粉煤灰源C-S-H吸附U(Ⅵ)性能及机理

以粉煤灰铝回收过程的脱硅液为原料,通过控制钙硅摩尔比的常规沉淀法制备得到大比表面积介孔C-S-H（401 m²·g^-1）,系统研究了初始浓度、投加量、pH和离子强度对C-S-H吸附U（Ⅵ）过程的影响,以及吸附的热动力学特征,并评价了C-S-H去除实际含铀废水中毒性金属的性能。结果表明,通过控制合成条件实现了低品质硅钙渣向高附加值吸附材料的转变。0.75 g·L^-1 C-S-H在pH 2仍具有较高的平衡吸附容量（q_e=67.9 mg·g^-1）,在富含CO₃^2-的碱性溶液中UO₂（H₂O）₅²⁺转变为UO₂（CO₃）₃^4-不利于带负电的C-S-H表面吸附U（Ⅵ）。当C-S-H投加量升高至2～5 g·L^-1,材料对U（Ⅵ）的吸附去除效率即能维持在相对较高水平（C[U（Ⅵ）]_initial=500 mg·L^-1,去除率88.3%～93.5%）,吸附可在数小时内达到平衡,符合拟二级动力学模型和两阶段Weber-Morris方程模型,吸附等温线符合Langmuir模型,吸附机理主要为离子交换（84.6%）和表面络合。材料对含铀废水中的U、Zn、Hg、Mn和Cd均表现出良好的吸附去除性能,因而C-S-H可成为在废水毒性金属去除方面极具应用前景的材料。     

污水处理厂污泥制备生物炭及应用的研究进展

以污泥为原料制备生物炭是实现污泥资源化利用的途径之一,具有成本低、方法简单等优点。为了推动污泥制备生物炭技术的发展和应用,本文从制备方法、影响因素和应用领域等方面总结和归纳了污水处理厂污泥制备生物炭的研究现状,阐述了污泥生物炭不同制备方法及其优缺点,详细分析了不同影响因素对污泥生物炭产率、比表面积、孔径大小和孔径分布等特点的影响,总结了污泥生物炭在环境和农业领域的应用情况,提出了目前污泥制备生物炭技术存在的生物炭产率低、重金属易析出和生产批次差异等问题,并指出了今后的发展方向。     

MIEX和PAC对微污染水源水的水质净化效果比较

研究了MIEX和PAC两种水处理吸附剂对微污染水源水的水质净化性能。实验分别考察了MIEX和PAC对DOC和UV₂₅₄的去除效率,并通过凝胶渗透色谱和三维荧光光谱分析,研究了MIEX和PAC对不同相对分子质量区间以及不同种类有机物的去除规律。在正常的吸附剂投加量下(MIEX 5~8 ml·L^-1,PAC 30~50 mg·L^-1),MIEX对DOC和UV₂₅₄的平均去除率比PAC高23%和20%。但随着吸附剂投加量的增加,两者去除效率差别逐渐减小,MIEX对DOC和UV₂₅₄的最大去除率仅比PAC高6%~8%。与PAC相比,MIEX去除的有机物相对分子质量分布范围更广,特别是对中等分子量(5000~50000)有机物,其去效率明显高于PAC。MIEX对腐殖酸和富里酸类有机物的去除率略高于PAC,而对蛋白质类有机物的去除率则远高于PAC。动力学分析表明,MIEX和PAC对DOC的吸附去除过程符合准二级动力学,MIEX对有机物的吸附速率是PAC的40倍左右。     

Quantification of “delivered” H2 by a volumetric method to test H2 storage materials

We set up and validated a volumetric method to quantify the amount of hydrogen “delivered” after saturation of a solid material as adsorber at different pressures (up to 100 kg_f/cm²) and temperatures (down to 77 K). This is the practically most relevant datum to quantify the effectiveness of an adsorbent for the present application. A complementary dynamic method has been also developed to take into account the reversibility of adsorption and to assess in at least a semi-quantitative way the strength of interaction between H₂ and the adsorbent. The method has been applied to compare the hydrogen storage capacity of some significant different carbon-based materials (two active carbons and one graphite), as supplied or after thermal treatments under oxidising or reducing conditions. The best results, ca. 7 wt% H₂ “delivered”, were achieved after saturation at 77 K, 20 kg_f/cm² with an active carbon with ca. 3000 m²/g of apparent specific surface area. The thermal treatments, almost always inducing a drop in surface area, showed effective only for saturation at 273 K, in particular the oxidising procedure. This was correlated to the formation of surface oxidised species, likely carboxylic groups, which improved the interaction strength between H₂ and the adsorbent.     

金属氧化物掺杂对钙基吸附剂吸附CO_2性能的影响

化石燃料火电厂排放的CO2约占全球CO2总排放量的1/3,采用化学吸附法直接脱除高温烟气中的CO2既可以减少系统的能量损失又可以保护环境。文中采用机械混合法制备金属氧化物掺杂的钙基吸附剂,并以静吸附量和CO2吸附率为评价指标,气相色谱为检测手段,在自制吸附剂评价装置上,研究不同金属氧化物的掺杂对钙基吸附剂吸附性性能的影响。实验表明,掺杂金属氧化物对钙基吸附剂的吸附性能有一定影响,其中质量分数为1%的Li2CO3掺杂的钙基吸附剂的静吸附容量与钙基吸附剂的理论吸附量比较接近,并且优于其他金属氧化物掺杂的钙基吸附剂。     

Histidine Containing Macroporous Affinity Cryogels for Immunoglobulin G Purification

A supermacroporous cryogel was prepared to obtain an efficient and cost effective purification of IgG from human plasma. N-methacryloyl-(L)-histidine methyl ester (MAH) was chosen as the pseudospecific ligand and/or comonomer. Poly(hydroxyethyl methacrylate-N-methacryloyl-(L)-histidine methylester) [PHEMAH] cryogel was produced by free radical polymerization initiated by N,N,N′,N′-tetramethylene diamine (TEMED) and ammonium persulfate (APS) pair in an ice bath. PHEMAH cryogel had a specific surface area of 38.6 m²/g. PHEMAH cryogel was characterized by swelling studies, scanning electron microscopy and elemental analysis. PHEMAH cryogel containing 113.7 µmol MAH/g was used in the purification of IgG from human plasma. Compared with the poly(hydroxyethyl methacrylate) (PHEMA) cryogel (0.4 mg/g), the IgG adsorption capacity of the PHEMAH cryogel (24.7 mg/g) was improved significantly due to the MAH incorporation into the polymeric matrix. The maximum amount of IgG adsorption from aqueous solution in phosphate buffer was observed at pH 7.4. The IgG adsorption amount from human plasma was 97.3 mg/g with a purity of 94.6%. It was observed that IgG could be repeatedly adsorbed and eluted with PHEMAH cryogel without significant loss in the adsorption capacity.     

Vacuum Pressure Swing Adsorption to Produce Polymer-Grade Propylene

We have evaluated the Vacuum Pressure Swing Adsorption (VPSA) technology to separate propane–propylene streams to produce polymer-grade propylene. Zeolite 4A is used as kinetic adsorbent since propylene diffuses much faster than propane. A single VPSA process is able to produce propylene with purity higher than 99.6%. However, propylene recovery is only 67% and therefore a second stage is used. In this VPSA unit, zeolite 4A with smaller crystal radius is employed to reduce kinetic limitations. The second VPSA (tail unit) produces purified propane and recovers propylene that is recycled to the feed of the first VPSA (front unit). Linking these two VPSA units allows us to produce polymer-grade propylene (PGP) recovering 95.9% of the propylene. Comparing the performance of this process with distillation, there is a significant decrease in the separation volume. However, further efforts are necessary to reduce the power consumption of VPSA which is still slightly higher than for distillation.     

仙人掌黄酮类化合物的超声波提取和纯化

采用超声波萃取法,研究仙人掌黄酮类化合物的提取工艺。通过试验确定了超声波功率、乙醇体积分数及辐射时间的最佳参数。选用AB8、DM130、WXI大孔树脂对仙人掌黄酮提取液进行分离纯化。结果表明,乙醇体积分数65%、功率550W、辐射时间12s提取效果最佳,AB-8型树脂分离提纯效果最好,吸附率为8481%,解吸率达8842%。     

柴油络合脱氮技术的研究进展

柴油络合脱氮技术相对于其他非加氢脱氮技术,具有反应条件温和、工艺流程简单、脱氮率及油品收率高等特点。综述了近年来国内外柴油络合脱氮的研究进展,重点介绍了π-络合吸附脱氮、离子液体脱氮及络合萃取脱氮技术的原理、研究现状及应用进展,指出了不同络合脱氮技术的特点、所存在的问题及研究方向。     

Development of adsorbents from used tire rubber: Their use in the adsorption of organic and inorganic solutes in aqueous solution

Using used tire rubber (UTR), carbonaceous adsorbents (CAs) were prepared by chemical treatment of the material with HCl, HNO₃ and NaOH aqueous solutions and by heat treatment at 900 °C for 2 h in N₂ atmosphere (H900). UTR and the UTR-derived products were first characterized in terms of texture by N₂ adsorption at − 196 °C and of oxygen surface groups by FT-IR spectroscopy and pH of the point of zero charge (pH_pzc). Then, the products were tested as adsorbents of phenol, p-aminophenol, p-nitrophenol, and p-chlorophenol and of chromium, cadmium, mercury and lead in aqueous solution. The development of porosity is very poor in UTR and in the chemically treated products. H900 is the only CA with a better developed porosity, mainly in the regions of meso and macropores. pH_pzc is close to 7.0 for most of the CAs. As an exception to the rule, pH_pzc is 8.4 for H900. For this CA, the adsorption of all the adsorptives is greater. Usually, adsorption kinetics are fast. This is so in particular for p-nitrophenol and p-chlorophenol, on the one side, and for mercury and lead, on the other side. Adsorption is much higher for mercury and lead than for the remaining adsorptives.