Al-CTMAB复合膨润土同时吸附处理水中菲和磷酸根

用AlCl₃和溴化十六烷基三甲基铵(CTMAB)共同改性制得无机-有机复合膨润土Al-CTMAB-Bent,并研究其同时吸附处理水中菲和PO₄^3-的性能.结果表明,在菲和PO₄^3-的初始浓度分别为1 mg/L和5 mg/L(以P计)、水土比为800∶1时,Al-CTMAB-Bent对菲和PO₄^3-的去除率分别为96.3%和90.2%.Al-CTMAB-Bent沉降性能良好,沉降1 h后剩余浊度比相应的有机膨润土下降81.4%,为解决实际污水处理中有机膨润土固-液分离难题提供依据.     

改性膨润土预处理垃圾渗滤液试验研究

以溴化十六烷基三甲基胺为改性剂制备了有机改性膨润土,并对其进行了性能表征。将其应用于COD高达20000～37000mg/L的垃圾渗滤液的预处理,以垃圾渗滤液的COD去除率为考察指标,对原土和有机改性土的处理效果进行了对比,确定了改性膨润土最佳用量以及最佳反应条件。研究结果表明,有机改性膨润土处理效果明显优于原土。在改性土用量为30g/L,pH值为5左右,搅拌时间为40min,静置时间为30min时,能够使垃圾渗滤液的COD去除率达到67%以上,减轻了下一步生物处理的负荷。     

改性低品质膨润土处理柴油废水

选择阴阳离子十六烷基三甲基溴化铵CTMAB-十二烷基磺酸钠SDBS改性低品质膨润土,在8%的CTMAB:SDBS=5:1有机膨润土用量6.0 g/L,温度30℃,pH4~8之间,搅拌速度150 r/min,搅拌时间30 min的最优条件下,对50.0 mg/L的柴油吸附量可达到8.06 mg/g。改性后膨润土阳离子交换容量增加了1.6倍。红外光谱图和XRD谱图显示,表面活性剂已经进入膨润土层间。有机膨润土可同时吸附废水中的重金属铬和柴油,吸附均符合Freundlich等温式,对柴油的吸附是分配作用和表面吸附共同作用的结果,对重金属铬主要是表面吸附。     

有机膨润土多次吸附模拟废水中苯酚的性能及机理

研究了一系列有机膨润土多次吸附水中高浓度苯酚的性能及机理.结果表明,有机膨润土能够重复多次吸附水中苯酚,吸附性能较好.当多次吸附所用苯酚溶液初始浓度为1000mg/L时,3种单阳离子有机膨润土对其的吸附能力大小依次为:120 CTMAB-膨润土＞120 CPC-膨润土＞120 DTMAB-膨润土.在多次吸附过程中,有机膨润土对苯酚的吸附机理发生变化,由最初的表面吸附作用为主转变为分配作用为主.对CPC改性的膨润土而言,由于芳香性吡啶环的存在,苯酚被吸附到有机膨润土上后,能够产生"协同效应”,表现为随着苯酚吸附量的增大,分配系数K_p(c_sc_{w相似文献}   

Removal of polycyclic aromatic hydrocarbons and phenols from coking wastewater by simultaneously synthesized organobentonite in a one-step process

The optimal condition for a one-step process removing organic compounds from coking wastewater by simultaneously synthesized organobentonite as a pretreatment was investigated. Results showed that sorption of organic compounds by organobentonite was positively correlated to the cation surfactant exchange on the bentonite and the octanol-water partition coefficient (K_ow) of the solutes. With 0.75 g/L bentonite and 180 mg/L (60% of bentonite cation exchange capacity) cetyltrimethylammonium bromide, the removal efficiencies of the 16 polycyclic aromatic hydrocarbon (PAHs) specified by the US Environmental Protection Agency in coking wastewater except naphthalene were more than 90%, and that of benzo(a)pyrene was 99.5%. At the same time, the removal efficiencies of COD_Cr, NH₃-N, volatile phenols, colour and turbidity were 28.6%, 13.2%, 8.9%, 55% and 84.3%, respectively, and the ratio of BOD₅/COD_Cr increased from 0.31 to 0.41. These results indicated that the one-step process had high removal efficiency for toxic and refractory hydrophobic organic compounds, and could improve the biodegradability of the coking wastewater. Therefore it could be a promising technology for the pretreatment of toxic and refractory organic wastewater.     

Nitrification and denitrification in biological activated carbon filter for treating high ammonia source water

Since the ammonia in the effluent of the traditional water purification process could not meet the supply demand, the advanced treatment of a high concentration of NH₄ ⁺-N micro-polluted source water by biological activated carbon filter (BACF) was tested. The filter was operated in the downflow manner and the results showed that the removing rate of NH₄ ⁺-N was related to the influent concentration of NH₄ ⁺-N. Its removing rate could be higher than 95% when influent concentration was under 1.0 mg/L. It could also decrease with the increasing influent concentration when the NH₄ ⁺-N concentration was in the range from 1.5 to 4.9 mg/L and the dissolved oxygen (DO) in the influent was under 10 mg/L, and the minimum removing rate could be 30%. The key factor of restricting nitrification in BACF was the influent DO. When the influent NH₄ ⁺-N concentration was high, the DO in water was almost depleted entirely by the nitrifying and hetetrophic bacteria in the depth of 0.4 m filter and the filter layer was divided into aerobic and anoxic zones. The nitrification and degradation of organic matters existed in the aerobic zone, while the denitrification occurred in the anoxic zone. Due to the limited carbon source, the denitrification could not be carried out properly, which led to the accumulation of the denitrification intermediates such as NO₂ ⁻. In addition to the denitrification bacteria, the nitrification and the heterotrophic bacteria existed in the anoxic zone. __________ Translated from Environmental Science, 2006, 27(1): 69–73 [译自: 环境科学]     

Utilizing surfactants to control the sorption, desorption, and biodegradation of phenanthrene in soil-water system

An integrative technology including the surfactant enhanced sorption and subsequentdesorption and biodegradation of phenanthrene in the soil-water system was introduced and tested. For slightly contaminated agricultural soils, cationic-nonionic mixed surfactant- enhanced sorption of organic contaminants onto soils could reduce their transfer to plants, therefore safe-guarding agricultural production. After planting, residual surfactants combined with added nonionic surfactant could also promote thedesorption and biodegradation of residual phenanthrene, thus providing a cost-effective pollution remediation technology.0ur results showed that the cationic-nonionic mixed surfactantsdodecylpyridinium bromide (DDPB) and Triton X-100 (TX100) significantly enhanced soil retention of phenanthrene. The maximum sorption coefficient Kd* of phenanthrene for contaminated soils treated by mixed surfactants was about24.5 times that of soils without surfactant (Kd ) and higher than the combined effects of DDPB and TX100 individually, which was about 16.7 and 1.5 times Kd , respectively.0n the other hand, TX100 could effectively remove phenanthrene from contaminated soils treated by mixed surfactants, improving the bioavailability of organic pollutants. Thedesorption rates of phenanthrene from these treated soils were greater than 85% with TX100 concentration above2000 mg/L and approached 100% with increasing TX100 concentration. The biodegradation rates of phenanthrene in the presence of surfactants reached over 95% in30days. The mixed surfactants promoted the biodegradation of phenanthrene to some extent in 10-22days, and had no obvious impact on phenanthrene biodegradation at the end of the experiment. Results obtained from this study provide some insight for the production of safe agricultural products and a remediation scheme for soils slightly contaminated with organic pollutants.     

钙预处理对磁性锆铁改性膨润土吸附水中磷酸盐的影响

本研究制备了2种不同Ca2+含量的磁性锆铁改性膨润土(ZrFeBTs),即磁性锆铁改性原始膨润土(ZrFeRBT)和磁性锆铁改性钙预处理膨润土(ZrFeCaBT),并通过吸附实验考察了ZrFeRBT和ZrFeCaBT对水中磷酸盐的吸附特征,以确定Ca2+预处理对ZrFeBTs吸附水中磷酸盐的影响。结果发现,本研究所制备的ZrFeBTs包含Fe3O4和Zr,并且ZrFeCaBT中可交换Ca2+的含量明显高于ZrFeRBT。ZrFeBTs对水中磷酸盐吸附平衡实验数据可以很好地采用Langmuir等温吸附模型加以描述,动力学实验数据可以很好地采用准二级动力学模型和颗粒内扩散模型进行描述。根据Langmuir模型确定的ZrFeRBT和ZrFeCaBT对水中磷酸盐的最大单位吸附量(以磷计)分别为8.70mg·g-1和11.5mg·g-1。ZrFeBTs吸附水中磷酸盐的过程属于化学吸附。随着pH值的增加,ZrFeBTs对水中磷酸盐的吸附效果逐渐降低。当溶液共存Cl-、HCO3-、SO42-、NO3-、Na+、K+、Mg2+和Ca2+等阴阳离子时,ZrFeBTs对水中磷酸盐的吸附具有很好的选择性,并且溶液共存的Ca2+会极大地促进了ZrFeBTs对水中磷酸盐的吸附。采用Ca2+对膨润土进行预处理,极大地提高了ZrFeBTs对水中磷酸盐的吸附能力。     

苯酚、菲在BS-12/DTAB复配修饰膨润土上吸附的差异

为了探究复配修饰膨润土吸附疏水性不同的污染物的差异,采用阳离子型表面修饰剂十二烷基三甲基溴化铵(DTAB)对两性表面修饰剂十二烷基二甲基甜菜碱(BS-12)修饰膨润土进行复配修饰,采用批处理法研究复配修饰膨润土总修饰比例对苯酚和菲的等温吸附影响,并对比不同温度、pH值和离子强度条件下供试土样对苯酚和菲吸附量、热力学参数的差异.结果表明:随着总修饰比例的增大,复配修饰膨润土对苯酚及菲的吸附能力逐渐增强,0~50%CEC修饰比例下,菲的吸附率大于苯酚的吸附率,当修饰比例超出50%CEC后,苯酚的吸附率大于菲的吸附率,总修饰比例超出150%CEC后,膨润土对苯酚的吸附率变化趋于平缓,而对菲的吸附率开始呈下降趋势;随着土样总修饰比例的增大,温度对苯酚及菲吸附量的抑制效果降低;在KNO_3浓度为0.001~0.1 mol·L~(-1)时,苯酚及菲的吸附量均随着KNO_3浓度的增大而增大;随着pH值的升高,苯酚的吸附量逐渐增大,在pH=7处达到最大,而菲的吸附量则始终呈降低趋势.热力学参数显示,随着总修饰比例的增大,复配修饰土样对苯酚和菲的吸附自发性增强,混乱度增大,当总修饰比例超出150%CEC后,自发性减弱,混乱度下降.     

Adsorption and partition of benzo(a)pyrene on sediments with different particle sizes from the Yellow River

Experiments have been carried out to study the sorption of Benzo(a)pyrene(Bap) on sediment particles from the Yellow River using a batch equilibration technique. Effects of particle size on the adsorption and partition of Bap were investigated with the particle content of 3 g/L. Several significant results were obtained from the study. (1) Isotherms of Bap could be fitted with the dual adsorption-partition model under different particle sizes, and the measured value of the adsorption and partition was in agreement with the theoretical value of the dual adsorption-partition model. (2) When the particle diameter was d ⩾ 0.025 mm, the adsorption was predominant in the sorption of Bap, which accounted for 68.7%–82.4% of the sorption. For the particles with the size of 0.007 mm⩽d<0.025 mm, the adsorption was predominant when the equilibrium concentration of Bap was 0–8.87 μg/L in the water phase; and the partition was predominant when the equilibrium concentration of Bap was higher than 8.87 μg/L in the water phase. When the particle diameter was d<0.007 mm, the partition was predominant. (3) On the point of particle size, the contribution of adsorption to sorption followed the order: “d⩾0.025 mm”>“0.007 mm ⩽d<0.025 mm” >“d<0.007 mm”. (4) The partition coefficients of Bap in solids with different particle sizes were linearly correlated with the organic content, and the K _oc of Bap was about 1.26 × 10⁵ (L/kg). Translated from Acta Scientiae Circumstantiae, 2006, 26(2): 269–274 [译自: 环境科学学报]     

沈阳市典型城市河流优先控制污染物筛选及生态环境风险评估

细河和蒲河接纳了沈阳市工业废水的排放,水体中有毒、有害污染物不容忽视.为了明确河流中优先控制污染物,评价实际暴露水平下优先控制污染物对该水系生态环境的风险,选择细河和蒲河表层水为研究对象,开展了平水期、丰水期和枯水期的采样及有机污染物的检测分析;通过改进的潜在危害指数法对水体中检出的52种有机污染物打分排序,筛选了优先控制污染物;将效应评价外推法与商值法结合评价了优先控制污染物的生态环境风险.结果表明:52种有机污染物在细河中检出的平均质量浓度范围为9.20×10-6~1.37×10-1 mg/L,在蒲河中检出的平均质量浓度范围为4.30×10-6~3.03×10-2 mg/L.细河或蒲河中这些污染物的危害指数总分值（R）在22分以上的分别有12和13种,其中,PAEs（酞酸酯类）占6种,苯酚类污染物占4种.在细河中,DBP（邻苯二甲酸二丁酯）、苯酚、对甲基苯酚、2,4-二甲基苯酚和2,4,6-三甲基苯酚的R_q（风险商）>1,表明这些污染物存在较大的生态环境风险;在蒲河中,DBP、DEHP[邻苯二甲酸二（2-乙基己基）酯]和苯酚的R_q>1,表明这些污染物存在较高生态环境风险水平.研究显示,在细河、蒲河中PAEs和苯酚类有机物为优先控制污染物,其中部分优先控制污染物具有较高的生态环境风险,可为该流域有毒、有害物污染控制方案的制定提供参考和指导.      

河流库区沉积物-水界面营养盐及气态氮的释放过程和通量

以九龙江北溪西陂电站库区为例,于2013年不同季节开展原状泥柱静态培养、气态氮水柱剖面观测和通量模拟实验,结合水和沉积物理化参数和微生物参数,研究河流库区沉积物-水界面营养盐及气态氮的释放过程和通量.结果表明,库区沉积物NH+4和PO3-4总体表现为释放行为[平均NH+4通量(480±675)mg·(m2·d)-1,平均PO3-4通量(4.56±0.54)mg·(m2·d)-1],而NO-3和NO-2表现为吸附行为.洪水季节带来大量的有机质沉积在库区,造成枯水期沉积物无机氮磷向上覆水体释放.湖泊区气态氮释放以N2为主(>98%),沉积物-水界面N2释放通量平均为(15.8±12.5)mg·(m2·d)-1.水柱N2净增量有明显的空间差异和垂向分布规律,受沉积物-水界面生地化过程(反硝化和厌氧氨氧化作用)和流动水团的综合影响.下游站位存在较强的硝化作用,N2O相对富集,主要受水中氨氮占无机氮的比例控制.     

Circulating fluidized bed biological reactor for nutrients removal

A new biological nitrogen removal process, which is named herein “The circulating fluidized bed bioreactor (CFBBR)”, was developed for simultaneous removal of nitrogen and organic matter. This process was composed of an anaerobic bed (Riser), aerobic bed (Downer) and connecting device. Influent and nitrified liquid from the aerobic bed enters the anaerobic bed from the bottom of the anaerobic bed, completing the removal of nitrogen and organic matter. The system performance under the conditions of different inflow loadings and nitrified liquid recirculation rates ranging from 200% to 600% was examined. From a technical and economic point of view, the optimum nitrified liquid recirculation ratewas 400%. With a shortest total retention time of 2.5 h (0.8 h in the anaerobic bed and 1.5 h in the aerobic bed) and a nitrified liquid recirculation rate of 400% based on the influent flow rate, the average removal efficiencies of total nitrogen (TN) and soluble chemical oxygen demand (SCOD) were found to be 88% and 95%, respectively. The average effluent concentrations of TN and SCOD were 3.5 mg/L and 16 mg/L, respectively. The volatile suspended solid (VSS) concentration, nitrification rate and denitrification rate in the system were less than 1.0 g/L, 0.026-0.1 g NH₄ ⁺-N/g VSS·d, and 0.016–0.074 g NO_x ⁻-N/g VSS·d, respectively. __________ Translated from Environmental Engineering, 2007, 25(6): 2, 7–10 [译自: 环境工程]     

Partition of polycyclic aromatic hydrocarbons on organobentonites from water

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Degradation of endocrine disruptor bisphenol A in drinking water by ozone oxidation

The ozone oxidation of endocrine disruptor bisphenol A in drinking water was investigated. A stainless completely mixed reactor was employed to carry out the degradation experiments by means of a batch model. With an initial concentration of 11.0 mg/L, the removal efficiencies of BPA (bisphenol A) could be measured up to 70%, 82%, and 90% when the dosages of ozone were 1, 1.5, and 2 mg/L, respectively. The impacts on BPA degradation under the conditions of different ozone dosages, water background values, BPA initial concentrations, and ozone adding time were analyzed. The results showed that ozone dosage plays a dominant role during the process of BPA degradation, while the impact of the contact time could be ignored. UV wavelength scanning was used to confirm that the by-products were produced, which could be absorbed at UV254. The value of UV254 was observed to have changed during the ozonation process. Based on the change of UV254, it could be concluded that BPA is not completely degraded at low ozone dosage, while shorter adding time of total ozone dosage, high ozone dosage, and improvement of dissolved ozone concentration greatly contribute to the extent of BPA degradation. The effects of applied H₂O₂ dose in ozone oxidation of BPA were also examined in this study. The O₃-H₂O₂ processes proved to have similar effects on the degradation of BPA by ozone oxidation. Translated from Environmental Science, 2006, 27(2): 294–299 [译自: 环境科学]     

Effect of background electrolytes on the adsorption of nitroaromatic compounds onto bentonite

To further elucidate interaction of nitroaromatic compounds with mineral surface, the sorption of m-dinitrobenzene (m-DNB) and nitrobenzene to original bentonite in aqueous solution containing di erent electrolytes (i.e., KCl, NH4Cl, CaCl2 and Tetramethylammonium bromide (TMAB)) was studied. The sorption of m-DNB was greatly enhanced with the presence of KCl and NH4Cl, while little influence was observed with CaCl2 and TMAB, following the order of KCl > NH4Cl TMAB, CaCl2, or DI water. For nitrobenzene, sorption enhancement only occurred at high nitrobenzene concentrations in the presence of KCl, and the solute equilibrium concentration at inflexion point was lowered with increasing KCl concentration. These sorption enhancements were significantly promoted with the increase of electrolyte concentration. The salting-out e ect is insu cient to account for the sorption enhancement by original bentonite with increasing KCl or NH4Cl concentration. X-ray di raction patterns of bentonite suspensions indicated that the sorption enhancement of m-DNB was attributed to the intercalation of K+ or NH4 + into bentonite interlayer and then dehydration with m-DNB to form inner-sphere complexes, which caused previously expanded bentonite interlayers to collapse in aqueous suspension, thus further enhanced the interaction of phenyl with siloxane surface. In comparison, the sorption enhancement of NB is attributed to the formation of outer-sphere complexes with K+ at high solute-loadings (> 200–400 mg/kg). The sorption of m-DNB to initially modified TMA+-bentonite and K+-bentonite was almost the same as respective sorption to original bentonite in solution containing TMA+ and K+.     

A new method of inhibiting pollutant release from source water reservoir sediment by adding chemical stabilization agents combined with water-lifting aerator

A new method of adding chemical stabilization agents combined with water-lifting aerator can inhibit pollutant release from source water reservoir sediment effectively.     

不同水环境下苦草腐解对水质的影响

为探究沉水植物在不同水环境下的腐解对水质的影响,在实验室条件下分别模拟不同生物量沉水植物苦草在高纯水、上覆水及底泥悬浮液环境下的腐解过程及其对水体水质的影响,并分别讨论了N、P等含量在底泥和上覆水环境下的差异性.结果表明:① 随着时间的推移,苦草腐解均会导致上覆水及底泥悬浮液中pH先降后升,ρ（DO）急剧降低.在上覆水环境中,pH自7.8降至7.2,再增至8.7;与试验初期相比,ρ（DO）在第10天降低了56%.在底泥悬浮液中,pH自7.8降至7.3,再增至8.3;在第10天ρ（DO）降低了近60%.② 在上覆水及底泥悬浮液中,苦草腐解以释放有机氮为主,NH₃-N次之;ρ（TP）在试验前期呈先升后降趋势,但在试验中期底泥悬浮液环境中ρ（TP）则呈动态平衡,约为1 mg/L.③ 不同生物量（0.1、0.2、0.4 g/L）的苦草腐解后水环境中的营养盐含量有所不同,其中ρ（COD_Cr）、ρ（TP）与生物量呈正相关,在试验前期ρ（TN）、ρ（NO₂--N）随着峰值的增大而增大.研究显示,苦草腐解对两种水环境的物化性质有着相似的影响,而对其主要营养盐氮、磷形态的变化有着显著性的差异.      

光合细菌接触氧化工艺的研究

一、前言 光合细菌法(简称PSB法)具有负荷高、效果好、占地省等优点,菌体污泥又有很高的营养价值,可以回收利用。因此这是近年来引人注目的一种废水资源化及综合利用的新技术。有不少排出高浓度有机废水的工厂,     

水体中总有机卤化物的测定

研究一种测定水体中有冲有机卤化物（ＴＯＸ）含量的方法,分别通过气提和乙醚萃取并使用高温热解分光光度法测定挥发性有机卤（ＰＯＸ）和非挥发有机卤（ＮＰＯＸ）,方法检测限为１μｍｏｌ／Ｌ,变异系数〈３％,测得１０种不同类型的模拟化合物的平均回收率为８１％,自来水测定结果ＴＯＸ为２１７－４８３μｇ／Ｌ。