CN103058724B - Preparation method of large-particle gadolinium oxide - Google Patents

Preparation method of large-particle gadolinium oxide Download PDF

Info

Publication number
CN103058724B
CN103058724B CN201210386973.4A CN201210386973A CN103058724B CN 103058724 B CN103058724 B CN 103058724B CN 201210386973 A CN201210386973 A CN 201210386973A CN 103058724 B CN103058724 B CN 103058724B
Authority
CN
China
Prior art keywords
gadolinium
concentration
hours
ammonia
macrobead
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201210386973.4A
Other languages
Chinese (zh)
Other versions
CN103058724A (en
Inventor
郝先库
张瑞祥
赵永志
汪立新
刘海旺
王士智
胡珊珊
马显东
许宗泽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINGRUI NEW MATERIAL CO Ltd BAOTOU
Original Assignee
JINGRUI NEW MATERIAL CO Ltd BAOTOU
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JINGRUI NEW MATERIAL CO Ltd BAOTOU filed Critical JINGRUI NEW MATERIAL CO Ltd BAOTOU
Priority to CN201210386973.4A priority Critical patent/CN103058724B/en
Publication of CN103058724A publication Critical patent/CN103058724A/en
Application granted granted Critical
Publication of CN103058724B publication Critical patent/CN103058724B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)

Abstract

The invention relates to a preparation method of large-particle gadolinium oxide, and belongs to a preparation technology of materials. The method comprises the following steps of: preparing an ammonium bicarbonate solution with ammonium bicarbonate, ammonia water and deionized water, adding gadolinium chloride solution to the ammonium bicarbonate solution to obtain a mixed solution of ammonium bicarbonate, ammonia water and gadolinium chloride, adding hydrogen peroxide to the mixed solution to generate an oxygen gadolinium carbonate precipitation, aging for 24-48 hours, filtering and washing the precipitation, and keeping the firing temperature at 900-1200 DEG C for thermal insulation for 4 hours to obtain the large-particle gadolinium oxide product, which has the characteristics of uniform particle, favorable liquidity, and the morphology of which appears to be a petal piled by sheet and the central grain size D50 of which is 120-240 micrometers.

Description

Prepare the method for macrobead gadolinium sesquioxide
Technical field
The present invention relates to a kind of method of preparing macrobead gadolinium sesquioxide, belong to a kind of material preparation process.
Background technology
Gadolinium sesquioxide is in field widespread uses such as catalysis, pottery, Solid Oxide Fuel Cell, luminescent material, polishing materials.For example gadolinium sesquioxide adulterated TiOx is made catalyzer can efficient degradation tropeolin-D, and gadolinium sesquioxide also can be used as the main component in solid fuel cell.Along with scientific and technological development, different technologies field has also proposed many requirements to gadolinium sesquioxide particle size.At present more to the research of nano level gadolinium sesquioxide, the research to macrobead gadolinium sesquioxide and preparation technology are relatively less.Granularity control and mensuration thereof when the gadolinium sesquioxide that document Deng Han celery is shown synthesizes, the tenth national rare earth elementary analytical chemistry symposium collection of thesis, 2003, provides gadolinium sesquioxide preparation method, prepare gadolinium oxalate precipitation with oxalic acid and Gadolinium trichloride, after gadolinium oxalate calcination, obtain 2-6 μ m gadolinium sesquioxide product; In rare-earth industry is produced, adopt oxalic acid, bicarbonate of ammonia, sodium carbonate as precipitation agent, Gadolinium trichloride is as feed liquid, and the gadolinium oxalate, the calcination of gadolinium carbonate precipitation process that obtain, obtain medium particle diameter D 50for the gadolinium sesquioxide product of 1-15 μ m.
Summary of the invention
The object of the present invention is to provide a kind of uniform particles, good fluidity, pattern is petal-shaped, the medium particle diameter D that thin slice builds up 50be the preparation method of the macrobead gadolinium sesquioxide of 120 μ m-240 μ m.
Technical solution: the present invention adds respectively ammoniacal liquor and the deionized water that bicarbonate of ammonia, concentration are 28% in reactor, the mol ratio of bicarbonate of ammonia, ammoniacal liquor and deionized water is 1: 1: 6.27, adding concentration is the Gadolinium trichloride solution of 1.09mol/L, bicarbonate of ammonia and Gadolinium trichloride mol ratio are 1: 0.031, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding concentration in mixing solutions, Gadolinium trichloride and hydrogen peroxide mol ratio are 1: 2.6, react 2.5 hours, ageing 24-48 hour, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 900-1200 DEG C, be incubated 4 hours, obtaining uniform particles, good fluidity, pattern is petal-shaped, the medium particle diameter D that thin slice builds up 50it is the macrobead gadolinium sesquioxide of 120 μ m-240 μ m.
Invention effect
In the present invention, peroxide gadolinium carbonate precipitation digestion time and calcination temperature are to prepare macrobead gadolinium sesquioxide key, in peroxide gadolinium carbonate preparation method, digestion time is the key factor that determines peroxide gadolinium carbonate granularity, digestion time is less than 4 hours, and peroxide gadolinium carbonate deposit seeds is very thin, sad filter, static ageing is more than 24 hours, obtain macrobead peroxide gadolinium carbonate, peroxide gadolinium carbonate is at 900-1200 DEG C at calcination temperature, obtains medium particle diameter D 50for the gadolinium sesquioxide product of 120-240 μ m, control peroxide gadolinium carbonate precipitation digestion time and calcination temperature, can prepare varying particle size, uniform particles, good fluidity, pattern is that thin slice builds up petal-like gadolinium sesquioxide product, and this technique is convenient to realize suitability for industrialized production.
Brief description of the drawings
Fig. 1 is the XRD figure of macrobead gadolinium sesquioxide of the present invention;
Fig. 2 is the particle size distribution figure of macrobead gadolinium sesquioxide of the present invention;
Fig. 3 is the SEM figure of macrobead gadolinium sesquioxide of the present invention.
Embodiment
Embodiment 1
In reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react 2.5 hours, ageing 24 hours, obtains peroxide gadolinium carbonate precipitation, and by sedimentation and filtration, washing, calcination temperature is 900 DEG C, insulation 4h, and obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 124.0 μ m.
Embodiment 2
In reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 32 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1000 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 158.4 μ m.
Embodiment 3
In reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 44 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1100 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 191.4 μ m.
Embodiment 4
In reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300m1 concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 48 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1200 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 240.7 μ m.

Claims (4)

1. prepare the method for macrobead gadolinium sesquioxide, it is characterized in that, in reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react 2.5 hours, ageing 24 hours, obtains peroxide gadolinium carbonate precipitation, and by sedimentation and filtration, washing, calcination temperature is 900 DEG C, insulation 4h, and obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 124.0 μ m.
2. prepare the method for macrobead gadolinium sesquioxide, it is characterized in that, in reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 32 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1000 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 158.4 μ m.
3. prepare the method for macrobead gadolinium sesquioxide, it is characterized in that, in reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 44 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1100 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 191.4 μ m.
4. prepare the method for macrobead gadolinium sesquioxide, it is characterized in that, in reactor, add ammoniacal liquor and deionized water 520ml that 350g bicarbonate of ammonia, 300ml concentration are 28%, then to add 125ml concentration be the Gadolinium trichloride solution of 1.09mol/L, obtain the mixing solutions of bicarbonate of ammonia, ammoniacal liquor and Gadolinium trichloride; Be 30% hydrogen peroxide to adding 36ml concentration in mixing solutions, react ageing 48 hours 2.5 hours, obtain peroxide gadolinium carbonate precipitation, by sedimentation and filtration, washing, calcination temperature is 1200 DEG C, insulation 4h, obtaining medium particle diameter is the macrobead gadolinium sesquioxide of 240.7 μ m.
CN201210386973.4A 2012-09-22 2012-09-22 Preparation method of large-particle gadolinium oxide Active CN103058724B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210386973.4A CN103058724B (en) 2012-09-22 2012-09-22 Preparation method of large-particle gadolinium oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210386973.4A CN103058724B (en) 2012-09-22 2012-09-22 Preparation method of large-particle gadolinium oxide

Publications (2)

Publication Number Publication Date
CN103058724A CN103058724A (en) 2013-04-24
CN103058724B true CN103058724B (en) 2014-12-03

Family

ID=48101659

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210386973.4A Active CN103058724B (en) 2012-09-22 2012-09-22 Preparation method of large-particle gadolinium oxide

Country Status (1)

Country Link
CN (1) CN103058724B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108483480A (en) * 2018-04-11 2018-09-04 内蒙古科技大学 The method for preparing gadolinium oxide with plant precipitating reagent
CN109052450B (en) * 2018-09-17 2020-10-16 江苏国盛新材料有限公司 Preparation method of high-purity gadolinium oxide

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1075171A (en) * 1992-02-02 1993-08-11 包头钢铁稀土企业集团稀土冶炼厂 The production method of cerous hydroxide
JP2641108B2 (en) * 1990-06-21 1997-08-13 大日精化工業株式会社 Method for producing cerium oxide fine powder
CN1635169A (en) * 2003-12-30 2005-07-06 北京方正稀土科技研究所有限公司 Process for preparing cerous hydroxide
JP2007022836A (en) * 2005-07-14 2007-02-01 Sumitomo Osaka Cement Co Ltd Method of manufacturing rare earth element-added cerium oxide powder
JP3877922B2 (en) * 1998-12-24 2007-02-07 信越化学工業株式会社 Method for producing rare earth compound
CN101186327A (en) * 2006-11-16 2008-05-28 北京方正稀土科技研究所有限公司 Large granularity high apparent density rare earth oxide and preparation method thereof
CN101279858A (en) * 2008-01-08 2008-10-08 南开大学 Preparation of rare-earth oxide macroporous material
CN101475201A (en) * 2009-03-05 2009-07-08 中国科学院长春应用化学研究所 Preparation of Gd(OH)3 and Gd2O3 nano-tubu
JP4518844B2 (en) * 2004-06-11 2010-08-04 第一稀元素化学工業株式会社 Method for producing yttria sol
CN102060319A (en) * 2011-01-27 2011-05-18 南昌大学 Preparation method of cerous carbonate midbody
CN102391865A (en) * 2011-09-21 2012-03-28 中国科学院福建物质结构研究所 Preparation method for doping gadolinium oxide nano-powders

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2641108B2 (en) * 1990-06-21 1997-08-13 大日精化工業株式会社 Method for producing cerium oxide fine powder
CN1075171A (en) * 1992-02-02 1993-08-11 包头钢铁稀土企业集团稀土冶炼厂 The production method of cerous hydroxide
JP3877922B2 (en) * 1998-12-24 2007-02-07 信越化学工業株式会社 Method for producing rare earth compound
CN1635169A (en) * 2003-12-30 2005-07-06 北京方正稀土科技研究所有限公司 Process for preparing cerous hydroxide
JP4518844B2 (en) * 2004-06-11 2010-08-04 第一稀元素化学工業株式会社 Method for producing yttria sol
JP2007022836A (en) * 2005-07-14 2007-02-01 Sumitomo Osaka Cement Co Ltd Method of manufacturing rare earth element-added cerium oxide powder
CN101186327A (en) * 2006-11-16 2008-05-28 北京方正稀土科技研究所有限公司 Large granularity high apparent density rare earth oxide and preparation method thereof
CN101279858A (en) * 2008-01-08 2008-10-08 南开大学 Preparation of rare-earth oxide macroporous material
CN101475201A (en) * 2009-03-05 2009-07-08 中国科学院长春应用化学研究所 Preparation of Gd(OH)3 and Gd2O3 nano-tubu
CN102060319A (en) * 2011-01-27 2011-05-18 南昌大学 Preparation method of cerous carbonate midbody
CN102391865A (en) * 2011-09-21 2012-03-28 中国科学院福建物质结构研究所 Preparation method for doping gadolinium oxide nano-powders

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
Mari E. de Vasconcellos et al.Solubility behavior of rare earths with ammonium carbonate and ammonium carbonate plus ammonium hydroxide: Precipitation of their peroxicarbonates.《Journal of Alloys and Compounds》.2007, *
Solubility behavior of rare earths with ammonium carbonate and ammonium carbonate plus ammonium hydroxide: Precipitation of their peroxicarbonates;Mari E. de Vasconcellos et al;《Journal of Alloys and Compounds》;20070418;第426–428页 *
唐定骥等.稀土中间合金分析.《稀土金属材料》.冶金工业出版社,2011, *
氧化钆合成时粒度控制及其测定;邓汉芹等;《第十届全国稀土元素分析化学学术报告会议论文集》;20031231;第154-156页 *
沈旭.沉淀工艺.《化学选矿技术》.2011, *
王正德等.碳酸钆及氧化钆纳米管的合成及表征.《包头钢铁学院学报》.2004,第23卷(第2期), *
碳酸钆及氧化钆纳米管的合成及表征;王正德等;《包头钢铁学院学报》;20040630;第23卷(第2期);第122-125页 *
邓汉芹等.氧化钆合成时粒度控制及其测定.《第十届全国稀土元素分析化学学术报告会议论文集》.2003, *

Also Published As

Publication number Publication date
CN103058724A (en) 2013-04-24

Similar Documents

Publication Publication Date Title
CN108609666B (en) Preparation method of metal element gradient doped cobaltosic oxide
CN106346021B (en) A kind of method that high pressure hydrogen reduction prepares cobalt powder
CN102247858A (en) Aluminium oxide-nickel-rare earth catalytic composite membrane as well as preparation method and application thereof
CN103193225A (en) Preparation method for nano metal oxide graphene composite material
CN103058724B (en) Preparation method of large-particle gadolinium oxide
CN104478699A (en) Preparation method of high-purity superfine cobalt oxalate powder
CN102328961A (en) Precursor of nickel cobalt lithium manganate positive material for lithium ion battery and production method thereof
CN107413343B (en) Preparation method of magnetic cobaltosic oxide/cobalt hydroxide/reduced graphene oxide ternary heterojunction photocatalyst
CN102115214A (en) Method for preparing small-particle-size cobalt carbonate
CN103086416B (en) Preparation method of large-particle samarium oxide
CN102992379B (en) Method for preparing spherical macro-granular neodymium oxide
CN103406120A (en) HNTs/rare earth oxide composite material and its microwave preparation method
CN103011231B (en) Method for preparing multihole sheet large-grain praseodymium oxide
CN103058256B (en) Method for preparing large-granule dysprosium oxide
CN102992381B (en) Method for preparing macrogranular ytterbium oxide
CN100532277C (en) Process for preparing nano NiO by ammonia water single phase precipitation
CN102583571A (en) Wet chemical method for preparing Bi2Fe4O9 nanometer powder
CN102992380B (en) Method for preparing macrogranular europium oxide
CN104386732A (en) Method and system for preparing nano cerium oxide by adopting adsorption and isolation agent
CN104261455B (en) A kind of preparation method of high purity stannic acid lanthanum nano-powder
CN104649888A (en) Preparation method of large-particle neodymium oxalate
CN113877540A (en) Preparation method of prussian blue analogue-based composite adsorption material for cesium separation
CN104876284A (en) Nano bead chain cobaltosic oxide and preparation method thereof
CN103143350B (en) Preparation method of modified palladium metal catalysts, prepared catalyst and applications thereof
CN101950680A (en) Nano nickel oxide composite electrode for super capacitor and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant