铜、锌氰配合物在离子交换纤维上的扩散、吸附机理

运用Boyd液膜扩散公式和范山鹰等提出的扩散模型,考察了碱性溶液中铜、锌氰配合物在离子交换纤维上的扩散行为;通过分析吸附前后纤维上官能团的位置变化以及解吸前后纤维上元素含量的变化,研究铜、锌氰配合物在纤维上的吸附机理。实验结果表明,离子交换纤维对铜、锌配合物的吸附在反应初期,以液膜扩散为主控制步骤,反应后期,以空隙扩散为主控制步骤。并运用离子交换纤维在水溶液中具有类似胶体型物质的双电层结构解释了不同控制阶段吸附速率不同的原因,虽然各阶段吸附速率有所不同,但纤维对铜、锌氰配合物的吸附均为离子交换机制。     

离子交换纤维对金属氰络合物吸附性能的研究

采用强碱性离子交换纤维对含氰废水中主要离子铜氰络合物、锌氰络合物的吸附性能进行了研究。实验结果表明：含氰废水的pH在8—11范围内，纤维材料对金属氰络合物具有良好的吸附性能；纤维对铜氰络合物、锌氰络合物的吸附速率很快，4min左右就可达吸附平衡；温度对铜氰络合物、锌氰络合物吸附影响不大，纤维的这些吸附特点对工业应用非常有利。     

离子交换纤维对金属氰络合物吸附性能的研究

采用强碱性离子交换纤维对含氰废水中主要离子铜氰络合物、锌氰络合物的吸附性能进行了研究.实验结果表明:含氰废水的pH在8～11范围内,纤维材料对金属氰络合物具有良好的吸附性能;纤维对铜氰络合物、锌氰络合物的吸附速率很快,4 min左右就可达吸附平衡;温度对铜氰络合物、锌氰络合物吸附影响不大,纤维的这些吸附特点对工业应用非常有利.     

离子吸附技术在废水处理中的应用和发展

本文介绍了废水中金属离子处理技术的发展 ,包括离子交换树脂技术 ,功能高分子吸附技术 ,生物吸附应用以及电渗析技术等。     

麦饭石对重金属离子的吸附作用研究

研究了麦饭石对重金属离子，如Ｐｂ＾２＋、Ｃｕ＾２＋，Ｚｎ＾２＋，Ｃｄ＾２＋的吸附作用，实验结果表明，麦饭石对重金属离子具有较强的吸附性能，ｐＨ是影响吸附的主要因素，探讨了麦饭石吸附作用机理，认为离子交换和表面络合反应是主要的吸附形式。并结合对实际重金属废水的吸附净化作用讨论麦饭石在废水处理方面应用的可行性。     

生物吸附-膜反应器富集生活污水中碳源物质的特性

设计并构建了生物吸附-微滤膜反应器,利用活性污泥的吸附作用及微滤膜的高效分离作用,处理来自不同生活污水处理厂的进水,分析典型城市污水中碳源物质的形态分布,以及生物吸附-微滤膜反应器对生活污水中含碳物质的富集分离效果。结果表明,生物吸附-微滤膜反应器对胶体COD的去除率较高,为60%~76%,对溶解态COD的去除率较低,为29%~38%;不同HRT对反应器的运行效果影响不大,综合考虑COD富集率及系统运行的经济性,本研究推荐的运行参数为SRT=2 d,HRT=22 min,藉此,生物吸附-膜反应器对碳源物质的富集回收率可达到50.0%左右。     

含铅废水处理技术及其展望

详细介绍了含铅废水的5种主要处理方法，包括化学沉淀法、离子交换法、液膜法、生物吸附法及电解法，对各种方法的优缺点及发展现状进行了介绍，另外，还对含铅废水处理的前景进行了展望，提出了电解法与离子交换法或与生物吸附法相结合是处理含铅废水的发展方向。     

活性炭纤维吸附废水中对硝基苯酚及其脱附研究

采用新型高效吸附剂——活性炭纤维吸附废水中对硝基苯酚，对其吸附和脱附影响因素进行了较详细的研究，确定了最佳工艺参数，并对动态吸附一脱附进行了稳定性实验。在最佳的吸附条件下，装填4g活性炭纤维可处理含对硝基苯酚1000mg/L的废水1400mL，出水对硝基苯酚浓度〈2mg／L，达到国家综合污水一级排放标准，活性炭纤维有效吸附量可达349．87mg／g。在最佳脱附条件下，脱附率〉99％，并可从高浓度脱附液中回收对硝基苯酚。稳定性实验表明，吸附-脱附性能稳定，采用活性炭纤维吸附处理对硝基苯酚废水是一种行之有效的处理方法。     

气质联用分析加硫酸化污泥中的有机酸

分别采用两种前处理方法分离富集加硫酸化污泥中的有机酸.方法一,利用阴离子交换树脂分离富集有机酸,在不洗脱的情况下直接和乙醇进行酯化反应,然后进行气质联用分析;方法二,利用活性炭纤维吸附型固相微萃取(ACF-SPME)的方法,顶空萃取分离后进行气质联用分析.两种方法的分析结果都未检测到酸化污泥中存在短链的有机酸,只检测到个别长链的和带苯环结构的有机酸.     

活性炭纤维在环境保护中的应用及前景

本文介绍了一种新型环境功能材料———活性炭纤维在环境保护中的应用现状及前景。通过与以颗粒活性炭为代表的传统碳材料在结构、性能方面的对比 ,概述了活性炭纤维优良的吸附、催化氧化等特性。然后全面介绍了活性炭纤维在气体处理、水处理、劳动防护、环境监测及清洁生产等方面的应用。同时结合目前活性炭纤维的研究开发现状 ,分析了制约其发展的因素 ,提出了相应的对策 ,并指出了发展方向。     

Polycyclic aromatic hydrocarbon removal from water by natural fiber sorption.

The use of two natural sorbents, kapok and cattail fibers, were investigated for polycyclic aromatic hydrocarbon (PAH) removal from water. Naphthalene, acenaphthylene, acenaphthene, fluorene, phenanthrene, anthracene, and fluoranthene were the PAHs studied. For comparative purposes, a commercial polyester fiber sorbent was included in the investigation. The PAH sorption and retention capabilities of the three fibers were determined through batch and continuous-flow experiments under non-competitive and competitive conditions. In the batch experiments, cattail fiber was the most effective sorbent. Kapok fiber provided the lowest PAH retention, while cattail fiber had slightly less PAH retention than polyester fiber. When two PAHs were present in the same system, a competitive effect on the much less hydrophobic PAH was observed. Similar results were obtained in the column experiments, except that polyester fiber performed much poorer on naphthalene. Cattail fiber is a promising sorbent for treating PAH-contaminated water, such as urban runoff.     

湿式纤维层非稳态过滤净化阻力的研究

在干式纤维层过滤净化阻力的理论基础上,提出清洗水均匀分布于纤维丝表面的基本假设,使湿式过滤中对液滴、液膜、液珠的分析简单具体化。并通过实验结论归纳出净化阻力随时间的变化规律,导出湿式纤维层非稳态过滤净化阻力的表达式,并用实验验证了其准确性。     

泥炭作为吸油材料的试验

为了研制一种理想的吸油剂,对泥炭、秸秆、锯末和改性泥炭用作吸油材料进行了对比试验.结果表明,未改性的风干泥炭吸油效果好于秸秆和锯末,而且是藓类泥炭吸油效果好于草本泥炭;对于同一类型的泥炭,中细纤维结构的吸油量高于中粗纤维结构的;与未改性的风干泥炭相比,不论采用物理方法还是物理化学方法进行改性,改性后泥炭的吸油效果均好于改性前的.试验证明了泥炭可以作为一种吸油材料,尤其是改性后的泥炭更是一种效率高、成本低、环保型的吸油材料.     

活性炭纤维及其在水处理中的应用

介绍了活性炭纤维材料的发展历史、类别、结构性能、制备过程。活性炭纤维比普通活性炭性能优越，吸附量大，机械强度高，吸附、脱附速度快，正逐渐地被用于废水处理和饮用水的净化。其具体方法有常用的吸附法、电解法，以及尚在起步阶段的生物活性炭纤维法。     

On Sorbent Activation in Coolside Desulfurization

In a coolside desulfurization process, partly unreacted sorbent from the boiler injection, or fresh sorbent injected into the flue-gas duct, is activated by a water spray. Primarily as a result of Inertial impactions between the sorbent particles and the water droplets, highly active slurry droplets are formed. In this paper, a theoretical model for the calculation of the sorbent activation efficiency is derived. The influence of design and operating parameters on the activation has been calculated with a simulation program. The initial mean value and standard deviation of the droplet diameter and the difference in Initial velocity between the droplets and the flue-gas are shown to be the most important parameters in addition to the water/gas ratio. The sorbent particles are activated primarily in the vicinity of the atomizing nozzles.     

Use of biomass sorbents for oil removal from gas station runoff

The use of biomass sorbents, which are less expensive and more biodegradable than synthetic sorbents, for oil removal from gas station runoff was investigated. A bench-scale flume experiment was conducted to evaluate the oil removal and retention capabilities of the biomass sorbents which included kapok fiber, cattail fiber, Salvinia sp., wood chip, rice husk, coconut husk, and bagasse. Polyester fiber, a commercial synthetic sorbent, was also experimented for comparison purpose. Oil sorption and desorption tests were performed at a water flow rate of 20 lmin-1. In the oil sorption tests, a 50 mgl(-1) of used engine oil-water mixture was synthesized to simulate the gas station runoff. The mass of oil sorbed for all sorbents, except coconut husk and bagasse, was greater than 70%. Cattail fiber and polyester fiber were the sorbents that provided the least average effluent oil concentrations. Oil selectivity (hydrophobic properties) and physical characteristics of the sorbents are the two main factors that influence the oil sorption capability. The used sorbents from the sorption tests were employed in the desorption tests. Results indicated that oil leached out of all the sorbents tested. Polyester fiber released the highest amount of oil, approximately 4% (mass basis) of the oil sorbed.     

Effects of Sorbent Injection on Participate Properties: Part I. Low-Temperature Sorbent Injection

Abstract

This article is the first of a two-part series dealing with the effects of sorbent injection processes on particulate properties. Part I reviews the effects on particulate properties of low-temperature sorbent injection processes (those processes that treat flue gas at temperatures near 300 °F). Part II reviews the effects on particulate properties of high-temperature sorbent injection processes (those processes that involve sorbent injection into the combustion or economizer sections of a boiler). In this article, we review what is currently known about the effects of the low-temperature sorbent injection processes on electrical resistivity, particulate mass loading, particulate size distribution, particulate morphology and cohesivity.

Mixtures of ash and sorbent produced by low-temperature sorbent injection processes are typically less cohesive than most types of fly ash. At temperatures within 30 °F of the water dew point, the combination of low cohesivity and low electrical resistivity of the ash and sorbent mixtures can cause electrical reentrainment in electrostatic precipitators. Deliquescent additives such as calcium chloride cause the water to be retained on the particle surface, thereby increasing cohesivity.

Sorbent injection has been reported to increase the particulate mass loading by a factor of 1.8 to 10, depending upon the reagent ratio and the coal sulfur content. Conventional and in-duct spray drying processes tend to shift the particle size distribution toward larger particles, while dry injection processes tend to shift the particle size distribution toward smaller particles.     

Efficiency of recycled wool-based nonwoven material for the removal of oils from water

The aim of this study was to highlight the potential use of recycled wool-based nonwoven material for the removal of diesel fuel, crude, base, vegetable and motor oil from water. Sorption capacity of the material in water and in oil without water, oil retention, sorbent reusability and buoyancy in static and dynamic conditions were investigated. The results show high sorption capacity of recycled wool for different kinds of oil. This sorbent also exhibited excellent buoyancy after 24h of sorption as well as a good reusability since the decrease in sorption capacity did not exceed 50% of the initial value after five sorption cycles in oil without water.     

Optimizing the specific surface area of fly ash-based sorbents for flue gas desulfurization

High performance sorbents for flue gas desulfurization can be synthesized by hydration of coal fly ash, calcium sulfate, and calcium oxide. In general, higher desulfurization activity correlates with higher sorbent surface area. Consequently, a major aim in sorbent synthesis is to maximize the sorbent surface area by optimizing the hydration conditions. This work presents an integrated modeling and optimization approach to sorbent synthesis based on statistical experimental design and two artificial intelligence techniques: neural network and genetic algorithm. In the first step of the approach, the main and interactive effects of three hydration variables on sorbent surface area were evaluated using a full factorial design. The hydration variables of interest to this study were hydration time, amount of coal fly ash, and amount of calcium sulfate and the levels investigated were 4-32 h, 5-15 g, and 0-12 g, respectively. In the second step, a neural network was used to model the relationship between the three hydration variables and the sorbent surface area. A genetic algorithm was used in the last step to optimize the input space of the resulting neural network model. According to this integrated modeling and optimization approach, an optimum sorbent surface area of 62.2m(2)g(-1) could be obtained by mixing 13.1g of coal fly ash and 5.5 g of calcium sulfate in a hydration process containing 100ml of water and 5 g of calcium oxide for a fixed hydration time of 10 h.