水杨酸生产废水的治理与资源化

采用新型超高交联吸附树脂NDA 80 0吸附法处理水杨酸生产废水 ,试验结果表明 ,NDA 80 0超高交联吸附树脂对水杨酸生产废水有良好的处理效果。当进水CODCr值约 2 0 0 0 0mg/L ,苯酚和水杨酸含量分别为 6 0 0 0mg/L和 130 0mg/L左右时 ,经过NDA 80 0树脂一级吸附处理 ,出水的CODCr、苯酚等污染指标均可达到排放标准 ,同时实现了水杨酸生产废水中苯酚和水杨酸等化工资源的生产回用     

连续式离子分离系统（ISEP）在水杨酸生产废水处理中的应用

采用连续式离子分离系统（ISEP）处理水杨酸生产废水，结果表明，该系统对水杨酸生产废水有良好的处理效果。当进水CODCr为18000－20000mg/L时，经一步吸附处理，出水CODCr可实现达标排放，苯酚、水杨酸去除率接近100％，脱附液中高浓度苯酚、水杨酸等资源可有效回收利用。     

水杨酸生产废水的治理与资源化

采用新型超高交联吸附树脂NDA-800吸附法处理水杨酸生产废水，试验结果表明，NDA-800超高交联吸附树脂对水杨酸生产废水有良好的处理效果。当进水CODCr值约20000mg／L，苯酚和水杨酸含量分别为6000mg／L和1300mg／L左右时，经过NDA-800树脂一级吸附处理，出水的CODCr、苯酚等污染指标均可达到排放标准，同时实现了水杨酸生产废水中苯酚和水杨酸等化工资源的生产回用。     

不饱和聚酯树脂生产废水治理技术

不饱和聚酯树脂生产废水CODCr高达 10 0 0 0 0mg/L ,pH为 1— 2 ,且排放无规律 ,处理难度大。采用先对缩聚废水进行蒸馏浓缩 ,再真空泵废水混合调质、降温、缺氧水解后 ,经高效的好氧生物处理工艺 (HCR)处理后与低浓度的冲洗水、生活废水混合 ,进行低负荷的生物接触氧化处理 ,出水CODCr稳定在 10 0mg/L以下。     

络合萃取法处理5-氯水杨酸生产废水的研究与实践

采用络合萃取法处理5-氯水杨酸生产废水,研究了萃取过程中PH、络合剂、稀释剂等对废水革取效果的影响。通过比较,确定以EPT-1为络合剂。试验表明,pH<1.5,按废水:络合剂:稀释剂-100:30:70的比例投加,可取得较好效果。萃取剂连续使用15次,废水的CODCr去除率并无显著下降。多次萃取后萃取剂经氢氧化钠溶液反萃取再生,即可回收萃取剂。     

Fenton试剂和氨吹脱法处理苯唑醇废水的试验研究

采用Fenton试剂催化氧化和氨吹脱法对苯唑醇生产废水的处理进行了研究。实验结果表明 ,此方法对废水的CODCr和氨氮具有良好的去除效果 ,平均去除率分别达到 73 .5 %和 95 %以上。处理后废水的BOD5 CODCr>0 .45 ,其可生化性良好。该技术具有能耗低、操作简便等优点     

酵母菌处理皂素生产废水的研究

通过小型批量试验 ,对酵母菌处理皂素生产废水的技术条件进行了研究。结果表明 :在pH为 5 .0 ,温度 30℃ ,处理时间 4 8h ,接种量 10 %的条件下 ,废水CODCr去除率可达 70 %。该技术操作简单 ,可作为预处理应用于实际工程中 ,并可回收一定的酵母蛋白 ,具有一定的经济效益     

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。     

玉米淀粉生产废水处理工程设计与实践

通过奋达淀粉有限公司生产废水的处理工程实践，介绍厌氧-二次氧化工艺处理高浓度玉米淀粉生产废水的调试运行情况，运行结果表明：在进水CODCr为3800mg／L、SS在200mg／L、pH为4～5。处理后水质CODCr〈100、SS〈70、pH为6-9，达到《污水综合排放标准》（GB8978-1996）一级标准。     

酵母菌处理皂素生产废水的研究

通过小型批量试验，对酵母菌处理皂素生产废水的技术条件进行了研究。结果表明：在pH为5．0，温度30℃，处理时间48h，接种量10％的条件下，废水CODCr去除率可达70％。该技术操作简单，可作为预处理应用于实际工程中，并可回收一定的酵母蛋白，具有一定的经济效益。     

Selective removal of some polyhydric phenols from aqueous solution by ferric antimonate

Ferric antimonate, a cation-exchanger, has been investigated as an adsorbent for the removal of phenol and polyhydric phenols from aqueous solution. It has been found that ferric antimonate in H+ form selectively adsorbs polyhydric phenols having hydroxyl groups on adjacent positions. While phenol, resorcinol, and quinol did not show any appreciable adsorption, catechol, pyrogallol, and gallic acid having hydroxyl groups on adjacent positions exhibited considerable adsorption on ferric antimonate. Batch equilibrium experiments were carried out to study the effect of contact time, initial concentration of phenolic compounds, and temperature on the adsorption of phenolic compounds on ferric antimonate. The equilibrium time was found to be 1.5 hours for gallic acid and pyrogallol and 2 hours for catechol and salicylic acid. The adsorption data of the phenols at temperatures of 30 degrees, 40 degrees, and 50 degrees C have been described by Langmuir and Freundlich isotherm models. The best fit was obtained with the Langmuir model in the whole range of concentrations studied at all temperatures, indicating a monolayer adsorption onto a homogeneous adsorption surface. On the basis of the Langmuir isotherm, the maximum adsorption capacity of ferric antimonate for gallic acid, pyrogallol, catechol, and salicylic acid was found to be 3.915, 3.734, 2.397, and 2.758 mg/g, respectively at 30 degrees C. The maximum sorption capacity of ferric antimonate for the phenolic compounds studied is in the following order: gallic acid > pyrogallol > salicylic acid > catechol. The adsorption of phenolic compounds was found to decrease with an increase in temperature. Thermodynamic parameters like free energy, enthalpy, and entropy changes were calculated and discussed. The adsorption of polyhydric phenols on ferric antimonate is exothermic and spontaneous in nature.     

Aniline degradation by electrocatalytic oxidation

The degradation of aniline solution in alkaline medium of pH 11.0 by electrocatalytic oxidation has been studied using an electrochemical reactor containing a SnO₂–Sb₂O₃–PtO anode and a Ti cathode, both of 54 cm² area. Hydroxyl radicals (HO^√) are produced at the anode, being tested with the trace catcher salicylic acid and phenol by spectrophotometery and high performance liquid chromatography. Intermediates dianiline, 4-anilino phenol and azobenzol were detected by gas chromatography–mass spectrometry. The existence of HO^√ produced in the aniline degradation was assayed with scavenger tertiary butanol. The results showed that electrocatalytic oxidation is an effective process for the degradation of aniline. A general reaction pathway that accounts for aniline degradation to CO₂ involving those intermediates is proposed.     

Sorption of weak organic acids in soils: clofencet, 2,4-D and salicylic acid.

The sorption behaviour of a new wheat hybridising agent (clofencet, 2-4-(chlorophenyl)-3-ethyl-2,5-dihydro-5-oxopyridazine-4-carboxylic acid) was investigated in batch equilibrium experiments and compared to that of two other organic acids (2,4-D and salicylic acid). Sorption coefficients Kd for the three compounds were determined in 18 Cambisols and Ferralsols. Kd values for clofencet were 0.3-9.4 l/kg for Cambisols and 2.1-68 l/kg for Ferralsols. Sorption of clofencet was strongly related statistically to that of salicylic acid. Sorption of clofencet and salicylic acid decreased exponentially with increasing solution pH in Cambisols whereas a bell-shaped curve was obtained for the sorption of salicylic acid in Ferralsols. Sorption of 2,4-D (2,4-dichlorophenoxyacetic acid) was not statistically related to the pH of the different soils. Positively charged oxide surfaces were shown to play a significant role in the sorption of clofencet and salicylic acid. The use of simple correlation and multiple linear regressions suggested that the main sorption mechanisms of clofencet in soils were likely to be ligand exchange on oxide surfaces and, to a lesser extent, cation bridging. Differences in the sorption behaviour of clofencet/salicylic acid and 2,4-D might be attributed to the possibility of the two former compounds forming bidentate complexes with metals.     

Antibiotic effect of exogenously applied salicylic acid on in vitro soilborne pathogen, Fusarium oxysporum f.sp.niveum

Salicylic acid, which is biosynthesized inside plant and is often found and accumulated in soil due to plant debris decaying, is considered as a signaling substance during plant-microbe interactions. It is involved in the cycling of biogeochemistry and related to plant resistance to biotic and abiotic stress. The antibiotic effect of salicylic acid on Fusarium oxysporum f.sp.niveum (FON) was studied to investigate the relationships between the salicylic acid and the fungus in the ecological interaction of plant-microbe. Results showed that the biomass, colony diameter, number of conidium germination and conidium production of FON were decreased by 52.0%, 25.7%, 100% and 100% at concentrations of 800 mg L(-1). However, mycotoxin yield was increased by 233%, pectinase activity raised by 168.0% and cellulase activity increased by 1325% compared to control at higher concentrations. It was concluded that salicylic acid as an allelochemical greatly inhibited FON growth and conidia formation and germination, though stimulated mycotoxin production and activities of hydrolytic enzymes by FON.     

The role of ferrous ion in Fenton and photo-Fenton processes for the degradation of phenol

The efficiency of different Fenton-related oxidative processes such as Fenton, solar-Fenton and UV-Fenton were examined using phenol as a model compound in simulated and industrial wastewater. A batch study was conducted to optimize parameters like pH, hydrogen peroxide concentration and ferrous ion concentration governing the Fenton process. At optimum conditions, different Fenton-related processes were compared for the degradation of phenol. Increased degradation and mineralisation efficiency were observed in photo-Fenton processes as compared to conventional Fenton process. The maximum mineralising efficiency for phenol with Fenton, solar and UV-Fenton processes were 41%, 96% and 97% respectively. In Fenton process, carboxylic acids like acetic acid and oxalic acid were formed as end products during the degradation of phenol while in photo-Fenton processes, both these ions were identified during the early stages of phenol degradation and were oxidized almost completely at 120 min of the reaction time. In photo-Fenton processes (solar and UV light) complete degradation were observed with 0.4 mM of Fe2+ catalyst as compared to 0.8 mM of Fe2+ in conventional Fenton process. In Fenton and solar-Fenton processes, an iron reusability study was performed to minimize the amount of iron used in treatment process. The efficacy of Fenton and solar-Fenton processes was applied to effluent from phenol resin-manufacturing unit for the removal and mineralisation of phenol.     

腐殖酸、细颗粒泥沙对粉末活性炭吸附苯酚特性影响的研究

通过一系列实验,探讨了粉末活性炭吸附水中苯酚时,腐殖酸(HA)浓度和细颗粒泥沙用量对苯酚吸附量和去除率的影响.实验结果表明:在中性条件下,随着HA浓度的增加,粉末活性炭对苯酚的吸附量减少;在不同质量细颗粒泥沙的影响下,苯酚的去除率基本不变;在未加HA时,粉末活性炭对苯酚的吸附行为用Langmuir吸附等温式拟合效果最好,对苯酚的最大吸附量为150.60 mg/g,而在有HA存在时,粉末活性炭对苯酚的吸附行为用Freundlich吸附等温式拟合效果最好,对苯酚的最大吸附量为28.49 mg/g.     

Combined biological and photocatalytic treatment for the mineralization of phenol in water

Phenol is degraded by biological treatment, however mineralization requires long time. To decrease the time and operational cost necessary for the mineralization of phenol, an optimum operation condition of the combined biological–photocatalytical treatment was investigated. The mineralization of phenol (50 mg l⁻¹) was conducted in a flow-type biomembrane tank combined with a batch-type TiO₂-suspended photocatalytic reactor. Phenol was degraded biologically to the concentration of 6.8 mg l⁻¹, an effective concentration for further photocatalytic treatment. After the biological treatment, the biotreated phenol was treated photocatalytically to complete the mineralization of phenol. The combined treatment shortened the mineralization time compared to the biological treatment and electric cost compared to the photocatalytic treatment only. The combined treatment may be suitable for a short-time mineralization of phenol in wastewater.     

超/亚临界水中四溴双酚A的脱溴降解特性研究

在超/亚临界水及其碱溶液中对四溴双酚A进行了水热脱溴降解研究。考察了温度、时间和碱类型对降解特性的影响。结果表明,在纯水中温度是影响四溴双酚A降解的关键参数,350℃下反应180 min和400℃反应30 min,脱溴率分别达到98.7%和96.7%,降解产物中苯酚和4-丁基苯酚分别占50%和20%以上,另外还有少量的烷基酚;向反应体系中加入碱不仅可以中和反应过程中产生的氢溴酸以保护超临界反应釜,而且可以在较低温度下实现高的脱溴率,产物中苯酚含量达50%以上、4-异丙烯基苯酚占10%左右,可以实现脱溴同时回收化工产品的目的。与传统的热解技术相比,超/亚临界水处理TBBPA具有明显的优势,本研究为含溴电子废弃物的清洁高附加值资源化利用提供了一条新的途径。     

Mineralization of phenol by Ce(IV)-mediated electrochemical oxidation in methanesulphonic acid medium: a preliminary study

The mediated electrochemical oxidation (MEO) process using cerium(IV) in methanesulphonic acid (MSA) as the oxidizing medium was employed for the mineralization of phenol in batch and continuous feeding modes. Although nitric acid was an extensively studied electrolyte for organic mineralization reactions in MEO processes it does possess the problem of NO(x) gas production during the reduction of nitric acid in the cathode compartment of the electrochemical cell. This problem could be circumvented by proper choice of the electrolyte medium such as MSA. The mediator cerium in MSA solution was first oxidized to higher oxidation state using an electrochemical cell. The produced Ce(IV) oxidant was then used for the destruction of phenol. It was found that phenol could be mineralized to CO2 by Ce(IV) in MSA. The evolved CO2 was continuously measured and used for the calculation of destruction efficiency. The destruction efficiency was observed to be 85% based on CO2 evolution for 1000 ppm phenol solution at 80 degrees C in continuous feed mode.