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1.
铝灰酸溶法制备聚合氯化铝   总被引:1,自引:0,他引:1       下载免费PDF全文
以铝灰为原料采用酸溶法制备了聚合氯化铝(PAC),并通过正交实验优化了PAC制备的最佳工艺参数,并考察了自制PAC对废水COD的去除效果。制备PAC的最佳工艺条件为:m(铝灰)∶V(HCl)∶V(H2O)=10∶20∶40,反应温度85℃,反应时间2.5h,搅拌转速80r/min,熟化时间30h,熟化温度60℃。采用生石灰可高效、经济地调节产品的盐基度,且产品在处理印染废水时COD去除率达64.7%,高于市售同类产品。  相似文献   

2.
本文通过染料,染料中间体废水气浮净水试验,结合国内外资料分析,概述了染料废水气浮净水的特点、工艺流程、处理效果,探讨了染料结构与气浮脱色的关系,并对提高气浮净水技术和浮渣处理提出了初步设想。  相似文献   

3.
硫铁矿烧渣酸解工艺研究   总被引:1,自引:1,他引:1  
刘毅  邹光中 《化工环保》2004,24(Z1):308-310
研究了硫铁矿烧渣酸解工艺及影响酸解的因素.通过正交试验,找到最适宜的工艺条件硫酸用量比1~1.1、水用量比75%、熟化温度250~300℃、熟化时间1~1.5 h,酸解率可达97%以上,制得硫酸铁盐溶液,可用作生产氧化铁系颜料的原料.  相似文献   

4.
用聚合硅酸铁处理砷化镓生产废水的研究   总被引:5,自引:0,他引:5  
用自制的聚合硅酸铁(PFSiC)对砷化镓生产中的含砷废水进行混凝处理。试验考察了硅铁比、熟化时间、PFSiC投加量、出水pH等对砷去除效果的影响,并与常用铁系混凝剂的除砷效果进行了比较。结果表明:在硅铁比为0.5:1、熟化时间为5d、PFSiC投加量为7~9mg/L、出水pH为6~8时,砷去除率达98.6%,除砷效果明显优于常规铁系混凝剂,出水水质达到GB8978—1996三级排放标准。  相似文献   

5.
苏洁  陈莉荣  刘文 《化工环保》2015,35(1):99-102
以高炉渣为原料,分别采用酸浸及碱浸-酸化工艺得到铁、铝离子及聚硅酸,再将铁、铝离子引入聚硅酸制得聚硅酸硫酸铝铁(PSAFS)混凝剂。考察了PSAFS的聚合条件对焦化废水混凝效果的影响,并与市售混凝剂进行了对比。实验结果表明:PSAFS的最佳制备条件为n(Al+Fe)∶n(Si)=0.53,混凝剂p H=1,熟化时间0.5 h,熟化温度60℃;PSAFS加入量为4 m L/L时,混凝效果最好,对焦化废水的浊度和COD的去除率分别达到98.9%和74.5%;PSAFS的性能优于市售的3种混凝剂。  相似文献   

6.
有机离子载入-复焙烧失法制备新型净水材料   总被引:3,自引:1,他引:2  
探索了一种制备介孔复合净水材料的新方法——载入有机离子一复焙烧失法。通过实验得到的最佳工艺参数为:有机载入剂为CTMAB,有机载入剂(质量浓度5g/L)加入量4mL/g,有机离子交换反应时间2h,反应温度40℃,复焙烧失温度230℃,复焙烧失时间1.5h。在最佳工艺条件下制备的净水材料对色度为7400倍、COD为3040mg/L的染料废水的脱色率为98.9%,略优于杏壳活性炭的脱色率(98.2%);COD去除率为91.3%,与杏壳活性炭的COD去除率91.7%相差无几。净水材料的染料吸附量是添加剂升温烧蚀后产品的近85倍,是酸洗刻蚀后产品的近590倍,是原材料的900多倍,其对染料废水的净化能力整体优于杏壳活性炭。  相似文献   

7.
高岭土制备聚合氯化铝新工艺   总被引:6,自引:0,他引:6  
介绍了以高岭土为原料,经盐酸预处理后,加水聚合、调整反应液pH,制备液体聚合氯化铝净水剂的新工艺。对所得产品的净水性能和技术指标进行了测定,结果表明,采用该工艺制得的聚合氯化铝产品技术指标符合GB1592-95标准。  相似文献   

8.
以鸡蛋壳为原料,对高温煅烧分解蛋壳、中和法制备乙酸钙(CA)的最佳反应条件进行了研究,试验结果表明:在反应温度为50 ℃、配料摩尔比为CaO∶乙酸=1∶2.8、乙酸浓度为15 mol/L、石灰乳浓度(以氧化钙计)为1.3 mol/L时CA产量最大.产品融冰试验表明:CA在环境温度-10℃以上使用时,其融冰效果较好.  相似文献   

9.
复合混凝剂CAF的研制与净水效果试验   总被引:14,自引:0,他引:14  
以天然物质甲壳素制备壳聚糖,并用壳聚糖、聚合铝和三氯化铁制成了复合混凝剂CAF。详细介绍了制备甲壳素、壳聚糖、CAF的工艺流程和最佳工艺参数,试验结果表明,CAF的净水效果明显优于无机混凝剂聚合铝和三氯化铁。  相似文献   

10.
以太原3~#净水活性炭为催化剂,在常压下,反应温度为80—90℃时,对含硫浓度为500毫克/升以下的废水,经一次处理可达1毫克/升以下,处理成本较空气氧化法经济。一、前言国外对含硫废水的处理方法,进行了较多的研究。1931年  相似文献   

11.
About 2.5 million tonnes of copper smelter slag are available in Küre, northern part of Turkey. This slag contains large amounts of metallic values such as copper and cobalt. A representative slag sample containing 0.98% Cu, 0.49% Co and 51.47% Fe was used in the experimental studies. Two different methods, direct acid leaching and acid baking followed by hot water leaching were used for recovering Cu and Co from the slag. The effects of leaching time, temperature and acid concentration on Cu- and Co-dissolving efficiencies were investigated in the direct acid leaching tests. The optimum leaching conditions were found to be a leaching time of 2 h, acid concentration of 120 g L(-1), and temperature of 60 degrees C. Under these conditions, 78% Cu and 90% Co were extracted. In the acid baking + hot water leaching tests, 74% Co was dissolved after 1 h of roasting at 200 degrees C using a 3:1 acid:slag ratio, whereas the Cu-dissolving efficiency was 79% and the total slag weight loss was approximately 50%.  相似文献   

12.
以凹凸棒土为载体、MnO_2为活性组分,制备了MnO_2陶粒臭氧氧化催化剂,并以草酸为模拟污染物,采用响应面法对催化剂的制备条件进行了优化。实验结果表明:各因素对草酸去除率影响的显著性顺序为MnO_2投加量盐酸溶液质量分数煅烧时间煅烧温度。催化剂的最佳制备条件为:MnO_2投加量200 mg/g,盐酸溶液质量分数20%,煅烧时间2 h,煅烧温度400℃。在初始草酸质量浓度150 mg/L、溶液pH 3.11、臭氧投加量8.10 mg/min、臭氧-氧气曝气量400 m L/min的条件下,最佳条件制备的催化剂在反应30 min时的草酸去除率达66.99%。催化剂具有良好的活性稳定性,且催化过程中Mn~(2+)溶出量低。催化剂具有较大的比表面积,负载的MnO_2类型为α-MnO_2和β-MnO_2。  相似文献   

13.
Properties of Starch/PVA Blend Films Containing Citric Acid as Additive   总被引:8,自引:0,他引:8  
Starch/polyvinyl alcohol (PVA) blend films were prepared successfully by using starch, polyvinyl alcohol (PVA), glycerol (GL) sorbitol (SO) and citric acid (CA) for the mixing process. The influence of mixing time, additional materials and drying temperature of films on the properties of the films was investigated. With increase in mixing time, the tensile strength (TS), elongation (%E), degree of swelling (DS) and solubility (S) of the film were equilibrated. The equilibrium for TS, %E, DS and S value was 20.12 MPa, 36.98%, 2.4 and 0.19, respectively. The mixing time of equilibrium was 50 min. TS, %E, DS and S of starch/PVA blend film were examined adding glycerol (GL), sorbitol (SO) and citric acid (CA) as additives. At all measurement results, except for DS, the film adding CA was better than GL or SO because hydrogen bonding at the presence of CA with hydroxyl group and carboxyl group increased the inter/intramolecular interaction between starch, PVA and additives. Citric acid improves the properties of starch/PVA blend film compared to glycerol and sobitol. When the film was dried at low temperature, the properties of the films were clearly improved because the hydrogen bonding was activated at low temperature.  相似文献   

14.
用副产盐酸和劣质高岭土制备聚合氯化铝   总被引:4,自引:0,他引:4  
开发出一种用废盐酸和劣质高岭土生产聚合氯化铝的方法。分别考察了焙烧温度,焙烧时间,盐酸用量以及酸浸时间对铝浸出率的影响。试验结果表明;依照该工艺生产的聚合氯化铝,其各项指标符合GB15892-95标准。  相似文献   

15.
蒋银峰  朱梦冰 《化工环保》2018,38(5):605-608
以含铝废硫酸和废铝渣为原料制备聚合硫酸铝(PAS)。优化了废铝渣的酸溶条件,确定了合适的稳定剂和碱化剂。实验结果表明:在酸溶反应温度为80 ℃、酸溶反应时间为40 min、以20 g/L Ca(OH)2溶液为碱化剂、以加入量为60 mg/L的固体柠檬酸为稳定剂的条件下,制备的PAS比聚合氯化铝(PAC)和Al2(SO43具有更优异的混凝性能。该工艺可回收利用废铝渣和含铝废硫酸,从而达到综合利用的目的。  相似文献   

16.
Simultaneous recovery of vanadium (V) and nickel (Ni), which are classified as two of the most hazardous metal species from power plant heavy fuel fly-ash, was studied using a hydrometallurgical process consisting of acid leaching using sulfuric acid. Leaching parameters were investigated and optimized in order to maximize the recovery of both vanadium and nickel. The independent leaching parameters investigated were liquid to solid ratio (S/L) (5–12.5 wt.%), temperature (45–80 °C), sulfuric acid concentration (5–25 v/v%) and leaching time (1–5 h). Response surface methodology (RSM) was used to optimize the process parameters. The most effective parameter on the recovery of both elements was found to be temperature and the least effective was time for V and acid concentration for Ni. Based on the results, optimum condition for metals recovery (actual recovery of ca.94% for V and 81% for Ni) was determined to be solid to liquid ratio of 9.15 wt.%, temperature of 80 °C, sulfuric acid concentration of 19.47 v/v% and leaching time of 2 h. The maximum V and Ni predicted recovery of 91.34% and 80.26% was achieved.  相似文献   

17.
郝旗  余静  袁率  朱顺利  王博  邱海浪 《化工环保》2017,37(3):340-345
以硝酸浸取废无汞碱性电池极性材料,再加入硝酸铁及蔗糖生成前驱体,最后通过焙烧制得锰锌铁氧体磁性纳米颗粒。优化了酸浸和焙烧条件,采用FTIR和DTA-TG技术研究了前驱体的形成和热解过程,采用XRD、FTIR、TEM技术和振动样品磁强计对锰锌铁氧体进行了表征。结果表明:废无汞碱性电池极性材料酸浸的最佳条件为H_2O_2加入量3%(w)、液固比10 mL/g、稀硝酸浓度4 mol/L、浸取温度40℃,该条件下浸取10 min锰和锌的浸出率均可达100%;所得前驱体为葡萄糖酸盐,其最佳焙烧条件为焙烧温度450℃、焙烧时间2 h;最佳条件下所得锰锌铁氧体为尖晶石型Mn_(0.5)Zn_(0.5)Fe_2O_4,其颗粒为球形、大小均匀,且磁性能优良。  相似文献   

18.
Date stone wastes have been utilized for production of activated carbon by chemical activation with phosphoric acid using a fluidized-bed reactor. The effects of the activation time, activation temperature, impregnation ratio, and particle size on the yield and the adsorptive capacity towards iodine were studied. The yield and the quality of the activated carbon prepared by using H3PO4 were compared with that prepared from date stones using the same equipment, and under similar conditions by using ZnCl2 as an oxidizing agent. The maximum value of the iodine number of the activated carbon produced using H3PO4 in this work was about 495 under the following conditions: impregnation ratio 0.4, activation time 60 min, activation temperature 800 degrees C, particle size 0.60 mm. The iodine number for the produced activated carbon was higher when phosphoric acid was used, compared to that when zinc chloride was used as impregnation reagent; however, the yield obtained when H3PO4 was used was lower than the yield when ZnCl2 was used. The iodine number increases significantly with increasing the activation temperature. By increasing the impregnation ratio at the same temperature, the iodine number decreased sharply and an oscillation is noticed for all the cases but it was clearer at 800 degrees C. The average variation of the iodine number for the whole range of particle size used in this work is +/-10%.  相似文献   

19.
The ability of Copper Smelter Slag (CSS) to reduce Cr(VI) in aqueous solutions has been investigated. The extent of reduction is dependent on the amounts of acid and reductant, contact time, Cr(VI) concentration, temperature of the solution and particle size of CSS. The amount of acid is the most important variable affecting the reduction process. When twice the amount of acid required with respect to Cr(VI) was used, Cr(VI) in 100 ml solution (100 mg/l) was completely reduced in a contact period less than 5 min by a 10 g/l dosage of CSS. Reduction efficiency increased with increase in temperature of solution, showing that the process is endothermic. Reduced chromium, and iron and other metals dissolved from CSS were effectively precipitated by using NaOH or calcinated carbonatation sludge from sugar plant.  相似文献   

20.
在对废SCR催化剂组成进行分析的基础上,采用草酸和酒石酸两种有机酸浸取废SCR催化剂中的V和W。实验结果表明:草酸对V、W的浸出率均大于酒石酸;在草酸浓度为1.00 mol/L、浸取温度为80 ℃、液固比为10 mL/g、浸取时间为180 min时,V和W的浸出率分别为63.50%和13.12%;在酒石酸浓度为0.5 mol/L、浸取温度为100 ℃、液固比为10 mL/g、浸取时间为180 min时,V和W的浸出率分别为44.00%和9.00%。酸性浸出未改变SCR催化剂中TiO2的晶型,剩余残渣中依然保留着TiO2骨架,可继续作为催化剂载体使用。  相似文献   

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