929 resultados para GRANULAR ACTIVATED CARBON


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A new two-step synthesis of ZrO2-MCM nanocomposites using the gel combustion technique was accomplished; the resulting material had a high-surface area and showed very high adsorption activity. The deposition of 25 nm ZrO2 particles over MCM was achieved using gel combustion technique with glycine as a fuel, and the formation of nanocomposites was confirmed using transmission electron microscopy. The composites were also characterized by XRD, SEM, FTIR and N2 adsorption-desorption analysis. The nanocomposites were tested for the adsorption of cationic dyes. High rates of adsorption and large dye uptake were observed over the nanocomposites. The rate of adsorption over the nanocomposites was higher than that observed for physical ZrO2-MCM mixtures and commercial activated carbon. The nanocomposite with 10 wt % ZrO2 showed the highest rate of adsorption owing to the synergistic effects of ZrO2 surface groups, smaller particle size, fine dispersion and high-surface area of the composite. (c) 2012 American Institute of Chemical Engineers AIChE J, 58: 29872996, 2012

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The knowledge of adsorption characteristics of activated carbon (porous material) in the temperature range from 5 to 20 K is essential when used in cryosorption pumps for nuclear fusion applications. However, such experimental data are very scarce in the literature, especially below 77 K. So, an experimental system is designed and fabricated to measure the adsorption characteristics of porous materials under variable cryogenic temperatures (from 5 K to 100 K). This is based on the commercially available micropore-analyser coupled to a closed helium cycle two-stage Gifford McMahon (GM) Cryocooler, which allows the sample to be cooled to 4.2 K. The sample port is coupled to the Cryocooler through a heat switch, which isolates this port from the cold head of the Cryocooler. By this, the sample temperature can now be varied without affecting the Cryocooler. The setup enables adsorption studies in the pressure range from atmospheric down to 10(-4) Pa. The paper describes the details of the experimental setup and presents the results of adsorption studies at 77 K for activated carbon with nitrogen as adsorbate. The system integration is now completed to enable adsorption studies at 4.2 K.

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We demonstrate observation of Raman signals of different analytes adsorbed on carbonaceous materials, such as, chemically reduced graphene, graphene oxide (GO), multi-walled carbon nanotube (MWCNT), graphite and activated carbon. The analytes selected for the study were Rhodamine 6G (R6G) (in resonant conditions), Rhodamine B (RB), Nile blue (NBA), Crystal Violet (CV) and acetaminophen (paracetamol). All the analytes except paracetamol absorb and fluoresce in the visible region. In this article we provide experimental evidence of the fact that observation of Raman signals of analytes on such carbonaceous materials are more due to resonance effect, suppression of fluorescence and efficient adsorption and that this property in not unique to graphene or nanotubes but prevalent for various type of carbon materials.

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For the purpose of water purification, novel and low-cost adsorbents which are promising replacements for activated carbon are being actively pursued. However, a single-phase material that adsorbs both cationic and anionic species remains elusive. Hence, a low-cost, multiphase adsorbent bed that purifies water containing both anionic and cationic pollutants is a desirable alternative. We choose anionic (Congo red, Orange G) and cationic (methylene blue, malachite green) dyes as model pollutants. These dyes are chosen since they are widely found in effluents from textile, leather, fishery, and pharmaceutical industries, and their carcinogenic, mutagenic, genotoxic, and cytotoxic impact on mammalian cells is well-established. We show that ZnO, (Zn0.24Cu0.76)O and cobalt ferrite based multiphase fixed adsorbent bed efficiently adsorbs model anionic (Congo red, Orange G) and cationic (methylene blue and malachite green) pollutants, and their complex mixtures. All adsorbent phases are synthesized using room-temperature, high-yield (similar to 96-100%), green chemical processes. The nanoadsorbents are characterized by using X-ray powder diffraction (XRD), scanning electron microscopy (SEM), Brunauer-Emmett-Teller (BET) surface area analysis, and zeta potential measurements. The constituent nanophases are deliberately chosen to be beyond 50 nm, in order to avoid the nanotoxic size regime of oxides. Adsorption characteristics of each of the phases are examined. Isotherm based analysis shows that adsorption is both spontaneous and highly favorable. zeta potential measurements indicate that electrostatic interactions are the primary driving force for the observed adsorption behavior. The isotherms obtained are best described using a composite Langmuir-Freundlich model. Pseudo-first-order, rapid kinetics is observed (with adsorption rate constants as high as 0.1-0.2 min(-1) in some cases). Film diffusion is shown to be the primary mechanism of adsorption.

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Polyaniline and graphene oxide composite on activated carbon cum reduced graphene oxide-supported supercapacitor electrodes are fabricated and electrochemically characterized in a three-electrode cell assembly. Attractive supercapacitor performance, namely high-power capability and cycling stability for graphene oxide/polyaniline composite, is observed owing to the layered and porous-polymeric-structured electrodes. Based on the materials characterization data in a three-electrode cell assembly, 1 V supercapacitor devices are developed and performance tested. A comparative study has also been conducted for polyaniline and graphene oxide/polyaniline composite-based 1 V supercapacitors for comprehending the synergic effect of graphene oxide and polyaniline. Graphene oxide/polyaniline composite-based capacitor that exhibits about 100 F g(-1) specific capacitance with faradaic efficiency in excess of 90% has its energy and power density values of 14 Wh kg(-1) and 72 kW kg(-1), respectively. Cycle-life data for over 1000 cycles reflect 10% capacitance degradation for graphene oxide/polyaniline composite supercapacitor.

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Tastes and odours are amongst the few water quality standards immediately apparent to a consumer and, as a result, account for most consumer complaints about water quality. Although taste and odour problems can arise from a great many sources, from an operational point of view they are either ”predictable” or ”unpredictable”. The former - which include problems related to actinomycete and algal growth - have a tendency to occur in certain types of water under certain combinations of conditions, whereas the latter - typically chemical spills - can occur anywhere. Long-term control is one option for predictable problems, although biomanipulation on a large scale has had utile success. Detection and avoidance is a more practicable option for both predictable and unpredictable problems, particularly if the distribution network can be serviced from other sources. Where these are not feasible, then water treatment, typically using activated carbon, is possible. In general there is a reasonable understanding of what compounds cause taste and odour problems, and how to treat these. An efficient taste and odour control programme therefore relies ultimately on good management of existing resources. However, a number of problems lie outside the remit of water supply companies and will require more fundamental regulation of activities in the catchment.

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Neste trabalho foi estudado o tratamento simultâneo por biofiltração de emissões de compostos orgânicos voláteis, COV e gás sulfídrico, H2S, em estações de tratamento de despejos industriais, de refinaria de petróleo, ETDI. A biofiltração dos gases emanados da EDTI mostrou ser uma técnica de alta eficiência, atingindo valores de 95 a 99 % para tratamento simultâneo de COV e H2S em concentrações de 1000 e 100 ppmv, respectivamente. Foram realizados testes em 95 dias consecutivos de operação, em uma planta piloto instalada na Superintendência da Industrialização do Xisto, SIX, em São Mateus do Sul, Paraná, de março a agosto de 2006. O biofiltro foi do tipo fluxo ascendente, com 3,77 m3 de leito orgânico, composto de turfa, carvão ativado, lascas de madeira, serragem brita fina além de outros componentes menores. Foi realizada inoculação biológica com lodo filtrado de estação de tratamento de esgoto sanitário. As vazões de gás aplicadas variaram de 85 a 407 m3/h, resultando em taxas de carga de massa de 11,86 a 193,03 g de COV/h.m3 de leito e tempos de residência de 24 segundos a 6,5 minutos, com tempo ótimo de 1,6 minutos. A capacidade máxima de remoção do sistema encontrada, nas condições testadas, foi de 15 g de COV/h. m3, compatível com os valores encontrados na literatura para depuração biológica de COV na escala praticada. Também foi verificada a redução de componentes específicos de BTX, demonstrando boa degradabilidade dos compostos orgânicos. Finalmente o biofiltro demonstrou boa robustez biológica diante dos desvios operacionais intencionalmente provocados, tais como falta de umidade do leito, baixa temperatura, alta vazão, falta de carga de COV e baixo pH do leito. Depois de retomada a condição de operação estável, a biofiltração rapidamente atingiu o estado de equilíbrio, assegurando o uso eficiente e confiável da técnica no tratamento de gases de EDTI na indústria do hidrocarbonetos ou em refinarias de petróleo.

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Apesar da importância das estações de tratamento de efluentes industriais (ETEIs) na conservação dos ecossistemas, estas podem ser geradoras de gases com maus odores contendo compostos orgânicos voláteis - COVs. Os maus odores têm sido motivos de protestos e reclamações por parte da população circunvizinha às fontes emissoras. Em virtude da conscientização ambiental, e dos impactos sobre a saúde do homem, o objetivo geral deste trabalho é avaliar a eficiência de um biorreator aeróbio piloto no controle de gases odoríferos emitidos em estação de tratamento de efluentes de indústrias de alimentos. Foi desenvolvido um sistema de difusão de ar odorífero em um reator aeróbio de lodo ativado, hermeticamente fechado, operado no regime de batelada sequencial, durante os dias 14, 21, 23, e 30 do mês de julho.Foram realizadas análises dos parâmetros físico-químicos do lodo ativado utilizado no reator aeróbio piloto, como determinação dos sólidos, DBO5, DQO, OD, pH, temperatura e IVL. A atividade da biomassa do lodo ativado foi avaliada por meio do teste de Respirometria. A eficiência do reator quanto à redução da DQO dos gases foi analisada por meio da absorção dos gases em solução de dicromato de potássio. Para avaliação da mensuração dos odores utilizou-se o método de cromatografia gasosa e espectrometria de massa, quantificando amostras de gases odorantes adsorvidas em tubos de carvão ativado, na entrada e na saída dobiorreator. Os resultados obtidos confirmaram o potencial do sistema de difusão em lodos ativados para o tratamento de gases odoríferos em ETEI, com eficiência de remoção dos COV`s variando de 97,3% a 98,9%.

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A study was undertaken examining the effect of malachite green on the development and survival of the zoeae, mysis and post-larvae of Penaeus monodon. Sensitivity varied with the different larval stages; the zoeae appeared to be the least tolerant. The prophylactic potentials of malachite green in the control of Lagenidiumand Zoothamnium infesting P. monodon larvae are considered briefly. Toxicity risks may be reduced by application between ecdyses or by the removal of the dye by filtration through activated carbon.

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砷是毒性最强的元素之一,水体中砷的污染己经引起人们广泛的关注。我国的新疆、内蒙、山西和台湾等省和地区地下水砷含量严重超标。全球共有5,000多万人遭受高砷饮用水的威胁,其中中国有1,500多万,是饮用水砷污染最严重的国家之一。WHO推荐饮用水砷的最高允许浓度从原来的50 µg•L-1已降至10 µg•L-1。更为严格的砷卫生标准的颁布,对作为饮用水源的地下水中的砷去除工艺提出了更高的要求。吸附法除砷比膜法、混凝法和离子交换法更安全、简便,是砷去除工艺中最有效的方法之一。 首先,本研究通过优化制备条件(包括炭种类的选择、炭的粒径大小、还原剂的浓度及滴定速率、反应温度、铁盐的种类及浓度、分散剂的比例及浓度),制备了负载型纳米铁。考虑到砷的去除效率、工程应用的可行性以及经济性,最优的制备条件如下:选用粒径为20~40目煤质炭,在室温、一定的分散剂比例及浓度,0.2 M KBH4滴速为20 d•min-1时所制备的Fe/炭为82.0 mg•g-1;纳米铁在活性炭孔内呈针状,其直径为30~500 nm,长度为1,000~2,000 nm。绝大多数的铁都负载到活性炭内部,这在处理水时铁不流失很重要。 其次,利用制备的负载型纳米铁作吸附载体,进行了饮用水中As(Ⅴ)的吸附去除实验。研究了该吸附剂对As(Ⅴ)的吸附等温线、动力学以及影响动力学的各种因素(包括As(Ⅴ)的不同初始浓度、吸附剂用量、pH值、共存离子和不同温度)、pH值、共存离子等环境条件对As(Ⅴ)去除的影响;以及吸附剂的再生及再生后的吸附效率等。研究发现在前12 h内吸附较快,72 h时达到了平衡。用Langmuir 吸附等温式估算出As(Ⅴ)的吸附量为12.0 mg•g-1。该吸附剂在pH 6.5, (25±2)℃, As(Ⅴ)初始浓度为2 mg•L-1,吸附剂用量为1.0 g•L-1时,As(Ⅴ)的去除率为75.2%;当把吸附剂的用量增加到1.5 g•L-1时,As(Ⅴ)的去除率可达99.9%以上。吸附剂可以用0.1M的NaOH浸泡12 h后即可再生,再生效率较高。常见的阴离子中PO43-、SiO32-对As(Ⅲ)的去除抑制较大,而SO42-、CO32-、C2O42-等离子对砷的去除影响较小。Fe2+对As(Ⅲ)的吸附抑制作用较大而其它阳离子影响不大。吸附剂可用0.1 M NaOH 有效再生,并且具有良好的机械性能。实验室初步实验数据表明,该吸附剂对饮用水除砷具有较好的应用前景。 第三,利用实验室制备的负载型纳米铁对饮用水中As(Ⅲ)的吸附去除也进行了研究。考察了吸附等温线、动力学以及影响动力学的各种因素、pH值、共存离子等环境条件对As(Ⅲ)去除的影响;以及吸附剂的再生及再生后的吸附效率等。研究发现,该吸附剂在pH 6.5, (25±2)℃, As(Ⅲ)初始浓度为2 mg•L-1,吸附剂用量为1.0 g•L-1时, 对As(Ⅲ)的去除率为99.8%;其吸附容量为1.996mg•g-1。吸附过程中部分As(Ⅲ)被氧化。与As(Ⅴ)的吸附相比,该吸附剂对As(Ⅲ)的效率比较高-而常见的其它除砷吸附剂如载铁纤维棉等,对As(Ⅴ)的效率比As(Ⅲ)高,为有效去除As(Ⅲ),常常需要专门加上氧化这一过程。 最后,利用负载型纳米铁对饮用水中As(Ⅲ) 的氧化性能进行考察,发现该吸附剂不但能够有效吸附去除饮用水中的砷,而且还能把As(Ⅲ)有效地氧化为As(Ⅴ)。经过对吸附剂的构成组分分析发现,活性炭表面因富含多种官能团而对三价砷的氧化作用最大;其次是纳米铁也能把As(Ⅲ)氧化为As(Ⅴ)。

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除草剂阿特拉津的大量生产和广泛使用形成了对饮用水源的严重污染,目前在世界范围内的地表水和地下水中均检出一定浓度的阿特拉津,这对人类健康构成严重威胁。本文研究了采用纳滤技术和生物活性炭技术去除微污染原水中阿特拉津的可行性,对上述两种技术的去除效率、作用机理和影响因素进行了研究,并探讨了它们在未来饮用水深度处理中的优势和不足。本论文获得了以下一些具有重要意义的研究结果:(1)除天然有机物外,原水中无机离子在膜表面或孔径内吸附,引起膜有效孔径减小,使纳滤膜对农药截留率提高并降低水通量;在所研究的两个系列四种纳滤膜中,UTC-20截留阿特拉津达90%,截留其他有机物>95%,对硝酸盐截留率>70%,是迄今报道的对硝酸盐去除效率最高的纳滤膜,适于去除原水中阿特拉津和硝酸盐的双重污染;由于水合作用,纳滤膜对分子量相似有机物的截留率与有机物的油水分配系数(LogP)呈显著线性负相关,这一研究结果丰富了对有机物疏水性影响纳滤膜截留性能的认识。(2)筛选到一株能够以阿特拉津为惟一碳源生长的菌株-SYSA,经生理生化特性鉴定和1 6SrRNA基因序列分析,该菌为阴沟肠杆菌(Enterobacter cloacae)。这是首次报道肠杆菌属微生物可降解阿特拉津。对SYSA菌的生物学特性研究表明,SYSA菌可耐”受阿特拉津浓度100mg/L;pH7-8,30℃时,在以阿特拉津(20mg/L)惟一碳源的培养基上经146h培养,降解率为87%,该菌代时为2.gld,生长速率为(R)0.344dsel。(3)将SYsA菌接入活性炭柱,形成生物活性炭去除水中微量阿特拉津。研究结果表明空床接触时间为40min、温度为16℃±4℃、溶解氧为4.3-4.6mg/L时,120天后未接菌对照柱去除率下降至30%,而降解菌柱的去除效率却仍保持在65%~75%,延长了炭的使用时间。DGGE图谱表明未接菌对照柱、土壤悬液柱和降解菌柱上均有自来水中的微生物,但降解菌柱上还是以SYSA菌为优势菌。上述研究结果为纳滤或生物活性炭技术用于处理微污染原水、井直接生产饮用水提供了科学依据。

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