氧化还原体系低温引发丙烯酸酯乳液聚合安全风险研究

以甲基丙烯酸甲酯、丙烯酸酯乙酯、丙烯酸酯丁酯为反应单体,十二烷基苯磺酸钠为乳化剂,过硫酸铵为氧化剂,亚硫酸氢钠为还原剂,在低温下进行乳液聚合。主要研究了反应单体的热稳定性及反应过程中的相关热力学参数,最后按照规定对该聚合体系进行了安全风险研究。研究结果表明,丙烯酸酯混合单体无热分解放热风险,丙烯酸酯乳液体系的绝热温升(△Tad)为49.6℃,失控体系能达到的最高温度(MTSR)为91.9℃,该体系的最终反应工艺危险度评估为1级,聚合工艺热风险低。     

环境空气中丙烯酸乙酯的气相色谱法测定

建立了环境空气中丙烯酸乙酯的TenaxGC吸附 -热解吸气相色谱测定方法。方法回收率为 87 3%～1 0 7 1 % ,变异系数为 5 3%～ 7 2 %。当采样体积为 2L时 ,检测限为 0 0 2mg/m3,具有采样时间短 ,不用任何溶剂等特点。     

Leaching characteristics of bisphenol A from epoxy-resin pavement materials

We investigated the leaching characteristics of bisphenol A (BPA) from two kinds of epoxy-resin pavement materials, one containing epoxy resins (EPs) and the other containing epoxy-acrylate resins (EPAs). Both samples contained residual BPA monomer, at levels of 9.0?µg?g^?1 for the EP resin sample and 4.4?µg?g^?1 for the EPA resin sample. These amounts were larger than amounts previously measured for polycarbonate samples. The amount of BPA leached from the samples increased with temperature. The leaching of BPA from EP was more strongly affected by temperature than the leaching from EPA. The pH also affected the amount of leached BPA. The maximum leached amount was observed under alkaline conditions (pH 10.8) for both sample types. The amounts of BPA that might leach from pavement materials during 1?h of heavy rain were estimated to be 0.9?µg?m^?2 for EP and 3.5?µg?m^?2 for EPA. Our results indicate that EPs disposed of in waste landfills without any treatment may be a source of BPA in leachate at landfill sites.     

改性阴极生物电芬顿系统降解罗丹明B

分别采用十八烷基三甲基氯化铵（OATC）和磷酸改性电极并负载铁涂覆在碳布表面,制得Fe/OC-OATC电极和Fe/PC电极用于构建生物电芬顿系统,提高电芬顿技术中H₂O₂的原位生产能力,达到高效降解印染废水的目的.通过极化曲线、功率密度曲线以及循环伏安曲线对2种复合电极的电化学性质进行分析,结果表明,Fe/OC-OATC的电流密度、最大功率密度以及氧还原能力等均优于Fe/PC,最大功率密度为4.89W/m³,相应的电流密度可达22.9A/m³.然后探究了2种复合电极构建的生物电芬顿系统对罗丹明B的降解效果,结果显示,Fe/OC-OATC体系﹥ Fe/PC体系,Fe/OC-OATC体系对罗丹明B的去除率最高达96.4%.最后根据动力学分析和反应机理的研究,分析了2种系统对罗丹明B的降解机理.     

螯合树脂去除丙烯酸丁酯废水中的二价阳离子

采用氨基膦酸螯合树脂C-900去除丙烯酸丁酯废水中的二价阳离子,考察了吸附温度和废水流量对树脂动态吸附性能的影响,并用Thomas模型进行动态吸附数据的拟合分析。实验结果表明,在吸附温度为35℃、废水流量为15SV的条件下,处理后出水中3种二价阳离子总质量浓度为1.0mg/L时的穿透体积为240BV,达到穿透体积时树脂对Ca²⁺,Mg²⁺,Cu²⁺的去除率分别为100%,99.2%,99.8%。     

丙烯酸酯类共聚物生产过程中职业病危害因素调查

通过对丙烯酸酯类共聚物生产过程中职业病危害因素进行调查,找出了职业病危害的关键控制点,并提出了防护要求。     

生物滴滤塔同步降解多组分挥发性有机物的实验研究

采用定向驯化活性污泥接种生物滴滤塔(BTF)同时处理甲苯、甲醇、丙烯酸乙酯挥发性有机化合物(VOCs)混合废气,考察BTF的长期稳定运行性能及微生物平均代谢活性.结果表明,混合气进口浓度低于910mg/m3时,BTF对VOCs混合废气总去除率可维持在80%以上,BTF可高效同步净化中低浓度VOCs混合废气;当进气负荷>120g/(m3·h)时,去除负荷趋于稳定,为100g/(m3·h)左右;CO2的生成量与混合废气的去除负荷的比值为1.731,表明BTF对此3种混合废气有较高程度的矿化;BTF对甲苯、甲醇、丙烯酸乙酯的降解行为符合Michaelis-Menten动力学模型,单位体积最大降解速率rmax分别是为90.9,50.5,58.5 g/(m3·h).平均吸光度(AWCD)值分析结果表明塔内微生物具有较高的代谢活性.     

高浓度有机废水脱除燃煤烟气NOx的试验研究

为研发经济、高效的有机废物与烟气NO_x协同控制技术,分别采用丙烯酸钠、工业酒精和萘磺酸钠高浓度有机废水替代氨水、尿素等常用脱硝剂,在热态燃煤试验炉上,研究了T(烟气温度)、φ(O₂)、停留时间和废水与烟气混合方式等参数对烟气脱硝的影响. 结果表明:在烟气温度为1 190 K时,丙烯酸钠、酒精和萘磺酸钠高浓度有机废水的脱硝效率分别为12.7%、14.2%和9.1%;烟气温度为1 360 K时,三者的脱硝效率分别达到37.6%、39.8%和35.9%;烟气温度高于 1360 K后,脱硝效率下降. φ(O₂)从4.1%增至5.2%时,脱硝效率降低了约21.5%、13.1%和15.7%;而φ(O₂)升至6.8%时,脱硝效率降至11.2%~13.6%. 丙烯酸钠废水喷射入温度分别为1 185和1 303 K的烟气时,逆向喷入比正向喷入的脱硝效率分别提高30.4%和19.3%;停留时间从0.67 s升至0.82 s时,3类废水脱硝效率分别提高16.0%、18.8%和16.6%.      

BS-18两性修饰膨润土对四环素和诺氟沙星复合污染的吸附

环境中抗生素污染已经成为当前研究的热点问题.为了探讨长碳链两性修饰膨润土对不同类型抗生素复合吸附的效应及机制,采用两性表面活性剂十八烷基二甲基甜菜碱（BS-18）修饰膨润土,研究了不同修饰比例、温度、pH值及离子强度条件下,BS-18两性修饰膨润土对四环素和诺氟沙星在单一及复合条件下的吸附,并结合两性修饰膨润土的表面特征来探讨其吸附机制.结果表明,与CK相比,经BS-18修饰后的土样CEC和比表面积下降,总碳和总氮含量上升.BS-18两性修饰膨润土对四环素的吸附量顺序为CK > 100BS > 25BS > 50BS,吸附符合Langmuir模型;而对诺氟沙星的吸附量顺序为25BS > 50BS > CK > 100BS,吸附符合Henry模型.四环素和诺氟沙星复合体系中,供试土样对四环素和诺氟沙星的吸附量均高于单一体系.随着温度的升高,两性修饰膨润土对四环素的吸附呈增温正效应,而对诺氟沙星随温度的升高吸附量总体上呈现下降的规律;当离子强度由0.001 mol·L^-1增加到0.5 mol·L^-1时,会抑制各供试土样对四环素和诺氟沙星的吸附;溶液pH会影响抗生素的存在形态,进而影响供试土样对其的吸附.BS-18修饰膨润土吸附四环素主要以电荷引力为主,而对诺氟沙星吸附则以电荷引力和疏水结合共同作用为主,两者辛醇/水分配系数对数值（lgKow）的不同以及结构的差异造成了吸附模式的不同;四环素+诺氟沙星复合体系中,形成了TC+NOR混合物促进了土样的吸附.     

New method for acrylic acid recovery from industrial waste water via esterification with 2-ethyl hexanol

Acrylic acid (AA) is an important component for the production of acrylate polymer. In a typical acrylic manufacturing unit, waste water contains AA in a range of 4–15 wt.% contributes to the high values of chemical oxygen demand. Due to the toxicity of AA to the aquatic organism, this wastewater should be treated before it is discharged to the environment. The waste water could be evaporated before sending to the incineration which was neither economic feasible nor environmental friendly. Esterification of wastewater containing carboxylic acid with alcohol could be a promising method to recover the acid by converting it to ester while purifying the wastewater. In the present study, recovery of AA via esterification with 2-ethyl hexanol (2EH) was investigated. The model industrial wastewater with various concentration of AA (10–100% w/w) was reacted with 2EH to produce 2-ethyl hexyl acrylate (2EHA) in the setups with total reflux and continuously water removal. These Amberlyst-15 (ion exchange resin) catalyzed reactions were carried out under the mass transfer resistance free region. The performance of both systems was compared. The yield for the reactions of the AA solutions with the AA concentrations of 30–80% was enhanced significantly when the reactions were carried out using the second setup. The kinetic data of the esterification of dilute AA was well described by the Eley–Rideal (ER) kinetic model incorporated with a correction factor to consider the catalyst fouling effect and pseudo-homogeneous (PH) kinetic model for the AA polymerization. The findings have shown the potential of recovering AA from the waste water stream via esterification. The concentrated AA solutions or larger amount of inhibitor should be adopted to prevent the catalyst fouling by the deposition of poly-acrylic acid on the catalyst surface.