脂肪酸的深度氧化及浮选机理研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
随着我国钢产量和钢消费量的高速增长,对铁矿石的需求越来越大。而国内铁矿资源丰而不富,复杂难选矿物储量大。复杂难选矿石选矿技术及选矿工艺的研究对提高我国铁矿资源综合利用率具有重要的现实意义。本文根据国内外利用阴离子捕收剂反浮选铁矿与石英的研究现状,针对现当前我国药剂的开发应用情况,结合单矿物和实际矿石浮选,研究合成了新型高效捕收剂MG-2,实现了药剂的工业化生产,并成功的在河北钢铁司家营选矿厂进行了工业试验,获得了良好的试验指标。
     以脂肪酸为原料,在催化剂紫外光催化条件下进行氧化反应;根据系统条件试验探索,确定MG-2的合成条件为:氧化剂用量为脂肪酸的15%,且氧化剂浓度为50%为宜;合成温度80℃,时间4-5h最佳;经红外光谱分析和碘值测试表明:合成产物为α-过氧羟基脂肪酸。单矿物试验表明:MG-2具有比脂肪酸更强的捕收性能和更好的选择性,药剂的捕收性随PV值的增大而增加;过氧羟基脂肪酸在水溶液中的CMC较高,具有很好的分散性,其耐低温能力较原脂肪酸有了较大的提高,与常用的药剂相比,具有耐低温的特点。
     以司家营铁矿为浮选给矿,通过正交试验确定各个药剂条件,在此基础上进行药剂比较试验、开路实验、闭路试验:试验表明,MG-2是司家营氧化矿的良好的捕收剂,与原脂肪酸相比,在铁精矿产率相当的前提下,精矿品位、回收率分别提高1.5%、3%,尾矿品位降低3%,且药剂用量减少30%左右:现场试验室小试与工业试验结果表明,用MG-2为捕收剂时,可以在满足司家营矿业公司对浮选精矿质量(>65%)要求的前提下,显著降低了浮选药剂用量,且浮选状态稳定,泡沫密且实,降低了出现泡沫跑槽的几率,解决了司家营铁矿浮选药剂用量大,成本高的缺点。
     氧化机理研究分析表明:脂肪酸氧化是典型的游离基反应,影响氧化反应的主要因素是游离基的存在与数量,因此,无论是催化剂、温度、时间和氧化剂的使用都是通过改变反应溶液中的游离基的存在和数量来控制反应进程的。石英Zeta研究表明,Ca~(2+)作为石英浮选的活化剂,其主要作用是起压缩石英表面双电层厚度,在高碱度区域内,MG-2与含钙离子的石英作用较强,适合于反浮选。通过红外光谱分析,对比有无用去离子水清洗的条件下,MG-2与石英作用机理,证明了在有钙离子活化时,MG-2与石英发生了化学吸附。
As the production and consumption of steel is growing rapidly,the demand of iron ore in our country is increasing.And domestic iron ore resources are plentiful but poor,lot of which are complex refractory iron ores.Therefore,the research of separation technology for complex iron ores has an important practical significance on improving comprehensive utilization of iron ore resources in China.Based on the domestic and international reserch for Separating iron ore and quartz by anion-collector reverse flotation,the research and application of anion-collector was analysissed.Through the experiment of pure mineral and actual mineral,a new collector MG-2 was studied.The industrial production MG-2 has been successfully applied to Concentrator of sijiaying and achieved good index.
     In this article,fatty acid was selected as raw material,ultraviolet radiation was selected as catalyzer,MG-2 was synthesized.Through a series of condition tests,the optimum synthesis condition was determined,the reaction temperature and time were respectively 80℃and 4-5 hour,Dosage of Oxidant was 15%of fatty acids,which appropriate Concentration is 50%.Through the Infrared Absorptions Spectra analysis and iodine value test,α-Peroxy-hydroxy aether fatty acid was found in the synthetic product.The pure mineral experiment show that the MG-2 has stronger collective power and selective than fatty acid.,it's collective power increases with the increase in PV value.It has high CMC value and difficult to form colloidal micelle in the water, so it has the feature of low temperature proofing.
     Take the magnetic concentrate of sijiaying as raw ore for flotation.Through orthogonal experiments,the condition of flotation reagent was confirmed.Baseing on these conditions,the collector comparison test,opened flotation and closed flotation were achieved.The test indicated that MG-2 was a good collector for sijiaying iron ore,Compare to the raw fatty acid,the grade and recovery of flotation concentrate were respectively increased by 1.5%and 3%,the grade of tail and the dosage were respectively reduced by 3%and 30%.Take the MG-2 as collector for flotation of sijiaying iron ore,it could satisfied for the demond of flotation concentrate quality(>65%),the amount of flotation reagent was significantly reduced and the bubble was stability and density.
     Through the research and analysis of oxidation mechanism,the oxidation of fatty acid was a typical free radical reactions,the major factor was the amount of free radical.So Controlling this reaction was the same as changed amount of radical reactions where changed catalyst,temperature or oxidant.Through the measurement on pure quartz by the Zeta-potential,taking the Ca~(2+) as activator for quartz,Ca~(2+) played a primary role in compressing the double electric layer of quartz.In the high concentration alkali solution,MG-2 had a strong effect with Ca~(2+)-containing quartz, which was suitable to reverse.From the Infrared analysis,the adsoption of MG-2 on the surface of quartz was mainly cheimical.
引文
[1]余永富.我国铁矿山发展动向、选矿技术发展状况及存在的问题.矿冶工程,2006(01):21-22.
    [2]张泾生.我国铁矿资源开发利用现状及发展趋势[J]金属矿山,2000(2):34-37.
    [3]印万忠.铁矿选矿新技术与新设备[M],冶金工业出版社,2007
    [4]袁致涛.我国难选铁矿石资源利用的现状及发展方向[J].金属矿山,2007,367:1-3
    [5]R.K.Upadhyay and A.S.Venkatesh,Current strategies and future challenges on exploration,benefication and value addition of iron ore resources with special emphasis on iron ores from Eastern India.Applied Earth Science,2006,Vol.115,No4.
    [6]杨晓峰.选别鞍山地区贫磁铁矿石的合理工艺流程研究[J].矿业工程,2008,28(3):57-59.
    [7]张立刚,余永富.太钢袁家村铁矿石英型氧化矿选矿工艺研究[J].矿业工程,2007,27(6):19-21.
    [8]HAYDN H.MURRAY.High-extraction magnetic filtration:A new beneficiation process for industrial minerals[J].GSA Bulletin,1981,92:18-61.
    [9]孙炳泉.近年我国复杂难选铁矿石选矿技术进展[期刊论文],金属矿山2006(3).
    [10]S.Songa,S.Lu,A.Lopez-Valdivieso.Magnetic separation of hematite and limonite fines as hydrophobic flocs from iron ores[J].Minerals Engineering,2002,15:415-422.VM Maliy,IP Bogdanova.High-intensity magnetic separation of limonite iron ores[J].Magnetic and Electrical Separation,1992:315-319.
    [11]谢富良.铁坑褐铁矿选矿新工艺研究[J].冶金矿山设计与建设,1996(5):19-211
    [12]李永聪,孙福印.新疆某褐铁矿的选矿工艺研究[J].金属矿山,2002(6):29-31
    [13]王毓华,陈兴华等.褐铁矿反浮选脱硅新工艺试验研究[J].金属矿山,2005(7):37-39
    [14]绍良,毛益平,储德应.梅山铁精矿粗细分级选别降磷研究[J].金属矿山,1995,(03)43-47.
    [15]孙炳泉.我国复杂难选铁矿石选矿技术进展[A].2005年全国选矿高效节能技术及设备学术研讨与成果推广交流会论文集[C],2005.
    [16]张芹,张一敏等.湖北巴东鲕状赤铁矿选矿试验研究[A].2006年全国金属矿节约资源及高效选矿加工利用学术研讨与技术成果交流会论文集[C],2006.
    [17]肖巧斌,戈保粱,等.云南某鲕状赤铁矿选矿试验研究[A].2005年全国选矿高效节能技术及设备学术研讨与成果推广交流会论文集[C],2005.
    [18]朱江,萧敢等.湖此宜昌某高磷赤铁矿的选矿工艺研究[J].金属矿山,2006(8):189-191
    [19]Forssberg R,Asolfsson G.Dephosphorisation of high-phosphorus iron ores by means of acid leaching[J].Erzmetal.1981,34:316-322.
    [20]Mamoun Muhammed and Yu Zhang.A hydrometallurgical process for the dephosphorization of iron ore.Hydrometallurgy,1989,21(3):277-292.
    [21]Cheng C Y,Misra V N,Clough J.Dephosphorisation of western australian iron ore by hydrometallurgicai process[J].Minerals Engineering,1999,12(9):1083-1092.
    [22]B.D.Sparks,A.F.Sirianmi.Benefication of a phosphoriferous iron ore by agglomeration metaods.International Journal of Mineral Processing,1974,1(3):231-241.
    [23]Yongshi Jin,Tao Jiang,Yongbin Yang,et al.Removal of phosphorus from iron ores by chemical leaching.The Chinese Journal of Nonferrous Metals,2006,(6):673-677.
    [24]卢尚文,张邦家.宁乡式胶磷铁矿用解胶浸矿法降磷的研究[J].金属矿山,1994,(08):57-61.
    [25]童雄,黎应书.难选鲕状赤铁矿石的选矿新技术试验研究[J].中国工程科学,2005,(S1)
    [26]闫武,张裕书.鄂西难选鲕状铁矿脱泥-反浮选试验研究[A].2008年全国金属矿山难选矿及低品位矿选矿新技术学术研讨与技术成果交流暨设备展示会论文集[C],2008]
    [27]Chudacek,M.W.,Fiehera,M.A.The relationship between the test tube-flotability test and batch cell flotation[J].Minerais Engineering.,1991.4(1):25-35.
    [28]Wang,Q.,Heiskanen,K.Selective hydrophobic flocculation in apatite-hematite system by sodium oleate[J].Minerals Engineering.,1992.5(3-5):493-501.
    [29]Antti,B.M.,Forssberg,E.Pulp chemistry inindustrial mineral flotation.Studieof surface complex on calcite and apatite surface using FTIR spectroscoPy[J].Minerals Engineering,1989.2(2):217-227.
    [30]Hanuumantha Rao,K.,Forssberg,K.S.E.mechanism of fatty acid adsorption in salt-type mineral flotation[J].Minerals Engineering,1991.4(4-7):879-890.
    [31]Yehia,A.,Miller,J.D.,Ateya,B.G.Analysis of the adsorption,behaviour of Oleate on Some Synthetic apatites[J]..Minerals Engineering.,1993.6(1 ):79-86.
    [32]Pavez,O.,Peres,A.E.C.Effect of sodium metasilieate and sodium sulphide on the floatability of monazite-zireon-rutile with oleate and hydroxamates[J].Minerals Engineering.,1993.6(1):69-78.
    [33]Pavez,O.,Brandao,P.R.G.,Peres,A.E.C.Adsorption ofoleate and octyl-hydroxamate on to rare-earths minerals[J].Minerals Engineering.,1996.9(3):357-366.
    [34]De Castro,F.H.B.,de Hoees,M.C.,Borrego,A.G.The effcet of PH modifier on the flotation of celestite with sodium oleate and sodium metasilieate[J].Minerals Engineering.,1998.11(10):989-992.
    [35]Liu,Q.,Peng,Y.The development of composite collceter for the flotation of rutile[J].Minerals Engineering.,1999.12(12):1419-1430.
    [36]Rodrigues,A.J.,Brandao,P.R.G.The influence of crystal chemistry properties on the floatability of apatites with sodium oleate[J].Minerals Engineering,1993.6(6):643-653.
    [37]Valdiviezo,E.,Oliveira,J.F Synergism in aqueous solutions of sufactant mixtures and its effcet on the hydrophobieity of mineral surfaecs[J].Minerals Engineering.,1993.6(6):655-661.
    [38]Sis,H.,Chander,S.Adsorption and contact angle of single and binary mixtures of surfactants on apatite[J].Minerals Engineering.,2003.16(9):839-848.
    [39]Sis,H.,Chander,S..Improving froth characteristics and flotation recovery of phosphate ores with nonionie surfactants[J].Minerals Engineering.,2003.16(7):587- 595.
    [40]Orhan,E.C.,Bayraktar,I.Amin-oleate interations in feldspar flotation[J].Minerals Engineering.,2005.InPress,Correeted Proof.
    [41]张泾生,阙煊兰.矿用药剂[M]冶金工业出版社,2008:125-126.
    [42]Han,K.N.et.al.J.ofColloidandInterf.Sei.,1973.44:407-408
    [43]陈让怀.羧酸类捕收剂改性研究进展[J].矿冶工程,1994.14(1):34-38.
    [44]林祥辉,靳芳琳等.靳芳琳等.新型铁矿捕收剂的研制及应用[J].矿冶工程,1986,6(4):35-38.
    [45]翟芝明等.新型高效捕收剂EM-2及其在包头矿石浮选中的应用[J].矿冶工程,1992.12(1):55-57.
    [46]陈远道,卢毅屏.改善羧酸类捕收剂浮选性能的方法[J].国外金属选矿,1986,4(3):22-26.
    [47]Glebosky,A.V.苏联硫化矿和非硫化矿新浮选药剂[J]国外金属矿选矿,1989.(5):1-6.
    [48]Samuel SW,et.al.Process for froth flotation of non-sulfide minerals[P]美国专利:4186083
    [49]Wang,s.s.,L.Eugene,s.j.,Huliganga,F.E.Process for froth flotation of non-sulfide minerals [P].U.S.A,1980.
    [50]陈竞清.脂肪酸类型捕收剂研究概况[J].矿业工程,1986.
    [51]纳加雷DR等.非硫化矿浮选综述[J]国外金属矿选矿,2002,39(4)4-8.
    [52]朱建光,赵景云.6RO-X系列捕收剂浮选含钙矿物[J].化工矿山技术,1990,19(6):32-34.
    [53]朱玉霜,朱建光.浮选药剂的化学原理(修订版)[M].长沙:中南一工业大学出版社.1996
    [54]朱建光.浮选药剂技术讲座-第一讲羧酸捕收剂[J].金属矿山,1988(5):63-67
    [55]晨杨.用新的阴离子捕收剂浮选锡石[J].国外金属矿选矿,1976.(11-12):71-72.
    [56]Dennis G等.《C.A.》1981;95:11888/C
    [57]朱建光.化工矿山技术.1988:(2):19
    [58]任俊.矿产综合利用[J].1990,(2):15.
    [59]穆同娜,张惠等.油脂的氧化机理及天然抗氧化物的简介[J].食品科学,2004,25:241-244.
    [60]孙丽芹,董新伟,刘玉鹏,姜爱莉,王凤玲,翁新楚.脂类的自动氧化机理[J].中国油脂,1998,(05)
    [61]周华龙,张新申等.不饱和油脂氧化机理的研究与技术开发(Ⅰ)氧化机理研究中的几个重要问题[J].中国皮革,2003,31(11):26-30.
    [62]周华龙.不饱和油脂氧化机理的研究与技术开发(Ⅱ)_油脂游离基的反应特点与技术开发[J].中国皮革,2003,32(13):4-8.
    [63]石云良,陈淳.石英的油酸盐浮选化学[J].有色金属,1999,51(1):31-34.
    [64]石云良,邱冠周.石英浮选中的表面化学反应[J].矿业工程,2001,21(3):43-45.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700