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The coagulation properties of some mixtures of 5% chitosan in 2% aqueous acetic acid were investigated with the goal of determining the optimal coagulation conditions for the spinning of chitosan fibers. The chitosan was characterized and found to possess a deacetylation value of 84.9 ± 0.2%. Molecular weight of the chitosan was also measured; based on intrinsic viscosity, the Mv value was 7.73 × 105 g mol−1, and based on high-pressure liquid chromatography, the Mw value was 1.14 × 105 g mol−1. Solutions of 5% chitosan/2% acetic acid were prepared, filtered, and extruded through a large-diameter hole syringe into coagulation baths of varying composition that were all strongly basic in nature, at least a pH of 12 or greater. For each coagulant, time was varied from between 22 s and 2 minutes at room temperature. A second set of experiments was conducted where the temperature was varied from 20°C to 70°C at a constant time of 45 s. In a third set of experiments, using a 1M NaOH coagulant, different chitosans were also analyzed. Throughout all of the experiments, a distinct moving boundary between coagulated and uncoagulated polymer was observed within the cylindrical-shaped polymer fibers. Using a series of equations based on Fick's 2nd Law, a straight line relationship has been demonstrated between boundary motion and time and between boundary motion and temperature for each coagulant tested. The activation energy for each coagulant was also determined. © 1997 John Wiley & Sons, Inc. J Appl Polym Sci 66: 117–127, 1997 相似文献
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Nely Rios‐Donato Ricardo Navarro Mario Avila‐Rodriguez Eduardo Mendizábal 《应用聚合物科学杂志》2012,123(4):2003-2010
This article reports on the removal of colloidal suspensions of kaolinite, bentonite, and alumina using chitosan sulfate (ChS). ChS was synthesized by partial introduction of sulfate groups in the chitosan (Ch) structure. The polyampholyte (chitosan sulfate) shows variable charge depending on the pH of the solution. ChS was characterized by FTIR, 13C‐NMR, elemental analysis, and potentiometric titrations. The ChS coagulation–flocculation capacity for kaolinite, bentonite, and alumina aqueous suspensions was systematically studied. The coagulation–flocculation process was carried out at various pH values and ChS concentrations. The pH range in which the largest ChS removal capacity was observed depended on particle type (4.5–5.5 for kaolinite, 4.5–7.0 for bentonite, and 7.0–8.0 for alumina). The removal of colloidal particles is explained by charge neutralization due to electrostatic interactions between ChS and particles and particle entrapping when the polyelectrolyte precipitates. © 2011 Wiley Periodicals, Inc. J Appl Polym Sci, 2012 相似文献
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混凝-吸附联合处理含铬废水的研究 总被引:1,自引:0,他引:1
采用新型混凝剂聚磷氯化铝铁(PPAFC)对含铬废水进行混凝处理;再采用铝化改性膨润土对含铬废水进行吸附处理。结果表明:在PPAFC 40mg/L,铝化改性膨润土2.0g/L,室温的条件下,总铬的去除率超过99.8%,出水中总铬的质量浓度达到《电镀污染物排放标准》(GB 21900-2008)要求。 相似文献
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Collin Knox Coleman Eric Mai Megan Miller Shalini Sharma Clark Williamson Hemali Oza Eleanor Holmes Marie Lamer Christopher Ly Jill Stewart Mark D. Sobsey Lydia S. Abebe 《International journal of molecular sciences》2021,22(18)
Viruses are major contributors to the annual 1.3 million deaths associated with the global burden of diarrheal disease morbidity and mortality. While household-level water treatment technologies reduce diarrheal illness, the majority of filtration technologies are ineffective in removing viruses due to their small size relative to filter pore size. In order to meet the WHO health-based tolerable risk target of 10−6 Disability Adjusted Life Years per person per year, a drinking water filter must achieve a 5 Log10 virus reduction. Ceramic pot water filters manufactured in developing countries typically achieve less than 1 Log10 virus reductions. In order to overcome the shortfall in virus removal efficiency in household water treatment filtration, we (1) evaluated the capacity of chitosan acetate and chitosan lactate, as a cationic coagulant pretreatment combined with ceramic water filtration to remove lab cultured and sewage derived viruses and bacteria in drinking waters, (2) optimized treatment conditions in waters of varying quality and (3) evaluated long-term continuous treatment over a 10-week experiment in surface waters. For each test condition, bacteria and virus concentrations were enumerated by culture methods for influent, controls, and treated effluent after chitosan pretreatment and ceramic water filtration. A > 5 Log10 reduction was achieved in treated effluent for E.coli, C. perfringens, sewage derived E. coli and total coliforms, MS2 coliphage, Qβ coliphage, ΦX174 coliphage, and sewage derived F+ and somatic coliphages. 相似文献
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壳聚糖对银杏叶水提液的絮凝工艺研究 总被引:6,自引:0,他引:6
采用天然高分子絮凝剂壳聚糖对银杏叶水提液进行絮凝提取,其目的是优化生产工艺,提高药液的澄清度和药液质量。实验利用光的吸收和散射定律,以絮凝率和总黄酮损失率为衡量指标,判断不同影响因素对絮凝效果的影响,并将其与醇沉工艺的提取方法进行比较。结果通过单因素实验先判断出有利于絮凝的趋势,之后又利用正交实验确定了絮凝的最佳工艺条件:絮凝剂质量浓度1.071 g/L,絮凝温度40℃,体系pH值4.9。并且得出壳聚糖对银杏叶水提液的絮凝工艺效果明显优于醇沉法。 相似文献
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以煤化工废水的总酚、COD、氨氮和浊度为评价指标,通过单因素试验分别考察了Fenton试剂、Fenton试剂联合聚合硫酸铝铁(PAFC)、Fenton试剂联合PAFC与阳离子型聚丙烯酰胺(CPAM)联合预处理煤化工废水的总体效果,并探究了联合处理方法降解煤化工废水的机制。结果表明,Fenton氧化联合混凝法处理煤化工废水的效果明显最优,废水预处理后的CODCr、NH3-N、总酚和浊度分别由3900、760.7、540 mg/L和28 NTU,降至2950、600.4、359.7 mg/L和5.3 NTU。另外,可生化性(BOD5/CODCr)由原来的0.11提升到0.29。由此可见,Fenton氧化联合混凝法预处理煤化工废水将强氧化性-助凝-絮凝作用有效结合,可以提高水质净化效果,大大降低后续的水处理负荷。 相似文献
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壳聚糖在海水混凝处理过程中的助凝作用研究 总被引:2,自引:0,他引:2
将天然高分子絮凝剂壳聚糖(CTS)与无机絮凝剂FeCl3协同使用,混凝处理渤海湾近岸海水,考察了壳聚糖投加量、pH值和沉降时间对浊度和其它污染物去除效果的影响。试验结果表明,CTS对FeCl3助凝效果显著,与单独使用FeCl3相比,其浊度、化学耗氧量(CODMn)和总磷(TP)去除率分别提高了8.3%、9.6%和9.4%。FeCl3与CTS协同使用还可明显改善絮体的沉降性能,缩短沉淀时间。综合考虑各项主要技术指标,其海水混凝适宜条件为m(FeCl3)/m(CTS)=15.0。 相似文献
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Yun‐Hwei Shen 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2005,80(5):581-586
A novel strategy of sweep coagulation to treat low turbidity water is presented herein. Study findings demonstrated that an Na+‐saturated bentonite with medium cation exchange capacity (CEC) resulted in significant turbidity removal at a bentonite dosage of 30 mg dm?3. Bentonite dispersion with fully delaminated platelets tended to undergo a more porous type of coagulation with intense face‐to‐face interactions of platelets and effectively entrapped TiO2 particles in band‐type structures. This type of coagulation usually results in a large volume of settled flocs with a fluffy structure and excellent turbidity removal efficiency for sweep coagulation. The sign and magnitude of electrical charge on TiO2 particles has a minor effect on the efficiency of sweep coagulation. Copyright © 2005 Society of Chemical Industry 相似文献
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Mikael Larsson Wei-Chen Huang Meng-Hsuan Hsiao Yen-Jen Wang Magnus Nydén Shih-Hwa Chiou Dean-Mo Liu 《Progress in Polymer Science》2013
Chitosan is among the most abundant biopolymers on earth and has been either used or exhibited potential in a wide variety of industrial and biomedical applications. With the advancement of materials technologies, chitosan has been chemically modified to self-assemble into nanoarchitectures that are usable in advanced biomedical applications, such as drug nanocarriers, macroscopic injectables, tissue-engineering scaffolds, and nanoimaging agents. Colloidal amphiphilically modified chitosan (AMC) is a relatively recent material receiving increased attention with numerous publications addressing the medical advantages of specific systems. To date, many reviews have focused on the synthesis and biomedical properties of chitosan-based biomaterials, but a comprehensive study focusing on the colloidal properties of AMC in relation to biomedical performance appears to be lacking. This review provides a survey of the field, critically reviewing the colloidal properties and biomedical performance of AMC systems, such as nanoparticle drug delivery systems and macroscopic medical devices. Finally, the future development, market potential, and clinical implications of these promising colloidal-structured biomaterials are summarised. 相似文献
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Chitosan (an amino‐polysaccharide obtained from deacetylation of chitin, the major constituent of crustaceous shells and insect cuticles) presents a cationic character in acidic media allowing its dissolution, its shaping and possible ion‐exchange interactions with anionic compounds (a property applied in adsorption and coagulation–flocculation processes). In neutral media, non‐protonated amino groups allow complexation of metal cations or organic chemicals. These different properties explain the interest taken by the scientific community in using this biopolymer. In solution it contributes to complex metals and their recovery by complexation‐assisted ultrafiltration. It can also be used to coagulate–flocculate organic compounds (as anionic dyes). In the solid state, it can be used for metal ion adsorption, as well as adsorption of organic compounds (dyes, pesticides, drugs, endocrine disruptors, etc.). The adsorption and coagulation–flocculation processes will be compared and examples considered. Moreover, it is noteworthy that the thermal degradation of this type of material is also more environmentally friendly than that of conventional synthetic resins (production of hazardous by‐products, etc.), a supplementary advantage of these biopolymer‐based sorbents. Combined with its ability to be chemically or physically modified improving the potential and phase separation of chitosan‐based materials, all these properties mean it is an excellent candidate for wastewater treatment. © 2017 Society of Chemical Industry 相似文献
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《分离科学与技术》2012,47(7):999-1007
The objectives are to evaluate the feasibility of treating oily wastewater using synthetic polymers (polyaluminum chloride (PAC), polyferric sulfate (PFS), and polyacrylamide (PAM)) combined with natural diatomite and to refine the operating parameters using diatomite as an adsorbent and a coagulant aid. The enhanced coagulation/flocculation by combining PAC with diatomite was investigated through mechanism analysis compared to the combination of PFS/PAM with diatomite, respectively. The effects of coagulant dose, initial pH, and settling time on chemical oxygen demand (COD) and turbidity were studied using PAC-diatomite in comparison with using PAC only. The enhanced coagulation/flocculation of diatomite with PAC was better than that with PFS/PAM in terms of COD/turbidity removal and floc settling characteristics, considering costs. The PAC-diatomite system reduced more than 70% of COD and 90% of turbidity over a wide pH range (7–10) within 20 min, with the optimum dose of PAC 50 mg/l and diatomite 1250 mg/l. The added diatomite effectively saved over 85% of PAC dose and simultaneously increased over 50% of COD removal efficiency. This study provided a novel and economical approach for diatomite utilization in the treatment of oily wastewater, satisfying the demands of reuse or reinjection into the ground. 相似文献
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Conventional jar tests and on-line size monitoring were used to investigate the effects of slow-mixing intensity and duration on residual turbidity and floc size during charge neutralization coagulation and sweep flocculation with polyaluminum chloride. The compensatory effect of slow-mixing on coagulation performance following inadequate or excessive rapid-mixing was also examined. It is found that slow-mixing intensity has a more marked positive effect on charge neutralization coagulation than on sweep flocculation. The optimal root-mean- square velocity gradient, G, for slow-mixing is 15 s-1 for both coagulation mechanisms, and charge neutralization coagulation requires a longer slow-mixing duration. The optimal slow-mixing duration, based on residual turbidity, is longer than the time to form the largest mean flocs. The optimal product of G and mixing duration, GT, for slow-mixing during charge neutralization coagulation (13500) are higher than that during sweep flocculation (4500) and both are less than the range of values recommended by the American Water Works Association (24000-84000). The optimal GT value under various slow-mixing conditions increases with G. Appropriate extension of slow-mixing duration during charge neutralization coagulation can improve coagulation performance after an inadequate or excessive rapid-mixing duration, but during sweep flocculation, appropriate shortening of slow-mixing duration after an excessive rapid-mixing or appropriate extension of slow-mixing duration after an inadequate rapid-mixing is favorable. 相似文献