Treatment of desizing wastewater from the textile industry by wet air oxidation

This paper describes the application of wet air oxidation to the treatment of desizing wastewater from two textile companies. A two-liter high temperature, high pressure autoclave reactor was used in the study. The range of operating temperatures examined was between 150 and 290℃, and the partial pressure of oxygen ranged from 0. 375 to 2.25 MPa. Variations in pH,CODCr and TOD content were monitored during each experiment and used to assess the extent of conversion of the process. The effects of temperature, pressure and reaction time were explored extensively. More than 90 ％ CODCr reduction and 80 ％ TOC removal have been obtained. The results have also been demonstrated that WAO is a suitable pre-treatment methods due to improvement of the BOD5/CODCr ratio of desizing wastewater. The reaction kinetics of wet air oxidation of desizing wastewater has been proved to be two steps, a fast reaction followed by a slow reaction stage.     

Catalytic wet air oxidation for the treatment of emulsifying wastewater

The wet air oxidation (WAO) and catalytic WAO(CWAO) of the high strength emulsifying wastewater containing nonionic surfactants have been investigated in terms of COD and TOC removal. The WAO and homogeneous CWAO processes were carried out at the temperature from 433 K to 513 K, with initial oxygen pressure 1.2 MPa. It was found that homogeneous catalyst copper(Cu(NO3)2) had an fairly good catalytic activity for the WAO process, and the oxidation was catalyzed when the temperature was higher than 473K. Moreover, several heterogeneous catalysts were proved to be effective for the WAO process. At the temperature 473 K, after 2h reaction, WAO process could achieve about 75% COD removal and 66% TOC removal, while catalysts Cu/Al2O3 and Mn-Ce/Al2O3 elevated the COD removal up to 86%-89% and that of TOC up to 82%. However, complete elimination of COD and TOC was proved to be difficult even the best non-noble catalyst was used. Therefore, the effluent from WAO or CWAO process need to be further disposed. The bioassay proved that the effluent from WAO process was amenable to the biochemical method.     

Homogeneous catalytic wet air oxidation for the treatment oftextile wastewaters

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Pretreatment of apramycin wastewater by catalytic wet air oxidation

IntroductionPharmaceuticalindustrybecomesmoreandmoreimportantallovertheworld .InChina ,therearemorethan30 0plantsmanufacturingantibioticproduction .However,theplantsoftenproducealotofwastewatercontaininghighconcentrated,colortoxicorganiccompounds.Ifthepol…     

湿式氧化处理高浓度难降解有机废水研究

在2L高压间歇反应釜中,系统地研究了高浓度难降解乳化废水的影响因素和动力学特征.结果表明:湿式氧化温度以220℃为宜;TOC去除率为73 2%～82 1%;供氧量以1 0～1 25倍理论需氧量为宜;在较宽浓度范围内仍具有良好的处理效果;并建立基于TOC指数型经验模型.     

Mn/Ce复合催化剂湿式氧化降解高浓度吡虫啉农药废水的研究

通过共沉淀法制备了用于湿式氧化吡虫啉农药废水的Mn/Ce复合催化剂,利用BET比表面积测定和XRD对催化剂进行了表征,研究了焙烧温度对Mn/Ce催化剂活性及稳定性的影响,探讨了湿式催化氧化吡虫啉农药废水的适宜反应温度和氧分压.结果表明,Mn/Ce催化剂晶粒细小,晶粒尺寸小于15nm;适当降低焙烧温度,对减小催化剂晶粒、增加比表面积、提高活性有利,但会使金属溶出量增大、稳定性下降;提高反应温度,湿式催化氧化反应速率加快,而氧分压大于1.6MPa后,反应速率不受氧分压影响;使用该催化剂,在温度190℃、氧分压1.6MPa、进水pH为6.21的条件下经120min处理,COD去除率达93.1%;Mn/Ce复合催化剂对湿式氧化吡虫啉农药废水显示较好的活性和稳定性.     

Use of catalytic wet air oxidation (CWAO) for pretreatment of high-salinity high-organic wastewater

Catalytic wet air oxidation (CWAO) coupled desalination technology provides a possibility for the effective and economic degradation of high salinity and high organic wastewater. Chloride widely occurs in natural and wastewaters, and its high content jeopardizes the efficacy of Advanced oxidation process (AOPs). Thus, a novel chlorine ion resistant catalyst B-site Ru doped LaFe_1-xRu_xO_3-δ in CWAO treatment of chlorine ion wastewater was examined. Especially, LaFe_0.85Ru_0.15O_3-δ was 45.5% better than that of the 6%RuO₂@TiO₂ (commercial carrier) on total organic carbon (TOC) removal. Also, doped catalysts LaFe_1-xRu_xO_3-δ showed better activity than supported catalysts RuO₂@LaFeO₃ and RuO₂@TiO₂ with the same Ru content. Moreover, LaFe_0.85Ru_0.15O_3-δ has novel chlorine ion resistance no matter the concentration of Cl⁻ and no Ru dissolves after the reaction. X-ray diffraction (XRD) refinement, X-ray photoelectron spectroscopy (XPS), transmission electron microscope (TEM), and X-ray absorption fine structure (XAFS) measurements verified the structure of LaFe_0.85Ru_0.15O_3-δ. Kinetic data and density functional theory (DFT) proved that Fe is the site of acetic acid oxidation and adsorption of chloride ions. The existence of Fe in LaFe_0.85Ru_0.15O_3-δ could adsorb chlorine ion (catalytic activity inhibitor), which can protect the Ru site and other active oxygen species to exert catalytic activity. This work is essential for the development of chloride-resistant catalyst in CWAO.

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芬顿试剂和湿式过氧化氢氧化法处理乳化液废水研究

研究了常温下芬顿试剂氧化乳化液废水的特性,当进水COD为50540mg·L-1,常温下芬顿试剂氧化的最佳条件为H2O2/COD的质量浓度比为2.0,Fe2 /COD的质量浓度比为0.075时,其COD去除约91%;常温下芬顿试剂氧化乳化液废水时存在明显的诱导期,用表观一级模型分别解释了快速和慢速的反应过程.另外,进一步研究了以H2O2替代部分或全部空气即湿式过氧化氢氧化工艺的氧化能力,湿式双氧水氧化可显著降低亚铁投量(Fe2 投量为50mg·L-1),150℃时COD去除率为82.4%;以少量的双氧水(H2O2/COD=0.05)为引发剂,在120℃下COD去除率达52.0%,催化效果显著.     

Kinetics study on catalytic wet air oxidation of phenol by several metal oxide catalysts

Four metal oxide catalysts composed of copper (Cu), stannum (Sn), copper-stannum (Cu-Sn) and copper-cerium(Cu-Ce) respectively were prepared by the co-impregnation method, and γ-alumina(γ-Al2O3 ) is selected as support. A first-order kinetics model was established to study the catalytic wet air oxidation of phenol at different temperature when these catalysts were used. The model simulations are good agreement with present experimental data. Results showed that the reaction rate constants can be significantly increased when catalysts were used, and the catalyst of 6% Cu-10% Ce/γ-Al2 O3 showed the best catalytic activity. This is consistent witht he result of catalytic wet air oxidation of phenol and the COD removal can be arrived at 98.2% at temperature 210℃, oxygen partial pressure 3 MPa and reaction time 30 rain. The activation energies of each reaction with different catalysts are nearly equal, which is found to be about 42 kJ/mol and the reaction in this study is proved to be kinetics control.     

Air pollutant emission potentials of cotton textile manufacturing industry

Cotton textile manufacturing operations cause air pollution. Air pollutants are generated by fossil fuel fired combustors due to their flues and/or a variety of chemicals in use for production. Excessive use of chemicals can be stopped or minimized by replacing them or by optimizing the production processes. Energy and water conservation are important goals in textile workplaces as well. There is substantial research and development to minimize pollution potentials of textile operations. In this paper air polluting potentials of cotton textile manufacturing operations are discussed and some quantitative examples are given for evaluating the risks to the environment. Studied impacts to environment cover direct discharges into the ambient air as well as the workplace atmosphere. Further studies are recommended for minimizing the impacts to the local and global air quality due to cotton textile production facilities.     

CeO2-ZrO2固溶体在催化湿式空气氧化苯酚废水中的作用

采用共沉淀法制备了CuO/ZnO/Ce O_2、CuO/ZnO/ZrO_2和CuO/ZnO/Ce O_2-Zr O_2催化湿式空气氧化苯酚废水催化剂,并采用N_2吸附-脱附、X射线衍射(XRD)、X射线光电子能谱(XPS)、程序升温还原(TPR)、N_2O滴定和电感耦合等离子体原子发射光谱等手段对催化剂进行了表征.结果表明,CuO/ZnO/Ce O_2-Zr O_2催化剂表现出最佳的催化性能.在200℃、2 MPa空气、苯酚初始浓度500 mg·L~(-1)的条件下,COD去除率为96.5%.XRD表明Ce O_2-Zr O_2复合氧化物载体以Ce_xZr_(1-x)O_2固溶体形式存在,增加了催化材料的储放氧能力.XPS表明Ce~(3+)和Ce~(4+)在催化剂表面共同存在,协调了氧化还原过程.TPR表明催化剂的还原性对催化剂的氧化活性起到至关重要的影响.由于CuO/ZnO/Ce O_2-Zr O_2催化剂活性组分和载体间的强相互作用,处理后的水样未发现金属离子,进而有效的提高了催化剂的稳定性和避免了对水样的二次污染.     

Degradation of H-acid in aqueous solution by microwave assisted wet air oxidation using Ni-loaded GAC as catalyst

A novel process, microwave assisted catalytic wet air oxidation( MW-CWO), was applied for the degradation of H-acid( l-amino8-naphthol-3, 6-disulfonic acid) in aqueous solution, Ni-loaded granular activated carbon (GAC), prepared by immersion-calcination method, was used as catalyst. The results showed that the MW-CWO process was very effective for the degradation of H-acid in aqueous solution under atmospheric pressure with 87.4% TOC (total organic carbon) reduction in 20 min. Ni on GAC existed in the form of NiO as specified by XRD. Loss of Ni was significant in the initial stage, and then remained almost constant after 20 min reaction. BET surface area results showed that the surface property of GAC after MW-CWO process was superior to that of blank GAC.     

Wet air oxidation treatment of H acid wastewater

１ＩｎｔｒｏｄｕｃｔｉｏｎＨａｃｉｄｍｏｎｏｓｏｄｉｕｍｓａｌｔ（４ａｍｉｎｏ５ｈｙｄｒｏｘｙ２，７Ｎａｐｈｔｈａｌｅｎｅｄｉｓｃｕｌｆｏｎｉｃａｃｉｄｍｏｎｏｓｏｄｉｕｍｓａｌｔ，ｈｅｒｅｉｎａｆｔｅｒｒｅｆｅｒｅｅｄｔｏａｓ“Ｈａ...     

催化湿式氧化法处理有机废水的催化剂研究

催化湿式氧化法是处理高浓度、有毒有害、难降解有机废水的一种有效手段.本文分析总结了过渡金属、贵金属和稀土金属等作为均相催化剂与非均相催化剂,采用催化湿式氧化法处理有机废水的性能,特别是比较了它们处理多种有机废水时对COD的去除效率和载体的使用情况.从分析中可以看出,氧化铝是非常好的载体,多组分复合催化剂比单组分催化剂具有更好的催化性能,以Cu、Mn、Ce为主要活性组分的复合催化剂具有很高的催化活性,并且应用范围广.最后探讨了催化剂的反应机理和发展前景.     

湿式氧化-磷酸盐固定化组合工艺处理磷霉素制药废水及其资源化

采用湿式氧化-磷酸盐固定化组合工艺处理COD为72750mg·L-1、总有机磷(TOP)为8225 mg·L-1的磷霉素制药废水并对废水中磷进行资源化回收.首先,采用湿式氧化工艺,利用分子氧作为氧化剂,将废水中有机磷转化成无机磷酸盐,分别考察了反应温度、氧分压和废水初始pH值对湿式氧化处理效果的影响,结果显示：在反应温...     

H2O2湿式氧化处理含酸性红B染料模拟废水的研究

用H2 O2 作氧化剂 ,在连续式的压力反应器内探索了WPO(过氧化氢湿式氧化法 )、CWPO(催化过氧化氢湿式氧化法 )氧化降解含酸性红B染料模拟废水的过程 ,分别考察温度、压力、氧化剂量及催化剂对反应过程与对象污染物降解的影响规律 .结果表明 ,与常规湿式氧化法相比 ,WPO能在较低的温度和压力下降解结构稳定的有机物 ,在 2 2 0℃、8min、0 1MPa时 ,含1 5 0 0mg·L-1 酸性红B染料模拟废水的COD和色度的去除率分别达到 6 0 5 0 %和 96 80 % .同时发现 ,通过升温和增加过氧化氢的投加量不能够使废水COD和色度的去除率进一步提高 ,故引入Cu2 作催化剂来实现CWPO过程 ,在 2 2 0℃、8min、0 1MPa条件下 ,CWPO对同一废水的COD和色度的去除率分别达到 82 5 0 %和 99 71 % .通过计算得出CWPO与WPO相比基于COD的表观活化能降低了 6 5 93 % .     

UNITANK+接触氧化工艺处理制皂废水

采用 U NITANK系统和生物接触氧化工艺处理主要污染物为油脂、甘油等的制皂工业废水。经过试验研究 ,工艺参数选择和运行处理效果分析 ,结果证明 ,采用该工艺处理制皂工业废水 ,三格池好氧 U NITANK系统的容积负荷为1.5 kg CODCr/m3· d时 ,COD去除率可达 80 % ,接触氧化池的 COD去除率亦在 80 %左右 ,处理效果稳定     

湿式空气氧化过程中氧气、二氧化碳和水蒸气分压的理论

介绍了亨利常数随温度、压力变化的经验公式,并采用湿式空气氧化（WAO） 工艺处理城市污水厂活性污泥,验证了湿式氧化过程中亨利常数经验估算公式,以期为湿式氧化工艺设计和运行实践提供依据．结果表明,在180 ℃时,氧气的初始分压为0.98MPa,氧气和二氧化碳的亨利常数分别为2.5778×10⁹、5.9894 ×10⁹N/mF²．     

Preparation of rare-earth metal complex oxide catalysts for catalytic wet air oxidation

Catalytic wet air oxidation (CWAO) is one of the most promising technologies for pollution abatement. Developing catalysts with high activity and stability is crucial for the application of the CWAO process. The Mn/Ce complex oxide catalysts for CWAO of high concentration phenol-containing wastewater were prepared by coprecipitation. The catalyst preparation conditions were optimized by using an orthogonal layout method and single-factor experimental analysis. The Mn/Ce serial catalysts were characterized by Brunauer-Emmett-Teller (BET) analysis and the metal cation leaching was measured by inductively coupled plasma torch-atomic emission spectrometry (ICP-AES). The results show that the catalysts have high catalytic activities even at a low temperature (80°C) and low oxygen partial pressure (0.5 MPa) in a batch reactor. The metallic ion leaching is comparatively low (Mn<6.577 mg/L and Ce<0.6910 mg/L, respectively) in the CWAO process. The phenol, COD_Cr, and TOC removal efficiencies in the solution exceed 98.5% using the optimal catalyst (named CSP). The new catalyst would have a promising application in CWAO treatment of high concentration organic wastewater. Translated from Techniques and Equipment for Environmental Pollution Control, 2005, 6(2): 40–44 [译自: 环境污染治理技术与设备]     

CeO2形貌结构对催化湿式空气氧化苯酚性能的影响

采用水热法、沉淀法和溶胶凝胶法制备了3种不同形貌的CeO₂催化材料,并将其用于湿式空气氧化苯酚水溶液过程中,探讨了CeO₂形貌结构对催化湿式氧化苯酚水溶液性能的影响.采用扫描电子显微镜（SEM）、透射电子显微镜（TEM）、X射线衍射（XRD）、程序升温还原（TPR）等手段对CeO₂催化材料进行了表征.结果表明,水热法制备的CeO₂催化材料表现出较好催化性能,主要原因是水热法合成的CeO₂呈现交错的纳米棒状结构,主要暴露（220）晶面,且沿着（220）晶向生长.在反应温度为200℃、空气压力为2MPa、苯酚初始浓度500mg/L的条件下,最终（240min）COD的去除率为95.5%.