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在三相流化床中NO_x全循环催化氧化预处理氰化尾渣的试验研究
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摘要
随着易处理金矿资源的日益消耗,难浸金矿和氰化尾渣的开发利用引起世界范围内的广泛关注。据统计,世界上80%的黄金冶炼企业采用氰化法提金,由此产生了大量的氰化尾渣,该尾渣含有可回收的金、银、铜、铅、锌、铁等有价金属元素。氰化尾渣的资源化,尤其是金、银、铁等元素的综合回收利用,不仅能消除氰化尾渣带来的环境污染,而且又能给炼金企业带来巨大经济效益,所以开发利用此类黄金资源具有十分重要的现实意义和长远意义。利用此类黄金资源最核心的内容是预处理方法的选择和运用,这将直接关系到不同元素的回收率,生产费用和环保等因素。
     在查阅大量文献资料和本课题组原有研究的基础上,提出采用在三相流化床中NO_x全循环催化氧化预处理氰化尾渣。本研究以产自中原黄金冶炼厂的氰化尾渣为物料,以NO_x为氧化剂,考察了深度预处理过程中影响铁浸出率的主要因素,研究得出最佳的预处理条件为反应温度为75℃,反应时间为3.5小时,硝酸质量浓度分数为15%,硫酸质量浓度分数为5%,气速为0.5m~3/h,分布板孔径为1mm-2mm,孔与孔之间距离为4mm-7mm。试验结果表明,在此条件下,氰化尾渣中铁的浸出率达到97.92%,失重率达到58.73%,氧化效果非常明显。在同等条件下预处理难浸金矿,铁的浸出率达到95.29%,失重率达到72.68%,表明该方法也是预处理难浸金矿的有效方法。并对其氧化机理进行初步分析。
     采用X射线衍射仪,LV扫描电子显微镜和X射线能谱仪对氰化尾渣和最佳工艺条件下预处理后的氧化渣分别进行X射线衍射,X射线线扫描和X射线面扫描微区分析和对比,得出该预处理方法能有效氧化黄铁矿,使包裹的金裸露出来,提高尾渣氰化提金率。把氰化尾渣和氧化渣在液固比5:1、PH=9-10、NaCN用量:2.0-3.0g/L、氰化时间为24h的条件下进行氰化提金,提金率从66.44%提高到99.39%。可见该预处理方法能够有效提高氰化提金率。
     最后比较了NO_x循环利用和不循环对预处理氰化尾渣的影响,研究结果表明NO_x循环利用能节约大量硝酸,缓解液体中硝酸浓度下降,提高反应速率,缩短氧化时间。实现了低温常压下NO_x自循环。在此基础上进行了扩大三相流化床催化氧化实验,研究表明,间隔一定时间只补充少量的硝酸就能维持氧化反应连续进行,铁的浸出率持续提高。
     本文所研究的预处理方法,预处理效果好,有效提高了氰化提金率,而且反应过程中实现NO_x全循环,减少了污染,符合环保节能减排的要求。但反应装置和材质需要进一步的研究和改进。
With increasingly exhausting of easily leachable gold ores,Developments of refractory gold ores and cyanide tailings have attracted extensive attention around the world.According to statistics,80%of the world's gold smelting enterprises to adopt cyaniding,resulting in a large number of cyanide tailings,the tailings contain recoverable gold,silver,copper,lead,zinc,iron and other valuable metal elements.These cyanide tailings are resourced,especially gold,silver, iron and other elements of a comprehensive recycling,it can eliminate the environmental pollution caused by cyanide tailings,but can bring tremendous economic benefits to the alchemical enterprise.It is practically Meaningful to explore better methods to utilize the refractory gold ores and cyanide tailings at present and in the future of china.Most important thing of developing this type of mineral is the choice and application of pretreatment method.This will directly relate to the recovery levels of different elements,cost,environmental protection and so on.
     According to in checking a large number of documents and the original study of our research group,the innovation of retreating cyanide tailings by the way of the catalytic oxidation system that in a three-phase circulating fluidized-bed with NO_x-wide circulation.In this paper,the cyanide tailings from Zhongyuan Gold Smelter used as the test materials,and NO_x reagent as the oxidant,The factors affecting the pretreatment process were examined,the optimum condition was obtained by study under conditions:Pretreatment temperature is 75℃,oxygenation time is 3.5h, initial concentration of nitric acid is 15%,initial concentration of Sulfuric acid is 5%,gas velocity is 0.5m~3/h,aperture of distribution plate is 1mm-2mm,the distance between the hole and the hole for 4mm-7mm.The results show,on this condition,the leaching rate of Fe reached 94.25%and weight loss reached 55.82%,oxidation effect is very obvious.Under the same conditions, pretreatment of refractory gold,the leaching rate of Fe reached 95.29%and weight loss reached 72.68%,indicating that the method of pretreatment of refractory gold is an effective way.The oxidation mechanism of the reaction was analyzed preliminarily.
     The X-ray diffraction(XRD),LV scanning electron microscopy(SEM) and Energy Dispersive Spectrometer(EDS) adapted to the cyanide tailings before and after the pretreatment respectively.Through analysis and comparison,this method of pretreatment is effective oxidation of pyrite,so that parcels out of gold exposed to enhance the rate of cyanide gold extraction.The cyanide tailings and oxide slag are cyanided gold under the conditions of the liquid-solid ratio 5:1, PH=9-10,NaCN dosage:2.0-3.0g/L,cyanide time for 24h,gold extraction rate from 66.44%to 99.39%.Can be seen that the pretreatment method to effectively improve the rate of cyanide gold extraction.
     Finally,Comparison of NO_x recycling and does not cycle on the effects of pretreatment cyanide tailings,the results show that recycling can save a lot NO_x nitric acid,nitric acid concentration in the liquid down to ease and improve the reaction rate and shorten the oxidation time.NO_x is achieved with a self-loop at low temperature and Normal pressure.On this basis,the catalytic oxidation experiments have been enlarged scale in three-phase fluidized bed.The results show that would only add a small amount of nitric acid oxidation reaction can be to maintain continuous in a certain time interval,and the iron leaching rate continued to improve.
     The pretreatment method studied in this paper,pretreatment effect is good,and effectively raise the rate of cyanide gold extraction.And the NO_x-wide circulation is achieved in reaction process;reduce pollution,environmentally friendly energy-saving emission reduction requirements.It is necessary to further study and improves the response equipment and the materials of equipment.
引文
[1]李俊萌.难处理金矿石预处理工艺及其选择[J].有色金属,2002,(5):16-23.
    [2]邝金才.氰化尾渣综合回收有价元素初探[J].黄金科学技术,2003,11(4):17-21.
    [3]郑哗,冯国臣,邹积贞.大水清金矿氰化尾渣综合回收利用研究[J].黄金 1998,19(1):43。
    [4]石同吉.氰化尾渣综合回收有价金属的研究与实践[J].金属矿山,2002,(3):39-41.
    [5]何柱生.提金废渣的综合利用[J].宝鸡文理学院报(自然科学版),1995,(2):40-44.
    [6]高俊峰,李晓波.我国氰化尾渣的利用现状[J].矿业工程,2005,3(4):38-39.
    [7]JL,i DabrowskiB,Miller JD,etal.The influence of pyrite pre-oxi-dation on gold recovery by cyanidation[J].Minerals Engineering,2006,(19):883-895.
    [8]杨振兴.难处理金矿石选冶技术现状及发展方向[J].黄金,2002,23(7):31-35.
    [9]DescostesM,Vitorge P,Beaucaire C.Pyrite dissolution in acidicmedia[J].Geochimica Cosmochimica Acta,2004,68(22):4559-4569.
    [10]楚宪峰,朱磊,吴向阳,康广凤,田建茹.氰化尾渣资源化应用的清洁生产技术研究[J].环境科学研究,2008,(6):72-75.
    [11]曾树凡.全球黄金按工艺方法分类和产量[J].国外金属矿选矿,1995,(5):35-41.
    [12]高俊峰,李晓波.我国氰化尾渣的利用现状[J].矿业工程,2005,3(4):38.
    [13]林海,菅小东.氰化尾渣的综合利用[J].矿产综合利用,1999,(4):41-43.
    [14]王宏军.超细粒氰化尾渣多金属浮选试验研究与实践[J].金属矿山,2003,(7):50-52.
    [15]李仕雄,李学强,张学政.从氰化尾渣高效回收铜、铅、锌、硫的新工艺研究[J].湖南有色金属,2009,25(1):13-16.
    [16]高俊峰,李晓波.我国氰化尾渣的利用现状[J].矿业工程,2005,3(4):38-39.
    [17]郑哗,冯国臣,邹积贞.大水清金矿尾渣综合回收利用研究[J].黄金,1998,19(1):43-46.
    [18]梁冠杰.河南某氰化尾渣中有价金属的综合回收[J].矿产综合利用,2001,(3):35-37.
    [19]林海,营小东.氰化尾渣的综合利用[J].矿产综合利用,1998,(4):4-6.
    [20]郑哗,冯国臣,邹积贞.大水清金矿氰化尾渣综合回收利用研究[J].黄金,1998,(1):43.
    [21]孙水裕,王淀佐,李柏淡.硫化矿物无捕收剂浮选基本规律及其分离方案[J].有色金属(选矿部分),1992,(6):4-8.
    [22]石同吉.氰化尾渣综合回收有价金属的研究与实践[J].金属矿山,2002,(3):39-41.
    [23]张大铸.综合回收氰化尾渣及尾液的探讨[J].有色金属(选矿部分),2002,(5):24-27.
    [24]龚焕高,印万忠.岩石矿石浮选-中国黄金生产实用技术[M].北京:冶金工业出社,1998.
    [25]林海.氰化尾渣回收铜、金、银的研究[J].矿产保护与利用,1998,(8):44-46.
    [26]梁冠杰.河南某氰化尾渣中有价金属的综合回收[J].矿产综合利用,2001,(6):35-37.
    [27]薛光,于永江.加压氧化-氰化浸出法从氰化尾渣中回收金[J].矿产资源综合利用,2004,(12):48-49.
    [28]张大铸.综合回收氰化尾渣及尾液的探讨[J].有色金属(选矿部分),2002,(5):24-27.
    [29]冯肇伍.金精矿氰化尾渣回收铜的研究与实践[J].有色金属(选矿部分),2002,(1):17-19.
    [30]郭宏,杨广军,张景和.天水金精矿氰化尾渣综合回收铜铅的试验研究[J].黄金,1999,(11):35-38.
    [31]邹积贞,郭普今,刘怡芳,杨晓枫,赵俊蔚.从中硫化物高砷矽卡岩型金矿石氰化尾渣中综合回收铜的工艺研究[J].黄金,1993,(8):29-32.
    [32]魏兆民,张德奎,郎淳慧.小口金精矿氰化尾渣综合回收铅的实验研究[J].吉林冶金,1996,(4):8-10.
    [33]贺政.氰化尾渣铅锌浮选试验研究[J),有色金属(选矿部分),2002,(6):9-12.
    [34]王宏军.超细粒氰化尾渣多金属浮选试验研究及实践[J].金属矿山,2003,(7):50-52.
    [35]张德魁,李伟,张英霞.从浮选粗精矿氰化炭浆法提金尾渣中综合回收铜铅金银的试研究[J].吉林冶金,1991,(1):19-24.
    [36]赵战胜.从氰化尾渣中提取S、Fe、Au的方法[J].黄金2007,7(28):40-41.
    [37]何柱生.提金废渣的综合利用[J].宝鸡文理学院报(自然科学版),1995,(2):40-44.
    [38]姬冲.氰化尾渣提金及制备铁红的研究[D].硕士论文,山东科技大学,2005.
    [39]刘建军,梁经冬,曾子高等.国内外固化焙烧难浸金矿工艺的现状及在我国应用前景[J].国外金属矿选矿,1997,3(2):36-37.
    [40]Sparrow G J,Woodcock J T.Cyanide and other Lixiviant Leaching Systems for Gold with some Practical Applications[J].Mineral Processing and Extractive Metallurgy Review,1995,(14):193-247.
    [41]童雄.强化贵金属金的选矿、化学提取、微生物浸出和深加工的新技术与新工艺[J].金属矿山,2005,(8):94-101.
    [42]李云.难处理砷金矿原矿焙烧试验研究[J].有色金属(冶炼部分),2005,(2):21-24.
    [43]Papangelakis,V.G.,Demopoulos,G.P.Acid pressure oxidation of pyrite[J].Hydrometallurgy,1991,26(3):305-325.
    [44]Yucel Kadioglu,Semra Karaca.Kinetics of pyrite oxidation in aqueous-suspension by nitric acid[J].Fuel Processing Technology,1995,(41):273-287.
    [45]谢斌,陆跃华,李关芳.生物冶金法处理难浸金矿的研究和应用[J].贵金属,1996,(3):47-54.
    [46]柯家骏.难浸金矿氰化提金的现状与问题[J].黄金科学技术,1998,6(1):32-39.
    [47]王康林,汪模辉,蒋金龙.难处理金矿石的细菌氧化预处理研究现状[J].黄金科学技术,2001,9(1):19-24.
    [48]杨振兴.难处理金矿石选冶技术现状及发展方向[J].黄金,2002,23(7):31-35.
    [49]熊英,柏全金等.黄铁矿包裹型难浸金精矿的细菌预氧化工艺研究[J].黄金,2003,24(11):32-36.
    [50]李育林,伍赠玲等.高硫高砷金精矿细菌氧化-氰化浸金实验研究[J].湿法冶金,2005,24(2):73-76.
    [51]魏以和,钟康年,王军等.微生物氧化处理崇阳难浸金矿[J].国外金属矿选矿,1996,(3):21-25.
    [52]李智伟.难浸金矿的细菌氧化工艺发展趋势[J].云南冶金,1997,(3):1-6.
    [53]苏建华,王继红.含砷含碳金精矿简而有效的预处理方法[J].黄金,2002,(9):38-39.
    [54]李波,张力先,徐继刚.难浸金矿石的预处理技术[J].沈阳黄金学学报,1996,15(1):79-82.
    [55]魏莉,贾微.难浸金矿预处理新工艺-微波焙烧[J].有色金属,2003,(12):29-31.
    [56]谷晋川,刘亚川.难浸金金矿微波预处理研究[J].有色金属,2003,55(2):55-56.
    [57]徐远志.难浸金矿的预处理方法及影响其工艺选择的冶金学因素[J].云南冶金,1998,(27):10-11
    [58]Simmons G L.Mineral and Metallurgical Processing[M].1994,286-289.
    [59]周一康.难处理金矿石预处理方法研究进展及对策建议[J].有色金属(冶炼部分)1999,(6):34-36.
    [60]孙全庆.难处理金矿石的碱法加压氧化预处理[J].湿法冶金,1999,3(2):14-17.
    [61]马尚文,孟庆芳.难浸金矿石提金研究现状[J].河南大学学报(自然科学版),1996,26(2):63-66.
    [62]曾青云,熊谟喜,陈均求等.赣南荡坪复合硫化矿的三氯化铁直接浸出的试验研究[J].江西有色金属,1995,(12):33-36.
    [63]胡全红,许民.三氯化铁浸出铅精矿工艺研究[J].江西化工,2001,(4):30-33.
    [64]李金丽,张明杰,王洪宽.三氯化铁浸出高冰镍[J].东北大学学报(自然科学版),1998,19(2):152-154.
    [65]刘谷山,不同氧化剂对Cu_2S、Ni_3S_2矿浮选行为的影响[J].湖南有色金属2003,19(3):11-12.
    [66]G.Van Weet,K.J.Fair,V.H.Aprahamian,2~(nd) International gold conference,1988,11,Canada.
    [67]G.Van Weet,K.J.Fair,J.C.Schneider,88~(th) Annual General Meeting of CIM.,1986,5,Canada.
    [68]Morris J.Beattie,Graham Balderson.International gold conference,1998,Austrialia.
    [69]刘建军,梁经冬,曾子高.国内外固化焙烧难浸金矿工艺的现状及在我国应用前景[J].国外金属矿选矿,1997,3(2):36-37.
    [70]夏光祥.关于硝化法预处理含砷难冶金矿石的进展概况[J].黄金,1989,10(7):20-25.
    [71]L.-S.范.Gas-Liquid-Solid Fluidization Engineering[M].北京:中国石化出版社.1993.
    [72]黄思才,刘国际.化学反应工程[M].北京:化学工业出版社,1995:169-170.
    [73]任欧旭,张少峰,韩莉果.气(汽)-液-固三相流研究进展[J].化工装备技术,2003,6(24):13-18
    [74]陈经明.关于硝酸氧化性的探讨[J].平顶山师专学报(自然科学版),1995,9(1):14-17.
    [75]张翠香.硝酸氧化性及还原产物教学初探[J].黑龙江教育学院学报,1995,(2):89-90.
    [76]陈经涛.也说浓硝酸与稀硝酸的氧化性[J].工陕西教育学院学报,1998,(3):76-79.
    [77]许端平,汪胜,钟力林.提高氮氧化水吸收效果途径初探[J].煤矿爆破,2001,(1):12-13.
    [78]郑存江,熊英,胡建平.微细粒包裹型金矿中金的赋存状态扫描电镜分析[J].理化检验,2006,42(4):184-186.
    [79]郑存江,熊英,胡建平.微细粒包裹型金矿中金的赋存状态扫描电镜分析[J].理化检验,2006,42(4):184-186.
    [80]郑玉春.金的处理工艺及其发展趋势[J].国外黄金参考(增刊),2001,(7):1-7.
    [81]王华译.回收金的几种基本工艺[J].国外黄金参考,1998,3(4):15-18,
    [82]童志权、陈焕钦.工业废气污染控制与利用[M].北京,化学工业出版社,1989:1.
    [83]黄达卿,陈亮,弯军英,桑小飞等.壳聚糖对金属离子的吸附选择性[J].广州化工,2005(6):36-38.

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