Combining Ion‐exchange (IX) technology and biological reduction for perchlorate removal

Ion‐exchange (IX) resin is perhaps the most promising technology to remove the contaminant perchlorate (ClO₄^?) from waters. However, ion exchange is only a separation technology that transfers the perchlorate from waters to the waste solutions used to regenerate the resins. The waste solutions contain high perchlorate concentrations, and treatment technologies for these regenerant solutions are needed. In this article, we review the latest knowledge on perchlorate removal by ion‐exchange resins; propose three systems that combine ion‐exchange resins (for perchlorate removal) and biological reduction for treating the waste solutions resulting from resin regeneration; and discuss the challenges and research needed to fully develop the proposed technology. © 2002 Wiley Periodicals, Inc.     

离子交换树脂法处理含铜废水的研究进展

介绍了离子交换树脂在处理不同类型的含铜废水中的应用,列举了络合铜废水、游离铜废水及多金属杂质含铜废水中适用的树脂种类及应用实例,对工业应用中存在的一些问题和对策做出总结归纳,并针对该技术的发展方向提出展望。离子交换树脂法是一种较为有效的废水处理方法,对常规浓度和低浓度的含铜废水的处理效果均较好,可将废水有效资源化利用。     

用弱碱性离子交换树脂分离2-萘磺酸的研究

介绍了采用弱碱性离子交换树脂回收2－萘磺酸废水中的2－萘磺酸的试验研究。进行了pH、交换温度、共存阴离子等影响因素的条件试验及树脂再生试验,在较佳条件下,2－萘磺酸交换吸附率达98％以上,洗脱率接近100％。     

树脂吸附法处理对硝基苯乙酮生产废水

采用AM-1吸附树脂和ND-900络合树脂对硝基苯乙酮生产废水进行吸附处理，试验结果表明，使用2种树脂串联的处理效果优于单独使用某一种树脂，而且ND-900络合树脂在前，AM-1吸附树脂在后串联处理的效果最好，废水体积为30BV时，COD去除率为92.8%；脱色率为100%，出水由原废水的橙红色变为无色，采用质量分数为8%的NaOH溶液作为脱附剂，脱附效果良好。     

火电厂离子交换树脂再生废水处理及减排

针对火电厂离子交换树脂再生废水中和处理过程中遇到的问题,探讨影响中和处理的因素,并提出减少火电厂离子交换树脂再生废水排放的措施.     

Ion exchange resin for PFAS removal and pilot test comparison to GAC

Amec Foster Wheeler and Emerging Compounds Treatment Technologies, Inc. tested pilot‐scale ex situ treatment technologies for treatment of poly‐ and perfluorinated alkyl substances (PFAS) in groundwater. The pilot test compared ion exchange resin to granular activated carbon (GAC) and evaluated in‐place regeneration of the resin to restore PFAS removal capacity. During the pilot test, both resin and GAC removed perfluorooctane sulfonate (PFOS) and perfluorooctanoic acid (PFOA) below U.S. Environmental Protection Agency (USEPA) health advisories (HAs) of 0.070 micrograms per liter (μg/L) combined. Compared at a common empty bed contact time (EBCT) of five minutes, the resin treated over eight times as many bed volumes (BVs) of groundwater as GAC before PFOS exceeded the USEPA HA and six times as many BVs for PFOA. On a mass‐to‐mass basis, resin removed over four times as much total PFAS per gram as GAC before breakthrough was observed at the USEPA HA. A solution of organic solvent and brine was used to regenerate the resin in the lead vessel, which had treated water up to the point of PFOS and PFOA breakthrough exceeding the USEPA HAs. The pilot test demonstrated successful in‐place regeneration of the resin to near‐virgin conditions. The regenerated resin was then used to treat the contaminated groundwater up to the same breakthrough point. Compared to the virgin resin loading cycles, PFAS removal results for the regenerated resin were consistent with virgin resin.     

Preparation of Cationic/Anionic Chitin Nanofiber Composite Materials

In this study, we investigated the preparation of cationic/anionic chitin nanofiber (CNF) composite materials by electrostatic interaction. An aqueous dispersion of amidinium CNF was prepared by a top-down approach, and a maleylated CNF film was obtained by a bottom-up approach from a chitin ion gel in an ionic liquid with subsequent maleylation on the CNFs. The resulting film was dispersed in ammonia (aq), which was then mixed with the aqueous cationic CNF dispersion to give the composite film. The composition of the two CNFs was evaluated by scanning electron microscopy and X-ray diffraction measurements. Tensile testing results indicated that the mechanical properties of the composites were enhanced with increasing degrees of substitution of the cationic and anionic groups on CNFs, and also when the molar ratio of these groups approached 1:1. The dissociation of the two kinds of CNFs by alkaline treatment of the composite film was achieved, suggesting the presence of an electrostatic interaction among the interactions between them.     

催化剂生产废水铵离子选择交换处理工艺

用铵离子选择交换工艺对催化剂生产过程排出的含氨氮废水进行处理。考察了再生液中NH3－N浓度、进水NH3－N浓度、进水悬浮物浓度、进水pH、再生液用量等因素对处理效果的影响；探讨了铵离子选择交换床液体空速与出水NH3－N浓度的关系、铵离子交换床总交换容量与进水NH3－N负荷之比与出水NH3－N浓度的关系。     

Treatment of Perchlorate‐Contaminated Groundwater Using Highly Selective,Regenerable Ion‐Exchange Technology: A Pilot‐Scale Demonstration

Treatment of perchlorate‐contaminated groundwater using highly selective, regenerable ion‐exchange technology has been recently demonstrated at Edwards Air Force Base, California. At an influent concentration of about 450 μg/l ClO₄^?, the bifunctional anion‐exchange resin bed treated approximately 40,000 empty bed volumes of groundwater before a significant breakthrough of ClO₄^? occurred. The presence of relatively high concentrations of chloride and sulfate in site groundwater did not appear to affect the ability of the bifunctional resin to remove ClO₄^?. The spent resin bed was successfully regenerated using the FeCl₃^?HCl regeneration technique recently developed at the Oak Ridge National Laboratory, and nearly 100 percent of sorbed ClO₄^? was displaced or recovered after elution with as little as about two bed volumes of the regenerant solution. In addition, a new methodology was developed to completely destroy ClO₄^? in the FeCl₃^?HCl solution so that the disposal of perchlorate‐containing hazardous wastes could be eliminated. It is therefore anticipated that these treatment and regeneration technologies may offer an efficient and cost‐effective means to remove ClO₄^? from contaminated groundwater with significantly reduced generation of waste requiring disposal. © 2002 Wiley Periodicals, Inc.     

化学镀镍废液的处理及再生技术研究进展

介绍了化学镀镍废液的产生和危害,综述了近年来国内外采用化学沉淀法、电解法、氧化还原法、萃取法、离子交换法、电渗析法等对化学镀镍废液进行处理及净化再生的技术研究进展,对各种方法的实用性进行了评价,并指出今后的发展方向。     

乙烯废碱液的再生

开发了除油-苛化-脱硫组合技术处理乙烯废碱液工艺,考察了影响各级处理效果的主要因素.实验结果表明:经石英砂-聚丙烯腈纤维膜-强碱性阴离子交换树脂组合装置除油后,碱液中油类物质质量浓度小于2 mg/L,NaOH,Na_2CO_3,Na_2S等无机组分含量基本不变;经苛化-脱硫处理后碱液中Na_2CO_3和Na_2S质量浓度分别小于4 430 mg/L和4 480 mg/L;再生碱液的流体力学性质及对酸性气体的吸收性能均可满足乙烯裂解气碱洗要求.     

Decomposition reactions of epoxy resin and polyetheretherketone resin in sub- and supercritical water

Epoxy resin and polyetheretherketone (PEEK) resin were decomposed into their monomers such as phenol, cresols, and their analogues by thermal treatment in sub- and supercritical water in a 10-ml tubing bomb reactor. The addition of basic compounds such as Na₂CO₃ was effective in promoting the decomposition reaction of the resins. In the reaction of epoxy resin, the yield of identified products reached 10% for the reaction at 703K over 1h. In the reaction of PEEK resin, the total yield of phenol and dibenzofuran reached 88% for the reaction at 703K over 3h. Chemical participation of water in the decomposition reaction was confirmed by the reaction of dinaphthylether.     

大孔树脂NKA-II对双酚A的吸附性能

研究了大孔树脂NKA-II对双酚A（BPA）的吸附性能,考察了吸附过程的动力学、热力学及树脂的再生性能。BPA溶液呈弱酸性,不需调节pH可直接进行吸附。BPA在大孔树脂NKA-II上的吸附过程可用准二级动力学方程很好地描述。树脂对BPA的吸附是吸热反应,符合Freundlich等温吸附方程,吸附过程属于可自发进行的物理吸附。BPA的吸附过程中同时存在着溶剂的解吸。大孔树脂NKA-II具有良好的重复使用性能,新树脂的平衡吸附量为10.44 mg/g,再生20次后平衡吸附量仍为10.43 mg/g。     

A Cost Comparison of Organic versus Inorganic Ion Exchange Resin for Remediation of High-Level Waste

Ion exchange (IX) can be used to aid in the remediation of underground storage tank (UST) radioactive waste at the U.S. Department of Energy's Hanford site in the state of Washington. In particular, IX can be used to concentrate the radionuclides in liquid-based waste prior to immobilization for final disposal. Concentration of the radionuclides can significantly reduce the final immobilized high-level waste volume and consequent overall remediation cost. Organic and inorganic IX resins each have unique advantages and disadvantages regarding the remediation process. This study presents a comparison of the remediation cost for UST waste at Hanford for a phenol-formaldehyde type organic resin versus crystalline silico-titanate inorganic resin. It was determined that with optimum processing conditions such as waste blending and sludge washing, remediation with the inorganic resin would be less expensive than the organic resin. Assuming baseline remediation conditions, the use of inorganic rather than organic IX resin for UST remediation at Hanford can save approximately $383 million. A limited sensitivity analysis was performed as pan of this study and is reported in the following. © 1999 John Wiley & Sons, Inc.     

The use of volcanic soil as mineral landfill liner--I. Physicochemical characterization and comparison with zeolites.

The main physicochemical characteristics of the volcanic soil of Southern Chile, with allophane as the main pedogenic mineral phase were analysed and compared with common zeolites (clinoptilolite) of the European market. The ultimate goal of this study was to test volcanic soil for the use as mineral landfill liner. The main results indicated that the clay and silt fractions together of the volcanic soil were between 38 and 54%. The buffering capacity of the volcanic soil was higher compared with the studied zeolites, whereas the cationic exchange capacity of the volcanic soil (between 5.2 and 6.5 cmol + kg(-1)) is of the same order of magnitude of the studied zeolites (between 9.7 and 11.4 cmol + kg(-1)). Moreover, the anionic exchange capacity of the volcanic soil was higher compared to the zeolites analysed. The hydraulic conductivity of the volcanic soil, measured in the laboratory at maximum proctor density, ranges between 5.16 x 10(-9) and 6.48 x 10(-9) m s(-1), a range that is comparable to the value of 4.51 x 10(-9) m s(-1) of the studied zeolite. The Proctor densities of the volcanic soil are in a lower range (between 1.11 and 1.15 g ml(-1)) compared with zeolites (between 1.19 and 1.34 g ml(-1)). The volcanic soil physicochemical characteristics are comparable to all the requirements established in the Austrian landfill directive (DVO, 2000). Therefore, the use as mineral landfill basal sealing of the analysed volcanic soil appears reasonable, having a pollutant adsorption capacity comparable to zeolites. It is of special interest for Southern Chile, because there are no alternative mineral raw materials for basal liners of landfills.     

芳香烃清洁硝化催化剂

综述了国内外有关芳香烃硝化过程中替代硫酸的催化剂的研究进展;介绍了沸石类催化剂、粘土类催化剂、离子交换树脂催化剂、固载化液体酸催化剂、金属氧化物及金属盐催化剂、杂多酸催化剂以及固体超强酸催化剂的合成及催化效率与优缺点.     

催化裂化钠碱脱硫液中钙镁离子的去除

研究了化学沉淀法和氨基膦酸型螯合树脂吸附法对催化裂化钠碱脱硫液中Ca~(2+)和Mg~(2+)的去除效果。实验结果表明:NaOH沉淀法可有效去除钠碱脱硫液中的Mg~(2+),当溶液pH为12、反应时间为15 min时,Mg~(2+)去除率达91.6%;NaOH-Na_2CO_3联合沉淀法无法去除钠碱脱硫液中的Ca~(2+);经过NaOH溶液有效除Mg~(2+)后的脱硫液再采用氨基膦酸型螯合树脂吸附柱去除其中的Ca~(2+)和Mg~(2+),可使出水硬度小于2 mg/L。提高进水pH、降低进水流量、降低进水硬度均可提高单位体积树脂的处理水量。     

废弃线路板热解油合成改性酚醛树脂

以废弃线路板热解油为原料,采用碱溶—中和—萃取工艺提取其中以苯酚为主的粗酚,并合成改性酚醛树脂。合成硼酸改性酚醛树脂的优化工艺条件为n(粗酚)∶n(外加苯酚)=2∶3,n(粗酚+外加苯酚)∶n(甲醛)∶n(NaOH)∶n(硼酸)=1∶1.5∶0.15∶0.17;合成有机硅改性酚醛树脂的优化工艺条件为n(粗酚)∶n(外加苯酚)=2∶3,n(粗酚+外加苯酚)∶n(甲醛)∶n(NaOH)∶n(正硅酸乙酯)=1∶1.3∶0.1∶0.1。所合成的硼酸改性和有机硅改性酚醛树脂的主要性能指标均满足YB/T4131—2005《耐火材料用酚醛树脂》中牌号为PFn-5301的热固性液体树脂性能的要求。     

微生物法处理含铬(Ⅵ)废水的研究

采用硫酸盐还原菌处理含铬(Ⅵ)废水，研究了其去除铬(Ⅵ)的最适宜工艺条件。实验表明，该菌的适用范围广，处理含铬废水的能力强。在菌液与废液体积比为1．0：1、铬(Ⅵ)质量浓度为150mg／L条件下处理36h，铬(Ⅵ)去除率达99．9％。     

强碱性阴离子交换树脂对苦味酸的吸附与解吸性能

研究了强碱性阴离子交换树脂(简称树脂)对苦味酸的吸附与解吸性能,探讨了吸附的热力学和动力学特性以及吸附机理.实验结果表明:树脂对苦味酸的吸附量随吸附温度升高而增大;溶液pH为2.7 ～12.0时树脂的苦味酸吸附量最大,稳定在120 mg/g以上;树脂对苦味酸的等温吸附规律符合Freundlich模型,相关系数大于0.9...