离子液体R_3NANR_3的制备及其脱硫性能

以二元酸和短链叔胺为原料,合成了已二酸三乙胺盐离子液体———R3NANR3。对该离子液体进行SO2气体的循环吸收和解吸行为的研究。实验结果表明,R3NANR3离子液体能对SO2气体进行有效的化学吸收。该吸收过程分二步进行,以第一步吸收为主。室温下（20℃）该离子液体在3 h以内吸收速率较快,3 h后吸收速率减慢并逐渐达到平衡。R3NANR3离子液体与SO2气体饱和吸收量的物质的量之比为1.08。较高温度将导致SO2气体的解吸,在90℃时饱和吸收液能较充分地解吸,残留量为0.0010 mol/L。多次吸收和解吸测试表明,R3NANR3离子液体能实现对SO2气体的循环吸收和分离,将成为烟气中SO2气体的脱除和利用的重要循环吸收剂。     

弱碱性树脂吸附-解吸苦味酸

考察了水中苦味酸在弱碱性离子交换树脂D301R上的吸附与解吸。研究了吸附热力学、动力学特性及吸附机理。结果表明,树脂在pH=2.7～10.2时,吸附能力最好。等温平衡吸附遵循Freundlich模型。吸附过程为吸热、熵增的自发过程。吸附动力学符合Lagergren准二级速率方程,颗粒内扩散为吸附速率的主要控制步骤,吸附速率常数为7.23×10-5～1.20×10-4g/(mg.min),吸附活化能为19.4 kJ/mol。树脂上吸附的苦味酸可用HNO3+丙酮混合液定量洗脱,洗脱率达99%。静态吸附和脱附的比较结果证实了吸附过程中存在不可逆化学吸附。树脂对苦味酸的吸附主要是通过静电吸附、酸碱络合吸附、氢键吸附等协同作用来完成的。     

室内空气总挥发性有机物检测的热解吸参数优化

总挥发性有机物(TVOC)是评价室内空气质量最重要的指标。为了提高TVOC检测的准确度,选取解吸气流量、热解吸温度、进样时间和热解吸时间四项因素设计正交实验,以热解吸率作为指标,对TVOC的热解吸过程进行了优化。并讨论在优化后参数的控制下,TVOC各组分的检测准确度。实验结果表明,优化的热解吸条件下各参数指标分别为解吸气流量40 mL/min、热解吸温度280℃、进样时间120 s、热解吸时间30 s。检测准确度的结果表明,在优化热解吸参数的控制下,各组分的回收率在90.3%～97.3%之间,满足TVOC的实际检测需求。     

土壤粒径及有机质对多溴二苯醚热脱附的影响

在实验室条件下,研究了土壤粒径与土壤有机质含量对多溴二苯醚(PBDEs)热脱附的影响,以期为PBDEs污染土壤热脱附修复提供理论依据。实验结果表明,300℃停留30 min条件下,粒径为<75、75～125、125～250、250～425和425～850μm的土壤中PBDEs去除率分别为49.53%、73.88%、79.39%、83.56%和87.09%,PBDEs总去除率随粒径的增大而增大,土壤BDE209较BDE206、BDE207和BDE208更易于脱除。此外,温度低于450℃时,H2O2氧化部分去除有机质后土壤中PBDEs的去除率较原土高;表明,土壤有机质可能抑制土壤中PBDEs的热脱附。     

改性疏水硅胶用于油气吸附解吸的研究

吸附法为油气回收的常用方法,对吸附剂的研究有着重要的意义。为了开发出高吸附量、高热稳定性和疏水性的油气回收专用硅胶,对常规硅胶的物理及化学改性方法进行了研究。通过分析热处理温度、热处理时间及升温速度等因素对改性硅胶吸附效果的影响,提出了汽油油气吸附率高、吸水率低的硅胶改性条件为:酒石酸改性剂,热处理温度550~650℃,热处理时间3~10 h,升温速度3~10℃/min。同时,研究了影响改性硅胶解吸效果的因素,结果表明,真空度越高,温度越高,解吸次数越多,改性硅胶的解吸率越高。     

离子交换树脂处理三乙胺废水

采用离子交换树脂对废水中三乙胺进行吸附。探讨了静态及动态吸附三乙胺的影响因素,考察了树脂的脱附条件及其吸附稳定性。实验结果表明:RX01型树脂对三乙胺的吸附性能优于HD-81型和D155型树脂;在三乙胺初始质量浓度为1 500 mg/L、初始pH为11.5、吸附时间为2 h、吸附温度为298 K的静态吸附条件下,三乙胺去除率为96.3%,饱和吸附量为145 mg/g,等浓度条件下阳离子影响的大小顺序为Ca~(2+)Mg~(2+)K~(+)Na~(+);当三乙胺初始质量浓度为1 500 mg/L、废水流量为60 BV/h、动态吸附柱高径比为5.37时,穿透体积为70 BV,出水三乙胺质量浓度小于3 mg/L,三乙胺去除率高达99.5%;以2 mol/L的HCl溶液为脱附剂,脱附剂流量为1 BV/h、出水体积为4 BV时,三乙胺的脱附率达94.8%;在最优动态吸附-脱附条件下重复使用10次,树脂性能稳定。     

羧甲基纤维素/有机蒙脱土纳米复合材料对刚果红的吸附与解吸性能

羧甲基纤维素(CMC)/有机蒙脱土(OMMT)纳米复合材料作为吸附剂应用于废水处理,对其结构进行了表征并对吸附时间、染料初始浓度、染料pH对该吸附剂吸附染料刚果红的影响进行了研究,同时探讨了吸附动力学和吸附热力学。结果表明,羧甲基纤维素与有机蒙脱土已经很好地复合,在吸附温度为30℃条件下,当吸附时间为4 h,染料初始浓度为800 mg/L,染料pH=10时吸附剂对染料表现出较好的吸附效果,吸附量可达156.64 mg/g。吸附符合伪二级动力学模型和Langmuir等温式。分别借助振荡器和超声波对吸附饱和的吸附剂进行解吸,研究解吸时间对吸附剂解吸实验的影响,结果表明,超声波条件下的解吸效果(34.45%)好于无超声波条件(15.69%),超声波有助于提高解吸率。     

Sorption-desorption behavior of metsulfuron-methyl and sulfosulfuron in soils

Sorption of metsulfuron-methyl and sulfosulfuron were studied in five Indian soils using batch sorption method. Freundlich adsorption equation described the sorption of herbicides with K_f (adsorption coefficient) values ranging between 0.21 and 1.88 (metsulfuron-methyl) and 0.37 and 1.17 (sulfosulfuron). Adsorption isotherms were L-type suggesting that the herbicides sorption decreased with increase in the initial concentration of the herbicide in the solution. The K_f for metsulfuron-methyl showed good positive correlation with silt content (significant at p = 0.01) and strong negative correlation with the soil pH (significant at p = 0.05) while sorption of sulfosulfuron did not correlate with any of the soil parameter. Desorption of herbicides was concentration dependent and, in general, sulfosulfuron showed higher desorption than the metsulfuron-methyl. The study indicates that these herbicides are poorly sorbed in the Indian soil types and there may be a possibility of their leaching to lower soil profiles.     

Effects of temperature on sorption-desorption processes of imidacloprid in soils of Croatian coastal regions

Sorption-desorption behavior of imidacloprid in six soils collected from five coastal regions in Croatia at 20, 30 and 40°C was investigated using batch equilibrium technique. Isothermal data were applied to Freundlich, Langmuir and Temkin equations, and the thermodynamic parameters ΔH°, ΔG°, ΔS° were calculated. The sorption isotherm curves were non-linear and may be classified as L-type, suggesting a relatively high sorption capacity for imidacloprid. Our results showed that the K ^sor _F values decreased for all the tested soils as the temperature increased, indicating that the temperature strongly influences the sorption. Values of ΔG° were negative (?4.65 to ?2.00 kJ/mol) indicating that at all experimental temperatures the interactions of imidacloprid with soils were spontaneous processes. The negative and small ΔH° values (?19.79 to ?8.89 kJ/mol) were in the range of weak forces, such as H-bonds, consistent with interactions and partitioning of the imidacloprid molecules into soil organic matter. The ΔS° values followed the range of ?57.12 to ?14.51 J/molK, suggesting that imidacloprid molecules lose entropy during transition from the solution phase to soil surface. It was found that imidacloprid desorption from soil was concentration and temperature-dependent, i.e. at lower imidacloprid concentrations and temperature, lower desorption percentage occurred. Desorption studies revealed that hysteretic behavior under different temperature treatments existed, and it was more pronounced at 20°C in the soils with higher OC content. The study results emphasize the importance of thermodynamic parameters in controlling soil pesticide mobility in different geographical locations, seasons and greenhouse conditions.     

Sorption–desorption of indaziflam and its three metabolites in sandy soils

Indaziflam is a relatively new herbicide for which sorption–desorption information is lacking, and nothing is available on its metabolites. Information is needed on the multiple soil and pesticide characteristics known to influence these processes. For four soils, the order of sorption was indaziflam (N-[1R,2S)-2,3-dihydro-2,6-dimethyl-1H-inden-1-yl]-6-[(1R)-1-fluoroethyl]-1,3,5-triazine-2,4-diamine) (sandy clay loam: K_f = 5.9, 1/n_f = 0.7, K_foc = 447; sandy loam: K_f = 3.9, 1/n_f = 0.9, K_foc = 276) > triazine indanone metabolite (N-[(1R,2S)-2,3-dihydro-2,6-dimethyl-3-oxo-1H-inden-1-yl]-6-[(1R)-1-fluoroethyl]-1,3,5-triazine-2,4-diamine) (sandy clay loam: K_f = 2.1, 1/n_f = 0.8, K_foc = 177; sandy loam: K_f = 1.7, 1/n_f = 0.9, K_foc = 118) > fluoroethyldiaminotriazine metabolite (6-[(1R-1-Fluoroethyl]-1,3,5-triazine-2,4-diamine) (sandy clay loam: K_f = 0.3, 1/n_f = 0.9, K_foc = 28; sandy loam: K_f = 0.3, 1/n_f = 0.9, K_foc = 22) = indaziflam carboxylic acid metabolite (2S,3R)-3-[[4-amino-6-[(1R)-1-fluoroethyl]-1,3,5-triazin-2-yl]amino]-2,3-dihydro-2-methyl-1H-indene-5-carboxylic acid) (sandy clay loam: K_f = 0.3, 1/n_f = 0.9, K_foc = 22; sandy loam: K_f = 0.5, 1/n_f = 0.8, K_foc = 32). The metabolites being more polar than the parent compound showed lower sorption. Desorption was hysteretic for indaziflam and triazine indanone metabolite, but not for the other two metabolites. Unsaturated transient flow K_d's were lower than batch K_d's for indaziflam, but similar for fluoroethyldiaminotriazine metabolite. Batch K_d's would overpredict potential offsite transport if desorption hysteresis is not taken into account.