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Chitosan is a natural high molecular polymer made from crab, shrimp and lobster shells. When used as coagulant in water treatment, not like aluminum and synthetic polymers, chitosan has no harmful effect on human health, and the disposal of waste from seafood processing industry can also be solved. In this study the wastewater from the system of cleaning in place (CIP) containing high content of fat and protein was coagulated using chitosan, and the fat and the protein can be recycled. Chitosan is a natural material, the sludge cake from the coagulation after dehydrated could be used directly as feed supplement, therefore not only saving the spent on waste disposal but also recycling useful material. The result shows that the optimal result was reached under the condition of pH 7 with the coagulant dosage of 25 mg/l. The analysis of cost-effective shows that no extra cost to use chitosan as coagulant in the wastewater treatment, and it is an expanded application for chitosan. 相似文献
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Seiichi Ishikawa Naoko Ueda Yuji Okumura Yoshikazu Iida Kenzo Baba 《Journal of Material Cycles and Waste Management》2007,9(2):167-172
Spent coagulant in water supply plant sludge was extracted with H2SO4 and the efficiency of the reused coagulant was studied. The optimum pH values for coagulant extraction and clarification
with the reused coagulant were 3.0–4.0 and about 6, respectively. In treating raw influent obtained from a sewage treatment
plant and wastewater from a coastal landfill site, the removal of chemical oxygen demand (COD), total nitrogen, and total
phosphorous with the recovered coagulant was higher than that with commercial aluminum sulfate or polyaluminum chloride. In
addition, the sludge settling properties, the extra sludge mass formation, the supernatant quality, and the cost of reagents
were also studied. The coagulant recovered from water supply plant sludge by H2SO4 extraction could be successfully reused for the clarification of domestic and food industry wastewaters. 相似文献
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Nadia Eladlani El Montassir Dahmane Abdelaaziz Ouahrouch Mohammed Rhazi Moha Taourirte 《Journal of Polymers and the Environment》2018,26(1):152-157
Chitosan, its nanoparticles and whiskers present an excellent capacity to complex chromium ions. However, this phenomenon is influenced by different parameters. In our search, we determined the appropriate range of pH to form chitosan–Cr(III), nanoparticles Cr(III) and whiskers–Cr(III) complex. We studied also the influence of chromium concentration and nature of chitosan-based materials on complexation process. Our main aim is approximate the optimal conditions to remove chromium(III) from tanning bath, recuperated from tannery wastewater of Marrakech in Morocco. However, the results of adsorption kinetic in tannery wastewater revealed that chitosan, its nanoparticles, whiskers and biocomposites are good sorbent of chromium as well, even if the adsorbed quantity is less compared to chromium solution. Although, according to ICP-OES analysis in this real effluent, nanoparticles are the best complexing ligand, after 24 h of contact nanoparticles can remove 70% of chromium from this tannery wastewater. 相似文献
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以拜耳法赤泥为原料、Na Cl为助溶剂,采用酸浸法溶出赤泥中的铁、铝元素,再与硅酸钠、硫酸氧钛反应制备出高效混凝剂含钛聚硅酸铝铁(T-PSAF),并将其用于模拟亚甲基蓝印染废水的脱色。实验结果表明:在硫酸浓度为8 mol/L、液固比(硫酸体积与干赤泥质量之比)为14 m L/g、酸浸温度为80℃、酸浸时间为80 min、Na Cl加入量为0.10 g/g(以干赤泥计)的优化酸浸条件下,铁、铝的浸出率分别为88.25%和73.21%;在n(Fe+Al)∶n(Ti)∶n(Si)=0.3∶0.3∶1、熟化p H为4~5、熟化时间为2 h、混凝剂加入量为25 m L/L的优化混凝条件下,初始亚甲基蓝质量浓度为10 mg/L的废水的脱色率可达87.1%,而当初始亚甲基蓝质量浓度增至150~200 mg/L时废水脱色率可达99%以上。 相似文献
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研究了聚酯化纤废水中有机污染物乙醛、乙酸、乙二醇含量与COD之间的相关性,确定了COD与上述特征污染物含量的比值,并测定了它们的氧化率,为企业的生产工艺管理和 保管理提供了基础数据。 相似文献
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沉淀-电解法回收COD分析废液中的银 总被引:4,自引:0,他引:4
采用沉淀-电解法从COD分析废液中回收银。首先将废液中银沉淀析出,制成高浓度含银电解液,然后以不锈钢作阴、阳极,在极距10mm、电流密度0.28A/dm ̄2条件下进行电解,回收废液中银。该方法操作简便,银回收率为95%以上,纯度达99.5%以上。 相似文献
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Nugraha E. Suyatma Alain Copinet Lan Tighzert Veronique Coma 《Journal of Polymers and the Environment》2004,12(1):1-6
Biodegradable film blends of chitosan with poly(lactic acid) (PLA) were prepared by solution mixing and film casting. The main goal of these blends is to improve the water vapor barrier of chitosan by blending it with a hydrophobic biodegradable polymer from renewable resources. Mechanical properties of obtained films were assessed by tensile test. Thermal properties, water barrier properties, and water sensitivity were studied by differential scanning calorimeter analysis, water vapor permeability measurements, and surface-angle contact tests, respectively. The incorporation of PLA to chitosan improved the water barrier properties and decreased the water sensitivity of chitosan film. However, the tensile strength and elastic modulus of chitosan decreased with the addition of PLA. Mechanical and thermal properties revealed that chitosan and PLA blends are incompatible, consistent with the results of Fourier transform infrared (FTIR) analysis that showed the absence of specific interaction between chitosan and PLA. 相似文献
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Organic and nitrogen removal from landfill leachate in aerobic granular sludge sequencing batch reactors 总被引:1,自引:0,他引:1
Granule sequencing batch reactors (GSBR) were established for landfill leachate treatment, and the COD removal was analyzed kinetically using a modified model. Results showed that COD removal rate decreased as influent ammonium concentration increasing. Characteristics of nitrogen removal at different influent ammonium levels were also studied. When the ammonium concentration in the landfill leachate was 366 mg L−1, the dominant nitrogen removal process in the GSBR was simultaneous nitrification and denitrification (SND). Under the ammonium concentration of 788 mg L−1, nitrite accumulation occurred and the accumulated nitrite was reduced to nitrogen gas by the shortcut denitrification process. When the influent ammonium increased to a higher level of 1105 mg L−1, accumulation of nitrite and nitrate lasted in the whole cycle, and the removal efficiencies of total nitrogen and ammonium decreased to only 35.0% and 39.3%, respectively. Results also showed that DO was a useful process controlling parameter for the organics and nitrogen removal at low ammonium input. 相似文献
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Rashidul Alam Mubarak A. Khan Ruhul A. Khan Sushanta Ghoshal M. I. H. Mondal 《Journal of Polymers and the Environment》2008,16(3):213-219
Chitosan films were prepared from dried prawn shell via chitin and then tensile properties like tensile strength (TS) and
elongation at break (Eb) of the films were evaluated. Six formulations were developed using methyl methacylate (MMA) monomer
and aliphatic urethane diacrylate oligomer (M-1200) in methanol along with photoinitator (Darocur-1664). Then the films were
soaked in the formulations and irradiated under UV radiation at different doses for the improvement of physico-mechanical
properties of chitosan films. The cured films were characterized by measuring TS, Eb, polymer loading (PL), water absorption
and gel content properties. The formulation containing 43% MMA and 15% oligomer in methanol solution showed the best performance
at 20th UV pass for 4 min soaking time. 相似文献
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Assaâd Sila Najwa Mlaik Nadhem Sayari Rafik Balti Ali Bougatef 《Journal of Polymers and the Environment》2014,22(1):78-87
Extraction and depolymerisation of chitin and chitosan from shrimp waste material was carried out using fish proteases aided process. A high deproteinization level (80 %) was recorded with an Enzyme/Substrate ratio of 10 U/mg. The demineralization of shrimp waste was completely achieved within 6 h at room temperature in HCl 1.25 M, and the residual content of calcium in chitin was below 0.01 %. The degree of N-acetylation, calculated from the 13C CP/MAS-NMR spectrum, was 85 %. The chitin obtained was converted to chitosan by N-deacetylation. X-ray diffraction patterns also indicated two characteristics crystalline peaks approximately at 10° and 20° (2θ). Chitosan was then evaluated in the treatment of unhairing effluents from the tanning industry. A result showed that chitosan as a coagulant has good performance in alkaline pH and at concentration of 0.5 g/L. Within these conditions, chitosan could decrease turbidity value, total suspended solids (89 % at 1.5 g/L), biological oxygen demand (33.3 % at 1.5 g/L) and chemical oxygen demand (58.7 % at 1.5 g/L). 相似文献