沸石法工业污水氨氮治理技术研究

本文研究了斜发沸石法去除工业污水中氨氮的方法 ,通过沸石对NH+4 的全交换容量、吸附和洗脱工艺条件对去除氨氮效果影响的试验 ,确定了处理氨氮废水的工艺流程和适宜参数。结果表明 ,在废水浓度pH =7的条件下 ,沸石对铵的平均全交换容量达到 12 .96mg/g沸石 ,且交换容量随PH值的增大而降低 ;高速低温有利于吸附 ,低速高温有利于洗脱 ;处理后污水氨氮含量低于 5 0mg/L ,达到了国家排放标准。

沸石强化A/O生物脱氮工艺氨氮去除机理研究

沸石强化A/O生物脱氮实验研究表明,沸石对配水氨氮具有良好的吸附性能,其吸附特征可以通过Frend lich和Langmu ir吸附等温线表征,但对污水中氨氮的吸附较配水吸附要复杂。由于沸石能与微生物构成沸石-生物复合体,从而增加了系统的硝化细菌和反硝化细菌数量,改善了A段的反硝化作用和O段的硝化作用。吸附饱和的铵沸石在硝化细菌和电导率的协同作用下,经好氧曝气4.5 h,能再生69.8%。在A段,进水氨氮浓度较高,沸石吸附氨氮,提高污水碳氮比,促进生物反硝化;进入O段,在盐度和微生物的协同作用下,混合液氨氮浓度因为生物降解而逐渐降低,不断打破铵沸石的吸附-脱附平衡,铵沸石不断释放氨氮而得到充分的再生。

改性铵型沸石对脱硫废水中有机物处理的影响

铵型沸石分别进行微波磷、复配表面活性剂改性并处理脱硫废水中的有机物。利用正交法分别考察两沸石对有机物最佳处理条件,通过扫描电镜观测其表观形态及孔隙程度。通过加权、极差分析得出处理有机物影响因素的权重及主要影响因素,借助orign建立主要影响因素与有机物吸附率的关系。结果表明:两沸石对有机物最佳处理条件均为沸石投加量6 g、有机物浓度35 mol/L、吸附温度30℃、吸附时间5 h;此时,有机物吸附率分别为85%、86.18%。沸石投加量、吸附温度分别为微波磷、复配表面活性剂改性沸石处理有机物的主要影响因素。改性铵型沸石的研制为火力发电系统低污染化处理脱硫废水提供一种新型处理材料,并对有机物的去除提供参考。

改性沸石用于水的降氟实验研究

本文采用伊盟天然沸石作为吸附F-的滤料,用于水的降F-实验研究。实验结果表明:沸石的灼烧温度、沸石的粒度、是否改性对沸石降F-效果有一定影响。而且经测定改性的20-40目无灼烧沸石降F-效果最好。

海水提钾万吨级产业化项目启动

由河北长芦黄驿盐业集团采用天津河北工业大学斜法沸石法海水提钾技术建设的年产1．2万t硫酸钾工程和年产1万t硝酸钾工程，日前分别在天津和河北沧州立项，并已进行建设前期工作，预计今年底建成投入生产。

法库沸石对氨氮的吸附特性和阳离子交互过程

以0.9~2 mm和3.3~4 mm粒径沸石的天然法库沸石作为实验材料,开展了等温吸附实验、动力学实验和阳离子影响实验,探讨了天然沸石对氨氮(NH+4-N)的吸附特性及阳离子交互过程。结果表明,法库沸石对NH+4-N等温吸附线符合Langmuir和Freundlich吸附方程,最大吸附量为10.41 mg/g。吸附动力学过程符合准二级和颗粒内经扩散动力学方程,其吸附NH+4过程为物理吸附和化学吸附过程,并以化学吸附为主。对反应过程中各离子浓度监测发现,沸石中与NH+4发生离子交换的主要是Na+、Ca2+和K+,三者占离子交换总量的99%。共存阳离子在沸石吸附NH+4过程中,Ca2+和Mg2+对吸附过程影响最大,Na+影响最小。

科技信息

海水提取硝酸钾和卤水提溴新技术天津长芦海晶集团与河北工业大学等单位承担的'海水提取硝酸钾新技术研究及应用'以及与天津海水淡化所共同承担的'气态膜法和卤水提溴新技术研究'项目近日通过科技部专家组验收。硝酸钾项目建成了200吨/年全流程中试装置,完成并突破了沸石法海水钾高效富集、萃取结晶法分离硝酸钾和氨回收等关键技术,形成了完整的沸石法海水直接提取硝酸钾技术,为万吨级产业化示范项目的实施打下了良好的基础。

Mineral transition of desilication products precipitated in synthetic sodium aluminate solution under atmospheric pressure

The liquor concentration, mineral proportion, crystal parameters and micro morphology of various desilication products（DSPs） precipitated in silica-supersaturated sodium aluminate solution at 95 ℃ under different reaction conditions were systematically researched. The DSPs formed under atmospheric pressure comprise amorphous phase, zeolite A, zeolite and sodalite, and the DSPs concentration and crystallinity increase with the increase of initial silica concentration, initial molar ratio of caustic Na2O to Al2O3（αK） and desilication duration. Decreasing the initial silica concentration, initial αK and increasing the desilication duration can reduce the proportion of zeolite A. The zeolite and sodalite are the stable DSPs, while the precipitation of zeolite A occurs at a high silica-supersaturated state in sodium aluminate solution. The DSPs are precipitated in the form of agglomerates, but the morphologies of various DSPs are quite different. Both the molar ratios of Na2O to Al2O3 and SiO-2 to Al2O3 in DSPs increase with the increasing desilication duration, resulting in the increase of the cell volumes of various DSPs. The precipitation sequence of DSPs under atmospheric pressure is： amorphous phase→zeolite A→zeolite→sodalite.

Adsorption of Chromium （Ⅵ） from Aqueous Solution Using Zeolite/Chitosan Hybrid Composite

This study investigated the adsorption ability of ZCHC （zeolite/chitosan hybrid composite） as adsorbent for chromium （Cr（Ⅵ））, ZCHC was prepared with sol-gel method by mixing zeolite and chitosan. Adsorption experiment from aqueous solutions containing known amount of Cr（Ⅵ） using zeolite, chitosan and ZCHC was explored to evaluate the efficiency of ZCHC as adsorbent for Cr in a batch system. The amount of Cr（Ⅵ） adsorbed at different pH values, initial concentrations, adsorbent dosages, and contact times were determined by ICP-AES （inductively coupled plasma-atomic emission spectrometry） in order to determine the optimum conditions for Cr（Ⅵ） adsorption. Furthermore, the adsorption mechanism of Cr（Ⅵ） by zeolite, chitosan and ZCHC was investigated by applying Langmuir and Freundlich isotherm equations to the data obtained. In addition, the rates of adsorption were found to conform to pseudo-second order kinetics.

Preparation and antimicrobial ability of natural porous antibacterial materials

The liquid ion exchange method, solid salt melt method and dry-wet circulation method were used to prepare natural porous antimicrobial materials with natural minerals, such as zeolite, spilite, palygorskite and montmorillonite, respectively. Atomic absorption spectrum and X-ray diffraction analysis were carried out to investigate the effects of Ag^＋ , Cu^2＋ and Zn^2＋ on antimicrobial abilities of natural porous minerals, and the effect of preparation method on ion exchange capacity of antimicrobial material, respectively. The results show that for the ion exchange capacity, clay mineral is higher than fibrous mineral, i.e. both zeolite and montmorillonite are higher; the antimicrobial ability of material with Ag^＋ is the bests the exchange capacities of materials with Cu^2＋ or Zn^2＋ are all higher, but the antimicrobial ability of Cu^2＋ is better than that of Zn^2＋ .

Ship-in-bottle synthesis of NaY zeolite encapsulated Cosalen complex and its catalytic performance for cyclohexane oxidation

N, N＇-bis （salicylidene） ethylenediiminocobalt （Cosalen） was encapsulated into microporous NaY zeolite via the technique of ＂ship-in-bottle＂. The encapsulated complex （Cosalen-NaY） was characterized by Fourier-transform infrared spectrum, ultraviolet-visible spectrum, Brunaner-Emmett-Teller surface areas, X-ray diffraction, thermogravimetry-differential thermal analysis and scanning electron microscope. The reaction of cyclohexane oxidation using oxygen was chosen to investigate the catalytic performance of Cosalen-NaY, and the effects of oxygen pressure, temperature and reaction time were also studied. The results show that Cosalen complex is encapsulated into the supercage of the zeolite and the structure of NaY zeolite remains integrity and the thermal stability of Cosalen is greatly enhanced after encapsulation. Cosalen-NaY shows the better activity in the oxidation of cyclohexane without reductant and solvent. The conversion of cyclohexane is up to 13.4% at 150 ℃ for 3 h under oxygen pressure of 0.85 MPa, with the higher total selectivity to cyclohexanol, cyclohexanone, cyclohexyl hydroperoxide （CHHP） and acid （79.2%） than the neat complex （55.5%）. NaY zeolite cartier maybe contributes to the results. There is no obvious induction period to initiate the reaction; furthermore, the amount of CHHP among the products is small, which indicates that the Cosalen-NaY has the strong ability to accelerate the decomposition of CHHP. Recycling tests show that the hybrid material can be used repeatedly with a negligible loss of active sites.

Performances of lateral flow biological aerated filter in treating domestic wastewater

A new biological aerated filter?lateral flow biological aerated filter(LBAF) is developed. The effects of air/water ratio, hydraulic loading and the length of LBAF on pollutants removal efficiency are tested. The results show that under optimal technological conditions when hydraulic loading is 0.43 m3 m?2 h?1 and air/water ratio is 10:1, the average removal efficiencies of COD, SS, NH3-N, and TN reach 88.01%, 95.18%, 78.97% and 52.58%, respectively. An LBAF has a large pollutants handling capacity; is less liable to be blocked, and has a longer operation cycle in comparison with a traditional BAF.

Effect of the Alumosilicate Gels pH on Zeolite Phase Composition for the Co-crystallization of BEA/MOR Zeolites in Na2O-TEABr-Al2O3-SiO2-H2O System

This paper deals with the method of zeolites BEA （beta） and MOR （mordenite） synthesis and the co-crystallization method of zeolites BEA/MOR. Synthesized zeolites were studied based on the SEM （scanning electron microscopy）, XRD （x-ray diffraction） and chemical analysis. The porous structure of these zeolites was investigated by nitrogen low-temperature adsorption. It has been illustrated that regulation of the BEA/MOR co-crystalline zeolites phase composition is possible due to variations of the initial alumosilicate gels composition and hydrogen ions concentration. Zeolites containing the co-crystalline phases of BEA/MOR could to be attractive in the processes using the catalysts, which based on the pure phases BEA or MOR zeolites.

Green Process for Synthesis of Zeolite with MFI Structure

A clean and environmentally friendly new process for synthesis of zeolite with MFI structure was presented. This process through recycling of vented gas and mother liquor can reduce or avoid discharge of nitrogen-containing offgas and waste liquid without affecting the physical and chemical properties of synthetic zeolite, leading to green synthesis of zeolite. This process can help to cut corners on production cost to achieve the sustainable development.