酸根浓度为1.5 mol/L、吸收液的初始pH值为5.0,脱硫效率稳定在99%左右。研究了水蒸气汽提法解吸SO2时初始柠檬酸根浓度、初始pH值、SO2浓度、富液流量和水蒸气流量对解吸效率的影响,得出了影响SO2解吸率的基本规律,并进行了分析。通过实验证明该方法在技术上是可行的,具有良好的应用前景。     

Competitive adsorption characteristics of Co2+, Ni2+, and Cr3+ by IRN-77 cation exchange resin in synthesized wastewater

Adsorption properties of Co2+, Ni2+, and Cr3+ on an Amberlite IRN-77 cation exchange resin were investigated in batch systems. Levels of adsorption rapidly approached an equilibrium state within 1 h. The adsorption characteristics of each metal onto the resin were accurately represented by Langmuir isotherms. Co2+ and Ni2+, which have an equivalent electrovalence, displayed similar levels of adsorption onto the resin when they coexisted in the solution. However, when Cr3+ was added to the solution it competitively replaced Co2+ and Ni2+ ions that had been previously adsorbed onto the resin, resulting in the desorption of these metals into the solution. The result was likely due to a higher adsorption affinity of Cr3+ relative to Co2+ and Ni2+. This implies that interactively competitive adsorption of multi-cations onto the resin should be thoroughly considered when contemplating the efficient operation of an ion exchange process in the treatment of industrial wastewater.     

Remediation of heavy metal polluted sediment by suspension and solid-bed leaching: estimate of metal removal efficiency

Remediation of heavy metal polluted sediment by extracting the metals with sulfuric acid can be performed as follows: abiotic suspension leaching, microbial suspension leaching, abiotic solid-bed leaching, and microbial solid-bed leaching. Abiotic leaching means that the acid is directly added, while microbial leaching means that the acid is generated from sulfur by microbes (bioleaching). These four principles were compared to each other with special emphasis on the effectiveness of metal solubilization and metal removal by subsequent washing. Abiotic suspension leaching was fastest, but suspending the solids exhibits some disadvantages (low solid content, costly reactors, permanent input of energy, high water consumption, special equipment required for solid separation, large amounts of waste water, sediment properties hinder reuse), which prevent suspension leaching in practice. Abiotic solid-bed leaching implies the supply of acid by percolating water which proceeds slowly due to a limited bed permeability. Microbial solid-bed leaching means the generation of acid within the bed and has been proven to be the only principle applicable to practice. Metal removal from leached sediment requires washing with water. Washing of solid beds was much more effective than washing of suspended sediment. The kinetics of metal removal from solid beds 0.3, 0.6 or 1.2m in height were similar; when using a percolation flow of 20lm(-2)h(-1), the removal of 98% of the mobile metals lasted 57-61h and required 8.5, 4.2 or 2.3lkg(-1) water. This means, the higher the solid bed, the lower the sediment-mass-specific demand for time and water.