膜萃取邻甲酚废水的传质特性研究

构造了卷绕式及管束式两种膜组件,采用均质硅橡胶膜,以氢氧化钠溶液为萃取液来萃取邻甲酚废水.通过考察邻甲酚初始浓度、两相流动状态、两相压差(△P)和温度等因素对传质过程的影响,研究了邻甲酚废水的膜萃取过程与机制.结果表明,初始质量浓度为21.93 g/L的邻甲酚废水很适合直接进行膜萃取;当△P<0.07 MPa时,总传质系数(Kov)随△P的增大而略有减小.当△P>0.07 MPa时,Kov随△P增大而显著增大,由实验数据拟合得到总的膜萃取传质模型.且该模型的实验值与理论值的相对误差在5%以内,满足工业设计要求.     

用HL离心萃取器处理含对硝基酚废水的研究

溶剂萃取法是目前回收处理含高浓度对硝基酚废水的有效方法.选用QH-1为萃取剂,采用HL离心萃取器对含对硝基酚废水的处理进行了实验研究.实验结果表明,对于对硝基酚硝酸溶液-QH-1体系,对硝基酚的分配比是1103.4,用Φ20 mm HL离心萃取器处理对硝基酚废水时,在合适的操作条件下,单级传质级效率E和三级串联萃取率ρ都可达99%以上,三级串联的反萃率也可达98%以上.     

生物柴油萃取高浓度吡啶废水

农药、医药等行业的生产过程中产生含有高浓度吡啶的废水,采用溶剂萃取法萃取废水中的吡啶既可改善废水的可生化性,又可实现吡啶的循环利用.实验以生物柴油为萃取剂,讨论了体系的pH值、温度、相比及时间等条件对萃取分配系数(D)及吡啶去除率的影响.结果表明,较为适宜吡啶萃取的条件是:萃取时间为30 min,pH值为6,温度为30℃,相比为1:1.在上述萃取条件下,生物柴油与吡啶水溶液进行六级错流萃取后,水中吡啶浓度从15%降至0.84%,吡啶去除率达到94.40%.     

用HL离心萃取器处理含对硝基酚废水的研究

溶剂萃取法是目前回收处理含高浓度对硝基酚废水的有效方法。选用QH-1为萃取剂，采用HL离心萃取器对含对硝基酚废水的处理进行了实验研究。实验结果表明，对于对硝基酚硝酸溶液-QH-1体系，对硝基酚的分配比是1103．4，用Φ20mmHL离心萃取器处理对硝基酚废水时，在合适的操作条件下，单级传质级效率E和三级串联萃取率ρ都可达99％以上，三级串联的反萃率也可达98％以上。     

萃取技术分离工业废水中的苯胺

研究以硝基苯为萃取剂,25℃下通过盐析萃取法回收工业废水中苯胺。以静态分批实验考察了废水酸度、初始苯胺浓度、萃取剂与废水比(油水比)、萃取级数、无机盐种类(NaCl,KCl,Na2SO4,CaCl2,K2SO4)和浓度对苯胺萃取率的影响,获得了最佳操作工艺条件。实验结果表明,硝基苯盐析萃取技术可以有效回收废水中苯胺,且高pH和溶剂比有利于苯胺萃取,随着无机盐浓度的增加苯胺回收率增加。在适宜的条件下,通过盐析作用,经过五级萃取苯胺萃取率接近100%。     

膜萃取处理高浓度工业苯胺废水

大连市某药业公司生产中产生的高浓度苯胺废水可生化性极差,传统工艺处理该废水难度大,且不能回收利用苯胺.采用膜萃取工艺处理该废水,工艺运行稳定,苯胺去除率高.实验结果表明,在进水流量为3.05 L/d、反应温度为50 ℃、萃取液pH≈1、膜管长18 m条件下,进水苯胺质量浓度为33 081 mg/L时,苯胺去除率稳定在97%以上.进行经济核算,每吨废水净收益为103.84元.     

萃取净化电镀含镉废水

研究了二壬基萘磺酸(DNNSA)形成的微乳液从模拟含镉废水中萃取镉离子的工艺条件。分别考察了相体积比(O/A)、萃取时间、温度及萃取剂浓度对废水中镉离子萃取的影响。结果表明,萃取平衡时间为10 mim,降低温度及增加萃取剂浓度均有利于萃取。紫外光谱证实当DNNSA萃取镉时,所形成萃合物对萘环的结构无影响,且不会破坏微乳相的结构;分子荧光光谱表明镉离子对配体DNNSA有荧光猝灭作用。     

Fenton氧化与铁炭微电解组合预处理DMF废水

对COD表征模拟废水中DMF去除率的可行性进行了探讨。在此基础上,分别对铁炭微电解、Fenton氧化-铁炭微电解和铁炭微电解-Fenton氧化组合工艺对DMF废水的处理效果进行分析,结果表明,Fenton氧化-铁炭微电解工艺的处理效果较好。在pH=5,反应时间为1 h,FeSO4·7H2O投加量为1 000 mg/L、H2O2投加量为2.67 mL/L和不曝气的最佳反应条件下,Fenton氧化-铁炭微电解工艺对实际废水和废液中COD的去除率分别达到66.67%和72.22%,从而验证了该工艺处理DMF废水的可行性。此外,Fenton氧化处理DMF废水过程实际上是将酰胺基团和羰基的不饱和双键氧化分解的过程。     

兰炭废水中酚类物质萃取及回收效果

为了去除并回收兰炭废水中的高浓度挥发酚类物质,实验研究了甲基异丁酮溶剂在不同条件下对兰炭废水中挥发酚的萃取及回收效果。结果表明,萃取时间为10 min,温度为35℃,p H低于8.0,萃取体积比(萃取剂体积/兰炭废水体积)在大于1∶5时,经过萃取后废水中挥发酚浓度由6 385 mg/L降至230 mg/L,去除率高达96.4%,有效减轻了后续生化处理的负担。而萃取剂经过蒸馏分离后,挥发酚的回收率可达95%以上,甲基异丁酮的损耗率为0.18%~0.2%。实验表明,甲基异丁酮是一种可以长期循环使用的工业萃取剂,显示了良好的应用前景。     

磷酸三丁酯络合萃取邻氨基苯酚及工业废水预处理研究

根据络合萃取的原理,考虑了萃取剂与稀释剂之间的作用,选择磷酸三丁酯(TBP)为萃取剂,以正辛醇和氯仿为极性稀释剂、四氯化碳和煤油为非极性稀释剂,对邻氨基苯酚(OAP)稀溶液进行了探讨,讨论了体系的pH、TBP的浓度、稀释剂种类对萃取分配比(D)的影响.结果表明,TBP主要通过与OAP的中性分子键合作用实现萃取;D值的变化与中性分子的摩尔分数有关,pH是影响D的主要因素;稀释剂的极性对OAP的萃取影响较大,在萃取剂体积分数为10%～30%时,其萃取能力为TBP-正辛醇＞TBP-煤油＞TBP-四氯化碳＞TBP-氯仿;在萃取剂体积分数为30%～50%时,萃取能力为TBP-煤油＞TBP-正辛醇＞TBP-四氯化碳＞TBP-氯仿.进而以30%TBP-煤油为萃取剂,对工业含OAP废水进行了错流萃取实验.实验表明,该方法可以对工业OAP废水进行有效的(94.7%)预处理;工业废水中的甲醇、乙醇,对萃取有较大影响.     

Compressed air-assisted solvent extraction (CASX) for metal removal

A novel process, compressed air-assisted solvent extraction (CASX), was developed to generate micro-sized solvent-coated air bubbles (MSAB) for metal extraction. Through pressurization of solvent with compressed air followed by releasing air-oversaturated solvent into metal-containing wastewater, MSAB were generated instantaneously. The enormous surface area of MSAB makes extraction process extremely fast and achieves very high aqueous/solvent weight ratio (A/S ratio). CASX process completely removed Cr(VI) from acidic electroplating wastewater under A/S ratio of 115 and extraction time of less than 10s. When synthetic wastewater containing Cd(II) of 50mgl(-1) was treated, A/S ratios of higher than 714 and 1190 could be achieved using solvent with extractant/diluent weight ratio of 1:1 and 5:1, respectively. Also, MSAB have very different physical properties, such as size and density, compared to the emulsified solvent droplets, making separation and recovery of solvent from treated effluent very easy.     

Study on reaction kinetics and selective precipitation of Cu, Zn, Ni and Sn with H₂S in single-metal and multi-metal systems

Determination of reaction kinetics and selective precipitation of Cu, Zn, Ni and Sn with H(2)S in single-metal and multi-metal systems were studied to develop a process of metal recovery from plating wastewater. As samples, single-metal model wastewaters containing Cu, Sn, Zn or Ni, and multi-metal model wastewater containing Cu-Zn-Ni or Sn-Zn mixtures were used. In both single-metal and multi-metal systems, the pH value was precisely controlled at a value of 1.5 for CuS and SnS precipitation, 4.5 for ZnS precipitation and 6.5-7.0 for NiS precipitation. Subsequently, the sulfidation of Cu, Sn, Zn and Ni was evaluated. It was found that an amount of H(2)S equimolar to a given metal was sufficient to achieve almost complete precipitation of the particular metal. Further, the selectivity of metal precipitation was found to be higher than 95% in the Cu-Zn-Ni multi-metal system and higher than 91% in the Sn-Zn system. It was also found that the sulfidation reaction proceeded in accordance with Higbie's penetration theory and reaction rate constants and mass-transfer coefficients under various experimental conditions were determined. Finally, the reaction rate constants obtained in single-metal and multi-metal systems were found to be almost the same indicating that the precipitation of a particular metal was not significantly affected by the presence of other components.     

Phosphorus recovery from wastewater--expert survey on present use and future potential

Today, a variety of different approaches to the recovery of phosphorus from wastewater, sludge, and sludge ash exist. These approaches differ basically by the origin of the used matter (wastewater, sludge liquor, fermented or nonfermented sludge ash) and the process (precipitation, wet-chemical extraction, and thermal treatment). To rate them according to their characteristics, the latter were phrased as hypotheses and subjected to an international expert survey. The survey showed that phosphorus recovery is expected to become an established process over the next 20 years in industrialized countries for economic reasons. A decisive aspect in this regard will be the quality of the produced fertilizer. Simple technologies such as the recovery from sludge liquor seem to be preferred. If sludge is incinerated, phosphorus recycling from ash then becomes more interesting and has to be considered. Phosphorus recovery and source-separating sanitation technologies are more appropriate for industrialized countries than for developing countries. Because the growing awareness of environmental issues will prevent sludge from being used agriculturally in an increasing number of countries in the next decade, the market potential for nutrient recovery technologies will increase in the immediate future.     

NaCl-丙醇双水相体系分离富集草甘膦生产废水中草甘膦铵盐

利用草甘膦生产废水中接近饱和的NaC1与丙醇形成的双水相体系分离富集废水中部分残留的草甘膦铵盐,达到了资源循环利用和资源的高效回收.通过分析表面活性剂种类及用量,pH,丙醇质量分数和NaC1质量分数4个因素确定了最佳萃取条件.最后对该方案进行仿真验证,表明利用该方案对实际废水的处理比较理想,实现了90.7％的高回收率,完全符合工业化要求.     

混凝沉淀前处理对丙烯酸丁酯废水陶瓷膜过滤膜污染的影响

采用混凝沉淀-双层滤料过滤-陶瓷膜过滤组合工艺去除丙烯酸丁酯废水中浊度物质。结果表明,废水pH值、混凝药剂投加量、混凝沉淀水力条件不仅对丙烯酸丁酯废水混凝沉淀出水和双层滤料过滤单元出水浊度具有重要影响,而且对后续陶瓷膜过滤单元膜污染均具有重要影响。双层滤料过滤出水浊度与陶瓷膜污染阻力具有明显的正相关关系,双层滤料过滤出水浊度越高,陶瓷膜污染阻力越大。废水pH在7.0~10.0范围内、混凝药剂PAC或PAM投加过量、废水流量过高都会造成双层滤料过滤出水浊度偏高,导致陶瓷膜污染严重。     

蒸汽驱采废水回用高压锅炉给水处理工艺的研究

对蒸汽驱采废水回用高压锅炉给水处理工艺进行了研究,并对比分析了不同的工艺组合流程对蒸汽驱采废水回用高压锅炉给水的处理效果。结果表明,蒸汽驱采废水回用高压锅炉给水处理在技术上是可行的,并提出推荐工艺流程。     

组合方法去除新型采油污水中有机污染物的研究

含聚丙烯酰胺采油污水的有效处理是近年来困扰油田三次采油生产的一个难题。研究采用移动床生物膜技术与O3/UV/H2O2高级氧化技术的组合方法来处理含聚丙烯酰胺采油污水。实验结果表明,移动床生物膜技术可以有效去除污水中的石油类有机物,但对聚丙烯酰胺几乎无效果。O3/UV/H2O2高级氧化技术可以降解污水中的聚丙烯酰胺。组合方法处理后的含聚丙烯酰胺采油污水水质可以达到污水综合排放标准中的一级要求。     

Determination of PAHs in wastewater irrigated agricultural soil using accelerated solvent extraction

A procedure was developed for determination of 16 polycyclic aromatic hydrocarbons (PAHs) in heavily contaminated paddy soil from wastewater irrigated farmland near Tianjin. The sample was distilled with accelerated solvent extraction (ASE), purified by a silica gel column, and measured with GC/MS. The optimal conditions for the distillation were at 140 degrees C (1500 psi) with a 1:1 mixture of dichloromethane and acetone for 5 min. Application of cyclohexane for extract transfer improved the recovery when the ASE extraction was followed by a silica gel cleanup procedure. Recoveries from the method for 16 PAHs ranged from 57-140% with the coefficients of variation of the results ranging from 0.35% to 5.75%. The total 16 PAHs in a composite sample collected from a wastewater irrigated paddy field near Tianjin was 3.90 mg/kg.