多聚磷酸脱砷工艺探讨
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
随着精细磷化工的不断发展,作为新的基础原料酸一多聚磷酸其纯度受到了广泛关注,因为纯度直接决定产品用途。元素砷是衡量磷酸纯度的重要指标之一,也是最难除去的杂质之一,因此如何降低多聚磷酸中的砷含量以达到低砷(≤10ppm)磷酸的要求是目前研究的热点也是难点。本论文便是根据这种需求,同时鉴于目前国内还未见这方面的报道,对多聚磷酸脱砷工艺进行探讨。
     论文首先通过各种磷酸脱砷工艺路线的比较,结合多聚磷酸的特点以及砷可能脱除的形式,确定了多聚磷酸脱砷的工艺方法一卤化物法,这是一种新的无需过滤及后处理的方法;同时考察了脱砷剂的选择、反应温度、反应时间、搅拌速率以及脱砷剂用量等因素对脱砷效果的影响;通过正交实验获得了最佳的工艺条件:
     1.以卤化氢气体为脱砷剂的最佳工艺条件:
     反应温度:150℃;反应时间:60min;搅拌速率:250 rpm;脱砷剂用量为多聚磷酸质量的0.8%。
     2.以氢卤酸为脱砷剂的最佳工艺条件:
     反应温度:135℃;反应时间:5min;搅拌速率:250 rpm;脱砷剂用量为多聚磷.酸质量的1.5%。
     通过前面两种脱砷剂处理后的多聚磷酸中的砷含量分别为:3.9ppm和2.8ppm,都达到了低砷酸的要求,产品回收率可达98%以上。在此基础上研究了如何拓宽此工艺方法的应用范围。
     另外,从热力学的角度对多聚磷酸脱砷反应机理作了初步探讨,对今后的研究工作有一定的指导意义。
Developing of the fine phosphorus chemical industry, the purity of polyphosphoric acid as a new , basis, raw material has been concerned widly, because the end use depends on its degree of purification . The element arsenic is not only one of important indicators on studying the degree of purification of phosphoric acid, but also one of the impurities that remove difficultly, thus how to reduce the content of arsenic of polyphosphoric acid to achieve the requirement of low arsenic (≤10ppm) phosphoric acid is a hot and difficult research currently . This paper is related to arsenic removal process of polyphosohoric acid , which is based on mentioned demand earlier, and in the light of no reports in this regard at present .
     In this paper, compared with various kinds of arsenic removal process of phosphoric acid, considered the characteristic of polyphosphoric acid, and the form of arsenic removal possible, at last define the arsenic removal process of polyphosphoric acid-halide process, this is a new process without filtration and treatment method; Inspect some factors, which contained how to choice arsenic removal substance, reaction temperature, reaction time, stirring rate as well as the amount of arsenic removal substance and so on, they effect arsenic removal simultaneously; Obtain the best conditions by orthogonal experiment.
     When hydrogen-halogenated is arsenic removal substance, the optimum conditions are reaction temperature: 150℃, reaction time: 60min, stirring rate: 250rpm and the amount of arsenic removal substance: 0.8%(w%).
     When Hydrohalogenic acid is arsenic removal substance, the optimum conditions are reaction temperature: 135℃, reaction time: 5min, stirring rate: 250rpm and the amount of arsenic removal substance: 1.5%(w%).
     The content of arsenic in polyphosphoric acid are 3.9ppm and 2.8ppm by the front arsenic removal process respectively, which have been reached a low arsenic trioxide requirements, the recovery rate is more than 98%. On the basis of this, study the process of how to broaden the scope of the application.
     Furthermore , discuss the reaction mechanism of arsenic removal of polyphosphoric acid from the perspective of thermodynamics preliminarily . This paper will have certain guiding sense to the future work.
引文
[1]A.V斯拉克[美],陈明磊等译.磷酸[M].北京:石油化学工业出版社,1997
    [2]周吉光,易婵娟.多磷酸的名称及含量与分析方法[J].磷酸盐工业,2000,1:13-16
    [3]《化肥工业大会》编辑委员会.化肥工业大全[M].北京:化学工业出版社,1988
    [4]R.A.Valieva,G.E.Kuznetsova,V.P.Evstigneeva.Corrosion resistance of some construction and sealing materials in 116%polyphosphoric acid at high temperatures.Corrosion and Protection of Chemical Equipment,1980,1:608-609
    [5]陈嘉甫,谭光薰.磷酸盐的生产与使用[M].成都科技大学出版社,1989
    [6]赵海燕.过磷酸在国内外应用[J].云南化工,2001,1:10-14
    [7]F·拉什奇等.聚磷酸盐化学基础及其在选矿中应用的评述[J].国外金属矿选矿,2000,11:2-9
    [8]陈福泉,翟励强,陈树明.聚磷酸盐复盐[J].磷酸盐工业,1998,3:23-25
    [9]Fredic B.Clarke,John W.Lyons.The alcoholysis of polyphosphoric acid.Research Department,Inorganic Chemical Division,1966,108:4401-4405
    [10]张宝昌,于祥.高聚物改性沥青稳定性研究[J].石油沥青,2007,6:13-16
    [11]白锡柱,曾寿智.磷酸生产技术开发的进展[J].硫磷设计与粉体工程,2006,5:1-5
    [12]陈五平主编,无机化工工艺学(三)化学肥料[M].北京:化学工业出版社.1989
    [13]陈善继.中国热法磷酸的发展前景[J].中国化工学会无机盐学术年会,2003:30-35
    [14]Robert B.Hudson,Kirkwood.Method of preparing ultraphosphoric acid [P].US 4309394,1982-01-05
    [15]陈雪萍.湿法磷酸净化研究[D]:[硕士学位论文].昆明:昆明理工大学,2007
    [16]Myers,Dennis L.,Hudson,Robert W.Method for making polyphosphoric acid[P].US 20030035768,2003-02-20
    [17]陈善继.中国热法磷酸生产现状概述[J].磷肥与复肥,2004,5:49-51
    [18]轻工业编辑.日用化工理化数据手册[M].轻工业出版社,1981
    [19]R.G.Dowing,D.E.Pearson.The apparent acidity function(H_0)of polyphosphoric acid.Department of chemistry,Vanerbilt University,Nashville 5,Texn,1961,83:1718-1721
    [20]Frank D.POPP and William E.MCEWEN.Polyphosphoric acid as a reagent in organic chemistry[M].Department of chemistry,University of Kansas,1967
    [21]J.R.Van Wazer.Phosphorus and its compounds.Interscience Publishers,1958,1:1580-1588
    [22]John Koo.Studies in polyphosphoric acid cyclizations.National Cancer Institute,National Institutes of Health,1952,75:1891-1889
    [23]相政乐,马沛生,冯丽梅.环己酮-环己烷混合液密度和粘度的测定及关联[J].化学工业与工程,2006,5:415-419
    [24]姚玉英,黄凤廉,陈常贵等编.化工原理(上册)[M].天津:天津科学技术出版社,2001
    [25]V.A.Platonov.Properties of polyphosphoric acid.Fibre Chemistry,2000,5:325-329
    [26]马沛生 编著.化工数据[M].北京:中国石化出版社,2003
    [27]Jong-Beom Baeka,Soo-Young Parkb,Gary E.Pricec.Unusual thermal relaxation of viscosity-and-shear-induced strain in poly synthesized in highly viscous polyphosphoric acid/P205 medium.Polymer,200546:1543-1552
    [28]莫笑萍,胡山鹰,沈静珠.我国磷资源产业的发展[J].化工矿物与加工,2005,8:1-4
    [29]华小西.磷化工2020年发展规划[J].无机盐技术,2004,5:30-33
    [30]Kiyooshi Hotta,Fukui(JP)and Fuyuhiko Kubota.Method for purification of phosphoric acid purity polyphosphoric acid[P].US 6861031,2005-03-01
    [31]汤德元,汤敏.低砷黄磷的生产途径[J].贵州化工,1995,1:19-23
    [32]李瑞英.低砷磷酸产品开发的技术探讨[J].磷酸盐工业,2003,1:20-23
    [33]刘定富,敖先权,何强民.黄磷脱砷的试验研究[J].贵州化工,1999,1:13-15
    [34]邱立萍.砷污染危害及治理技术[J].新疆环境保护,1999,3:15-19
    [35]山根靖弘[日]等编著,贺振东等译.环境污染物质与毒性:无机篇[M].成都:四川科学技术出版社,1981
    [36]苏毅,李国斌,杨万明等.黄磷净化脱砷研究进展[J].云南化工,1998,2:3-6
    [37]Gotoh,Hideto and Takayuki.Cleaning method[P].JP 309172,2000-10-10
    [38]赵延仁,刘建清,尹其光.湿法磷酸精制技术的现状与进展[J].化工进展,1992,3:45-49
    [39]Schimmel,Gradl and Heymer.Process for removing heavy metal ions and arsenic from wet-processed phosphoric acid[P].US 4466948,1984-04-21
    [40]Roy A.Hutchins.Marketplace accepts purified wet-process phosphoric acid[J].Fertilizer Research 36:193-201,1993
    [41]张允湘,钟本和,罗洪波.磷酸的净化方法评述[J].磷酸盐工业,2001,2:21-25
    [42]Ekaterinia IV.Todorova & Ivan P.Dombalov.Production of phosphoric acid with low content of impurities.Fertilizer Research,1995,41:125-128
    [43]J.M.Bisang,F.Bogado,M.O.Rivera and O.L.Dorbessan.Electrochemical removal of arsenic from technical grade phosphoric acid.Journal of Applied Electrochemistry,2004,34:375-381
    [44]Ernest O.Kartinen and Christopher J.Martin.An overview of arsenic removal processes[J].Desalination 103:79-88,1995
    [45]黄伟九,张俊.溶剂沉淀法净化湿法磷酸技术的现状与进展[J].化工进展,1997,6:39-43
    [46]申士富,孙传尧.溶剂萃取法净化磷酸的研究[J].矿冶,2004,3:42-46
    [47]J.I.Skorovarov,L.I.Ruzin and A.V.Lomonosov.Solvent extraction for cleaning phosphoric acid in fertilizer production.Journal of Radioanalytical and Nuclear Chemistry,1998,229:111-116
    [48]赵显铭,段建兴.离子交换法除热法磷酸中的硫酸根的研究[J].无机盐工业,1989,3:31-33
    [49]M.P.Gonzalez,R.Navarro,I.Saucedo,M.Avila and J.Revilla.Purification of phosphoric acid solutions by reverse osmosis.Desalination,2002, 147:315-320
    [50]高洁.浅谈湿法磷酸的净化[J].化学矿物与加工,2004,7:37-39
    [51]Tadeusz K.Wiewiorowski and Phillip D.Molleve.Phosphoric acid crystallization process[P].US 4655789,1987-04-07
    [52]蒋丽红.结晶法净化湿法磷酸复合分解生产磷酸钾盐的研究[D]:[硕士学位论文],成都:四川大学,2000
    [53]化学工业标准汇编,无机化工[M].中国标准出版社,1995
    [54]化学工业标准汇编,食品添加剂[M].中国标准出版社,1996
    [55]化学工业部化肥司,中国磷肥工业协会,磷肥和复合肥料生产分析规程[M].北京:化学工业出版社,1993:72-73,422
    [56]单云,贺与平,熊敏等.氢化物发生原子荧光光谱法测定磷酸中的砷[J].分析试验室,2003,3(22):65-67
    [57]罗江琳,邬振宇,熊艳生等.双光道原子荧光光谱同时测定食品中砷和铅的方法研究[J].中国卫生检验杂志,2007,6:1136-1137
    [58]山西省忻州市质量技术监督检验测试所.原子荧光法测定饲料添加剂中的砷[J].上海计量测试,2006,6:30-31
    [59]宋吉利,于春夏,于作文等.微波消解-原子荧光光谱法同时测定有机-无机复混肥料中砷和汞的含量[J].磷肥与复肥,2006,11:65-67
    [60]张毅民,姜晖,吕学斌等.用ICP-AES方法测定淀粉中铅、砷的含量[J].光谱学与光谱分析,2006,3(26):554-556
    [61]骆德池.由工业磷酸连续操作生产食品级磷酸[J].硫磷设计与粉体工程,2005,6:27-29
    [62]Maurer,Alexander & Heymer.Process for dearsenification of polyphosphoric acid[P].US 4399114,1983-08-16
    [63]王永福.热法工业磷酸的脱砷试验[J].磷酸盐工业,2001,4:21-23
    [64]骆德池.浅谈连续热法食品磷酸生产[J].贵州化工,2005,4:27-29
    [65]Horst Dieter Wasel-Nielen,Erftstadt-Lechenich and Gero Heymer.Process for the continuous dearsenification of polyphosphoric acid[P].US 3790661,1974-02-05
    [66]Wolfgang Scheibitz,Leverkusen and Hasso Spott.Process for the dearsenication of polyphosphoric acid[P].US 3991164,1976-11-09
    [67]Luis Cumbal and Arup K.Sengupta.Arsenic removal using polymer supported hydrated iron oxide.Environ.Sci.Technol,2005,39:6508-6515
    [68]任露泉 编著.实验优化设计与分析[M].北京:高等教育出版社,2003
    [69]李伯骥 编著.化学化工实验师手册[M].大连:大连理工大学出版社,1996
    [70]袁一,胡德生 编著.化工过程热力学分析法[M].北京:化学工业出版社,1985
    [71]J.M.史密斯,H.C.范奈司 著.化工热力学导论第三版[M].北京:化学工业出版社,1982
    [72]李秋荣,郑海武,白明华.三种脱硫剂的脱硫反应的热力学分析及机理研究[J].燕山大学学报,2007,2(31):142-147
    [73]叶大伦 编著.实用无机物热力学数据手册[M].冶金工业出版社,1981
    [74]石宏奎.原子荧光法分析地表水中砷的价态[J].内蒙古环境科学,2007,3:87-89
    [75]陈锦风,高国伟.氢化物发生-原子荧光光谱法测定土壤中水溶态As(Ⅲ)和As (Ⅴ)的方法研究[J].江西化工,2005,2:78-81

© 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