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从废催化剂中回收钼的新工艺 总被引:4,自引:2,他引:2
确定了用新型复合浸取剂从废催化剂中回收钼的最佳工艺条件废催化剂颗粒度100目焙烧温度750℃,焙烧时间1h复合浸取剂中助浸剂质量为5%,浸取固液质量比1:3,浸取温度60℃,浸取时间6h,在该条件下,钼的浸取率达到92.7%~95.5%。 相似文献
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采用清洁生产概念与思维模式,对铜铬催化剂生产全过程进行审核,找出造成其产率低、活性差、污染重的原因及影响因素。以新催化剂研制理论和方法为指导,探讨铜铬催化剂用于糠醇生产过程中提高其产率、活性、原材料利用率以及减轻污染的清洁生产工艺。试验结果表明,在pH为6.2~6.5、Cu/Cr质量比为1:1、反应温度为65℃,活化温度为400℃的条件下,催化剂能获得较高产率和活性。按此新工艺生产的催化剂,产率可提高22%,Cr^6 的排放量可减少95%,活性可提高一倍,废品率可由原来的10%降至零。 相似文献
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以纯SO2及燃煤电厂烟气作实验气,利用积分法固定床CFB方式进行了DS-Ⅰ型催化剂与活性炭催化性能的对比试验,对不同还进行了不同烟气温度、SO2浓度、湿度、烟气流速等工艺参数对DS-Ⅰ型催化剂催化性能的影响试验。对不同催化剂进行优化组合,可在除尘器后直接脱硫、脱氮、其脱硫率达86%、脱氮率达68%。催化剂经再生,可反复使用。 相似文献
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常温常压下催化湿式过氧化氢氧化工艺的研究 总被引:4,自引:0,他引:4
采用浸渍焙烧法制备了几种负载型催化剂,以偶氮染料模拟废水为处理对象,考察了这几种催化剂在常温常压下催化湿式过氧化氢氧化工艺中的催化活性。研究结果表明,Fe/γ~Al2O3的催化活性和稳定性最好。处理质量浓度为500mg/L的甲基橙模拟废水,当Fe/γ-Al2O3和H2O2加入量分别为30g/L和330mg/L时,处理3h后,废水的脱色率为79.67%,COD去除率为80.92%,总有机碳去除率达72.88%。在上述相同工艺条件下,分别处理质量浓度为500mg/L的甲基橙、酸性橙和活性黑模拟废水,其中,甲基橙较易被降解,酸性橙次之,活性黑最难被降解。 相似文献
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采用絮状锰悬浊液催化剂空气氧化处理含硫废水 总被引:7,自引:0,他引:7
探讨了一种快速降解含硫废水中硫化物的新方法。用可溶性二价锰盐在pH为10.5-12.0时曝气,制得絮状锰悬浊液催化剂。使用该催化剂可将废水中S^2-的氧化反应速率大为提高,反应时间大为缩短,S^2-去除率几近100%;同时还可大大降低废水的COD,因此可大大降低生化处理系统的负荷。处理S^2-质量浓度为50-2000mg/L含硫废水的最佳工艺条件:絮状锰悬浊液催化剂与废水的体积比为0.8-1.0,pH为10-12,曝气量为50L/h左右,反应温度为15-45℃。絮状锰悬浊液催化剂可循环使用。 相似文献
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Waste plastics contain a substantial number of valuable chemicals. The wastes from post-consumer as well as from industrial production can be recycled to valuable chemical feedstock, which can be used in refineries and/or petrochemical industries. This chemical recycling process is an ideal approach in recycling the waste for a better environment. Polymer cracking using a laboratory fluidised bed reactor concentrated on the used highly contaminated catalyst, E-Cat 2. Even though E-Cat 2 had low activity due to fewer acid sites, the products yielded were similar with amorphous ASA and were far better than thermal cracking. The high levels of heavy metals, namely nickel and vanadium, deposited during their lifetime as an FCC catalyst, did not greatly affect on the catalyst activity. It was also shown that E-Cat 2 could be used with and without regeneration. Although there was more deactivation when there was no regeneration step, the yield of gases (C2-C7) remained fairly constant. For the first time, these results indicate that “waste” FCC catalyst (E-Cat) is a good candidate for future feedstock recycling of polymer waste. The major benefits of using E-Cat are a low market price, the ability to tolerate reuse and regeneration capacity. 相似文献
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采用热解—氨浸工艺处理含铜废催化剂(w(Cu)为23.6%),优化了工艺条件,并通过蒸氨还原法制备出Cu2O产品。实验结果表明:热解工段中,控制管式热解炉的空气流量为3.0 m3/min,在升温速率20 ℃/min、热解终温600 ℃、终温保持时间90 min的优化条件下,含铜废催化剂中的有机物热解完全;氨浸工段中,以NH4Cl-NH3-H2O溶液为氨浸液,控制氨浸温度为40 ℃,在烧成料研磨时间90 min(粒径29.43 μm)、氨浸液总氨浓度4 mol/L、氨浸时间80 min的优化条件下,铜浸出率达到98%;经蒸氨还原法制得的Cu2O产品的质量符合HG/T 2961—2010《工业氧化亚铜》中的一等品标准,产率为24%。 相似文献
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以颗粒活性炭(GAC)为载体、铜为活性组分、铈为助剂组分、草酸钠为沉淀剂,采用浸渍焙烧法制得CuO_x-CeO_2/GAC催化剂。以H_2O_2为氧化剂,微波强化催化湿式过氧化氢氧化(CWPO)处理二甲亚砜(DMSO)初始质量浓度为1 000 mg/L的废水,处理3 min后DMSO去除率达93.8%。催化剂第7次使用时DMSO去除率仍保持在75%以上。初始废水pH在3~9范围内,DMSO去除率均在85%以上。助剂Ce的加入提高了催化剂表面活性组分的分散性和稳定性,使催化剂的活性稳定性和使用寿命显著提高。 相似文献
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以沉淀一热解法制备了纳米级Co3O4催化剂,并用X射线衍射仪、红外光谱仪对Co3O4催化剂进行了表征。以300W高压汞灯为光源,研究了Co3O4催化剂对不同活性染料的光催化氧化活性。实验结果表明:在活性染料质量浓度为20mg/L、250mL染料溶液中Co3O4催化剂加入量为150mg、反应2h的条件下,Co3O4催化剂对B—GFF黑、B—RN蓝、K—NR艳蓝3种活性染料溶液的脱色率分别为95%,87%,77%;适当加入酸或碱有利于提高处理效率,反应后染料溶液的pH为7.12~8.37,染料溶液初始pH为10.00时的脱色率最高为100%;Co3O4催化剂具有一定的再利用价值。 相似文献
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Jeong-Geol Na Byung-Hwan Jeong Soo Hyun Chung Seong-Soo Kim 《Journal of Material Cycles and Waste Management》2006,8(2):126-132
Catalytic pyrolysis of low-density polyethylene (LDPE) was investigated using various fly ash-derived silica–alumina catalysts
(FSAs). FSAs were prepared by a simple activation method that basically includes NaOH treatment of fly ash by a fusion method,
followed by an aging process. A series of LDPE pyrolysis experiments was conducted and the catalytic performance of FSAs was
assessed in terms of the degradation temperature and the simulated boiling point distribution of the liquid products. The
effects of synthesis conditions such as NaOH/fly ash weight ratio and aging time were examined by X-ray diffractometer (XRD),
Brunauer-Emmett-Teller (BET) surface area analyzer, and scanning electron microscope to clarify the controlling factors affecting
the catalytic activity. To obtain catalyst with high activity, it is necessary to produce sufficient silica and alumina species
that can be easily co-precipitated into solid acid catalyst by destruction of the fly ash structure and to optimize the activation
time for catalyst synthesis to prevent the transformation into inactive phases. The catalytic performance of FSA obtained
from optimal conditions was equivalent to that of commercial catalysts, demonstrating the effectiveness of the catalyst. 相似文献
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采用溶胶-凝胶法制备了活性炭纤维负载TiO2催化剂(TiO2/ACF),并通过SEM和XRD等手段对TiO2/ACF进行了表征。以邻苯二甲酸二甲酯(DMP)为目标降解物,考察了催化材料的电催化活性。实验结果表明:在反应温度为25 ℃、初始DMP质量浓度为100.0 mg/L、电解质Na2SO4质量浓度为100 mg/L、电流密度为62.5 mA/cm2、电极板间距为4 cm的条件下,经过40 min的降解,DMP质量浓度为1.8 mg/L,DMP去除率为98.2%;TiO2/ACF在反应过程中可以原位再生,经6次重复使用后仍保持很高的催化活性,对DMP的去除率仍达90%以上。 相似文献
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采用水热法制备了纳米α-MnO2催化剂,并通过XRD和SEM技术对催化剂的成分和形貌进行了表征。采用纳米α-MnO2催化剂催化臭氧氧化降解水中的双酚A(BPA),考察了初始溶液pH、催化剂加入量和反应温度对BPA去除率的影响。实验结果表明,纳米α-MnO2催化剂催化臭氧氧化降解BPA的最佳工艺条件为:催化剂加入量100 mg/L,初始溶液pH 8.5,反应温度18 ℃。在此最佳条件下处理质量浓度为10 μg/mL的BPA溶液120 min,BPA去除率为96.4%。回收洗涤后第二次使用的催化剂的BPA去除率为80.5%,第三次使用的催化剂的BPA去除率为74.1%,催化剂的活性随重复使用次数的增加而缓慢降低,活性较稳定。 相似文献
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López A de Marco I Caballero BM Adrados A Laresgoiti MF 《Waste management (New York, N.Y.)》2011,31(8):1852-1858
In this work, a study of the regeneration and reuse of ZSM-5 zeolite in the pyrolysis of a plastic mixture has been carried out in a semi-batch reactor at 440 °C. The results have been compared with those obtained with fresh-catalyst and in non-catalytic experiments with the same conditions. The use of fresh catalyst produces a significant change in both the pyrolysis yields and the properties of the liquids and gases obtained. Gases more rich in C3-C4 and H2 are produced, as well as lower quantities of aromatic liquids if compared with those obtained in thermal decomposition. The authors have proved that after one pyrolysis experiment the zeolite loses quite a lot of its activity, which is reflected in both the yields and the products quality; however, this deactivation was found to be reversible since after regeneration heating at 550 °C in oxygen atmosphere, this catalyst recovered its initial activity, generating similar products and in equivalent proportions as those obtained with fresh catalyst. 相似文献