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将具有螯合功能的黄原酸基和酰胺基接枝到交联淀粉分子结构中,制备了高分子重金属螯合絮凝剂ISXA。通过单因素试验和正交试验获得了ISXA的最佳制备条件为:淀粉交联阶段,环氧氯丙烷与淀粉质量比为1.2∶10,反应温度为40℃,p H值为10;黄原酸化阶段,CS2与淀粉质量比为6.3∶10,反应温度为35℃,p H值为11;丙烯酰胺(AM)接枝阶段,AM与淀粉质量比为1.5∶10,反应温度为45℃,p H值为5。经FTIR、元素分析,ISXA具有黄原酸基及酰胺基结构。对Cu2+的螯合絮凝试验结果表明,ISXA在在弱酸性下有很好的捕集沉淀效果,p H值为6时,对于Cu2+质量浓度分别为5、20和50 mg/L的溶液,ISXA的投加量分别为24、90及200mg/L,Cu2+去除率可达99%。絮体颗粒密实,在不同p H值下沉降性能良好。黄原酸基中的硫原子与Cu2+发生配位反应而形成ISXA-Cu螯合沉淀物,吸附架桥和网扫卷捕是ISXA絮凝反应的主要机理。 相似文献
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利用过氧化氢在不同条件下对玉米秸秆制备生物乙醇的酶水解残渣进行氧化改性,氧化产物分别与Fe2+、Cu2+、Zn2+、Mn2+四种离子进行螯合反应制备微肥。探讨了不同氧化条件对金属离子螯合率的影响,并确定了适宜的氧化工艺条件:过氧化氢用量20%,温度70℃,pH值为11,时间60 min,此时残渣溶出率为32.5%,氧化产物对Fe2+、Cu2+、Zn2+、Mn2+四种金属离子的总螯合率分别为5.0%,4.5%,3.9%,4.0%。通过正交试验分析,氧化条件对酶解残渣的溶出率和总螯合率的影响主次顺序为:pH值,过氧化氢用量,温度。 相似文献
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为考察聚环氧琥珀酸对Ca~(2+)的螯合能力及其影响效果,采用滴定法考察了聚环氧琥珀酸与Ca~(2+)在不同反应条件下发生螯合反应的钙螯合值。单因素试验结果表明,聚环氧琥珀酸的钙螯合值受反应温度的影响较为明显,在5~45℃范围内随温度升高而增大,在45~65℃范围内随温度上升而减小。但在溶液初始pH值为6.5~9.5的条件下,钙螯合值受溶液初始pH值的影响较小。通过正交试验获得的最大钙螯合值为124.5 mg/g,对应的螯合官能团最大利用率仅为54.4%,而剩余的螯合官能团可能为PESA的致晶格畸变作用和分散作用提供了物质基础。 相似文献
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超临界水氧化处理偏二甲肼废水研究 总被引:1,自引:0,他引:1
采用Cu2+为催化剂、H2O2为氧化剂,在24~30MPa和480~500℃的条件下,在一连续流反应器中进行了催化超临界水氧化偏二甲肼实验。研究了温度、压力、停留时间和Cu2+浓度对偏二甲肼氧化降解的影响。结果表明,在超临界水中偏二甲肼能被有效去除。偏二甲肼的去除率随反应温度和压力的升高、停留时间的延长和Cu2+浓度增大而提高。当Cu2+浓度为30 mg.L-1时,偏二甲肼的去除率与无催化剂时相比有了较大的提高。当30MPa、500℃、3.9s和Cu2+浓度为15 mg.L-1时,COD去除率高达99.4%。 相似文献
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螯合沉淀法处理电路板碱氨蚀刻废水 总被引:3,自引:2,他引:1
研究了环境友好型的有机硫螯合剂TMT处理电路板碱氨蚀刻废水的影响因素,用元素分析、红外与X衍射等手段表征了生成的沉淀产物,并对它的热分解性与在去离子水中的渗滤性作了初步探讨。结果表明,TMT能与铜离子强力螯合并沉淀,处理电路板碱氨蚀刻废水的效果好,废水的pH值为8,总铜的质量浓度为350.9mg/L,总氨质量浓度为349.4 mg/L,当TMT与Cu的量比为2.1:3时,上清液中残余铜的质量浓度为0.10 mg/L,铜去除率达99.97%。生成的沉淀物为非晶态的Cu3(C3N3S3)2.1.5H2O,它的热稳定性较高,在去离子水中渗滤出的饱和铜浓度很低,不会对环境造成二次污染。 相似文献
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利用1398中性蛋白酶水解的脱脂豆粕作为多肽的来源,对多肽络合锌的制备工艺条件进行了初步研究。研究了配位体摩尔比和pH值对络合反应的影响,确定合适的配比反应条件为:配位摩尔比为2:1,pH=8.0,产品络合率达到97%以上。并且用化学分析法和红外光谱法鉴定了产品。初步实验得出多肽络合锌具有抗氧化性。 相似文献
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合成了乙二胺四乙酸酰肼,研究了水溶液中EDTAH与Fe^3+的反应。利用UV分光光度计测定了Fe^3+-EDTAH螯合物的组成、表观稳定常数。 相似文献
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Girish M. Deshmukh Aparna Shete Deepali M. Pawar 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2013,88(3):432-436
BACKGROUND: Oxidative absorption of hydrogen sulfide into a solution of ferric chelates is studied in a stirred cell glass reactor. The experiments were performed to investigate the degradation of chelates sodium salt of nitrilotriacetic acid (NTA) (Merck), ethylenediaminetetraacetic acid diadisodium salt (EDTA) and diethylenetriaminepentaacetic acid (DTPA) at 313 K, pH 6, iron concentration 10 000 g L?1 and Fe:chelate molar ratio 1:2. RESULTS: Oxidative absorption of hydrogen sulfide into a solution of Fe‐NTA was found to be more successful, therefore, further experiments with 10%, 50% and 100% concentrations of hydrogen sulfide were performed. It was shown that this process is applicable for removal of low and high concentrations of hydrogen sulfide. The effect of antioxidants using sodium thiosulfate was also studied in order to minimize degradation of NTA. The kinetics were studied and it was observed that the reaction appeared to be first order in ferric chelate with rate constants for 100, 50 and 10% hydrogen sulfide concentration: 0.035, 0.013 and 0.019 h?1, respectively. CONCLUSIONS: Gas sweetening processes have commercial importance in natural gases, refinery of gases and biogas processing. Desulphurization and cleaning (i.e. removal of H2S and CO2) of petroleum gas and biogas is important to make the gas methane rich and to increase the calorific value of fuel. The same techniques of desulphurization and cleaning can be used for treating natural gas or petroleum gas. The desulphurization and cleaning processes can minimize the atmospheric emission of gases like SOx, NOx and CO. As the iron chelate based process is based on the principle of redox reaction of metal chelate with hydrogen sulfide, this method is very useful for desulphurization of petroleum gas and biogas. This work studied the effective use of Fe‐NTA solution for removal of high to low concentrations of H2S as found in biogas and industrial waste gases. © 2012 Society of Chemical Industry 相似文献
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以苯酚、乙醛酸和乙二胺等为原料,通过曼尼希反应一步得到乙二胺二邻羟苯基乙酸(o,o-EDDHA),通过FT-IR、1H NMR对其进行了表征。研究了反应温度、反应时间、配料比、原料浓度、相转移催化剂种类等对o,o-EDDHA收率和选择性的影响。研究结果表明EDDHA的优化合成条件为:反应温度55℃,反应时间为3 h,配料比为苯酚∶乙醛酸∶乙二胺∶氢氧化钠=2.6∶2∶1∶0.1(摩尔比),乙醛酸的浓度为20%,相转移催化剂为四丁基氢氧化铵,目标产物o,o-EDDHA的最高收率可达到69.7%,选择性达97%,与相关文献报道中的收率和选择性相比具有很大提高。 相似文献
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The simultaneous separation of various metal ions (nickel, copper, calcium, and iron) from chelating agents (EDTA and citric acid) in water streams using Nanofiltration membranes is analyzed. Assuming that multiply-charged species are highly rejected, chemical speciation computations reproduce the observed patterns of metal and ligand rejection at different pH values and concentrations. The separation of metal ions from citric acid is achieved in acidic conditions, where multiply-charged free metal ions and neutral or singly charged free chelating species are abundant. Overall, speciation studies help to evaluate the applicability of Nanofiltration for recycling chelating agents used for metal extraction. 相似文献
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