CN103303979B - Tungsten oxide (WO3) nanopowder prepared by pyrolysing method - Google Patents
Tungsten oxide (WO3) nanopowder prepared by pyrolysing method Download PDFInfo
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- CN103303979B CN103303979B CN201310252868.6A CN201310252868A CN103303979B CN 103303979 B CN103303979 B CN 103303979B CN 201310252868 A CN201310252868 A CN 201310252868A CN 103303979 B CN103303979 B CN 103303979B
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- Prior art keywords
- apt
- citric acid
- ammonium paratungstate
- tungsten oxide
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- 238000000034 method Methods 0.000 title claims description 13
- 239000011858 nanopowder Substances 0.000 title abstract 2
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 title abstract 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 72
- XAYGUHUYDMLJJV-UHFFFAOYSA-Z decaazanium;dioxido(dioxo)tungsten;hydron;trioxotungsten Chemical compound [H+].[H+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O XAYGUHUYDMLJJV-UHFFFAOYSA-Z 0.000 claims abstract description 54
- 239000000843 powder Substances 0.000 claims abstract description 21
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 13
- 239000001301 oxygen Substances 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 238000007669 thermal treatment Methods 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims description 26
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims description 25
- 238000003756 stirring Methods 0.000 claims description 25
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 25
- 238000001035 drying Methods 0.000 claims description 10
- 238000000197 pyrolysis Methods 0.000 claims description 10
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000012141 concentrate Substances 0.000 claims description 5
- 239000012153 distilled water Substances 0.000 claims description 5
- 238000001704 evaporation Methods 0.000 claims description 5
- 230000008020 evaporation Effects 0.000 claims description 5
- 238000000227 grinding Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 2
- 239000011164 primary particle Substances 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 abstract description 11
- 239000000203 mixture Substances 0.000 abstract description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 2
- 229910021529 ammonia Inorganic materials 0.000 abstract 1
- 239000002243 precursor Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 description 5
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 4
- 229910052721 tungsten Inorganic materials 0.000 description 4
- 239000010937 tungsten Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001698 pyrogenic effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Abstract
The invention relates to nanoscale tungsten oxide (WO3) powder and a pyrolysing preparation method thereof, wherein an optimized raw material composition consisting of ammonium paratungstate (APT), citric acid and ammonia in corresponding proportion is adopted, the molar ratio of APT and citric acid is 1.5, and parameters of a preparation process matched are used. The flow of oxygen based on per gram of precursor is 55ml/min, and the thermal treatment temperature is 520 DEG C, so that WO3 nanopowder with uniformly distributed grain size is obtained.
Description
Technical field
The present invention relates to a kind of Tungsten oxide 99.999 (WO
3) and preparation method thereof, the particularly Tungsten oxide 99.999 (WO for preparing of a kind of pyrolysis method
3) nanometer powder.
Background technology
Tungsten oxide 99.999 (WO
3) be yellow greenish powder, be a kind of important oxide compound of tungsten, at present mainly for the manufacture of W powder and WC powder, namely tungsten bar, tungsten filament and Wimet etc. are Tungsten oxide 99.999 (WO
3) primary terminal object.
Tungsten oxide 99.999 (WO now
3) preparation method's mainly fumed pyrogenic method, the raw material of wherein pyrolysis is then mainly concerned with ammonium paratungstate (APT) and wolframic acid (H
2wO
4), corresponding thermal decomposition type is respectively:
5(NH
4)
2O·12WO
3·5H
2O＝12WO
3+10NH
3+10H
2O (1)，
H
2WO
4＝WO
3+H2O (2)，
But the Tungsten oxide 99.999 (WO that above-mentioned pyrolysis method is obtained
3) granularity is comparatively thick, the product granularity that usual APT raw material obtains is at 10-20 μm, and the product granularity that wolframic acid raw material obtains is at 3-10 μm.And in order to obtain chemically reactive higher in following process process, with to the better promoter action of the alloy of some particular requirements, often require Tungsten oxide 99.999 (WO
3) there is thinner granularity and larger specific surface area, this makes the Tungsten oxide 99.999 (WO prepared by traditional pyrolysis method
3) being more and more difficult to meet must demand in granularity.People have started research steering other Tungsten oxide 99.999 (WO
3) preparation method, such as vapor phase process, although but vapor phase process etc. can obtain the Tungsten oxide 99.999 (WO of more meticulous such as tens of nm
3) powder, but its preparation cost significantly rises compared to pyrolysis method, and industrialized scale is also difficult to meet the demands.
For this reason, improve pyrolysis method and produce Tungsten oxide 99.999 (WO
3) fine degree, thus obtain one can meet granularity requirements, also can adapt to the cost-effective Tungsten oxide 99.999 (WO of output needs
3) production method and corresponding product, become technical problem urgently to be resolved hurrily.
Summary of the invention
Namely object of the present invention is to provide one can prepare nanoscale tungsten (WO
3) the pyrolysis preparation method of powder and obtained Tungsten oxide 99.999 (WO thereof
3) powder.
For achieving the above object, the technical solution used in the present invention is:
A kind of Tungsten oxide 99.999 (WO
3) nanometer powder and pyrolysis preparation method thereof, described powder is obtained by following steps:
First, select the high-purity ammonium paratungstate (APT) of granularity about 5 μm as reaction raw materials, in reaction vessel, add distilled water, and adopt magnetic stirrer to stir, add citric acid solution while stirring;
The second, wait for that citric acid solution all dissolves and after mixing, adds high-purity ammonium paratungstate (APT) while stirring in reaction vessel;
3rd, add ammoniacal liquor after high-purity ammonium paratungstate (APT) adds, stir and obtain reaction soln;
4th, described reaction soln is placed in container for evaporation and concentrates, the concentrated concentrated solution obtained carries out drying and obtains presoma in drying plant at 150-160 DEG C;
5th, presoma is pulverized in grinding plant, puts into the crucible being connected with oxygen subsequently and heat-treat, finally obtain Tungsten oxide 99.999 (WO
3) nanometer powder;
The purity of wherein said high-purity ammonium paratungstate (APT) is greater than 99.9wt%, and the add-on of described citric acid solution is calculated as 1-3 with ammonium paratungstate (APT) and the mol ratio of citric acid; The concentration of described ammoniacal liquor is 30%; Described stirring velocity is 180-200r/min; During described thermal treatment, calculate the flow of oxygen for 50-60ml/min with every g presoma, temperature is 500-520 DEG C, and the time is 1.2-1.5h.
Preferably, the add-on of described citric acid solution is calculated as 1.5 with ammonium paratungstate (APT) and the mol ratio of citric acid, and describedly calculates the flow of oxygen for 55ml/min with every g presoma, and described thermal treatment temp is 520 DEG C.
Advantage of the present invention is: have employed preferred raw material composition and corresponding proportioning, mainly the selecting of ammonium paratungstate (APT) and citric acid, and the two suitable proportioning, and preparation technology parameter with matching, the mainly flow of oxygen and thermal treatment temp, obtains the Tungsten oxide 99.999 (WO of uniform particle sizes distribution
3) nanometer powder.
Accompanying drawing explanation
Fig. 1 is the Tungsten oxide 99.999 (WO that the present invention obtains
3) the SEM photo of nanometer powder.
Embodiment
Below, by specific embodiment 1-3, the present invention is described in detail.
Embodiment 1.
First, select the purity of granularity about 5 μm to be greater than the ammonium paratungstate (APT) of 99.9wt% as reaction raw materials, in reaction vessel, add distilled water, and adopt magnetic stirrer to stir, stirring velocity is 180-200r/min, adds citric acid solution while stirring;
The second, wait for that citric acid solution all dissolves and after mixing, adds high-purity ammonium paratungstate (APT) while stirring in reaction vessel, final ammonium paratungstate (APT) is calculated as 3 with the mol ratio of citric acid;
3rd, add the ammoniacal liquor that concentration is 30% after high-purity ammonium paratungstate (APT) adds, stir and obtain reaction soln;
4th, described reaction soln is placed in container for evaporation and concentrates, the concentrated concentrated solution obtained carries out drying and obtains presoma in drying plant at 150-160 DEG C;
5th, presoma is pulverized in grinding plant, puts into subsequently to be connected with and calculate with every g presoma the crucible that the flow of oxygen is 60ml/min oxygen and heat-treat in 510 DEG C, finally obtain Tungsten oxide 99.999 (WO
3) nanometer powder.
Embodiment 2.
First, select the purity of granularity about 5 μm to be greater than the ammonium paratungstate (APT) of 99.9wt% as reaction raw materials, in reaction vessel, add distilled water, and adopt magnetic stirrer to stir, stirring velocity is 180-200r/min, adds citric acid solution while stirring;
The second, wait for that citric acid solution all dissolves and after mixing, adds high-purity ammonium paratungstate (APT) while stirring in reaction vessel, final ammonium paratungstate (APT) is calculated as 1.5 with the mol ratio of citric acid;
3rd, add the ammoniacal liquor that concentration is 30% after high-purity ammonium paratungstate (APT) adds, stir and obtain reaction soln;
4th, described reaction soln is placed in container for evaporation and concentrates, the concentrated concentrated solution obtained carries out drying and obtains presoma in drying plant at 150-160 DEG C;
5th, presoma is pulverized in grinding plant, puts into subsequently to be connected with and calculate with every g presoma the crucible that the flow of oxygen is 55ml/min oxygen and heat-treat in 520 DEG C, finally obtain Tungsten oxide 99.999 (WO
3) nanometer powder.
Embodiment 3.
First, select the purity of granularity about 5 μm to be greater than the ammonium paratungstate (APT) of 99.9wt% as reaction raw materials, in reaction vessel, add distilled water, and adopt magnetic stirrer to stir, stirring velocity is 180-200r/min, adds citric acid solution while stirring;
The second, wait for that citric acid solution all dissolves and after mixing, adds high-purity ammonium paratungstate (APT) while stirring in reaction vessel, final ammonium paratungstate (APT) is calculated as 1 with the mol ratio of citric acid;
3rd, add the ammoniacal liquor that concentration is 30% after high-purity ammonium paratungstate (APT) adds, stir and obtain reaction soln;
4th, described reaction soln is placed in container for evaporation and concentrates, the concentrated concentrated solution obtained carries out drying and obtains presoma in drying plant at 150-160 DEG C;
5th, presoma is pulverized in grinding plant, puts into subsequently to be connected with and calculate with every g presoma the crucible that the flow of oxygen is 50ml/min oxygen and heat-treat in 500 DEG C, finally obtain Tungsten oxide 99.999 (WO
3) nanometer powder.
The product obtained after embodiment 1-3 reaction is Tungsten oxide 99.999 (WO through XRD diffraction test confirmation
3); Fig. 1 is the SEM photographic result of embodiment 2, can find out, the application preparation method obtains Tungsten oxide 99.999 (WO
3) nanometer powder has the size of about 20-50nm, and be primary particle substantially; In embodiment 1, because the ratio of citric acid is slightly low, the effect of its crystal grain thinning is abundant not, there is the offspring of a certain amount of cohesion, and in embodiment 3, because citric acid ratio is higher, thermal treatment also charge less divides, C in product, N content are high, remaining certain organism, also have a small amount of undecomposed ATB intermediate product.
Result above comprehensive is known, and the material rate in embodiment 2 and processing parameter obtain best preparation effect.
Claims (1)
1. Tungsten oxide 99.999 (the WO that a pyrolysis method is obtained
3) nanometer powder, it is characterized in that: obtained by following steps:
First, select the high-purity ammonium paratungstate (APT) of granularity 5 μm as reaction raw materials, in reaction vessel, add distilled water, and adopt magnetic stirrer to stir, add citric acid solution while stirring;
The second, wait for that citric acid solution all dissolves and after mixing, adds high-purity ammonium paratungstate (APT) while stirring in reaction vessel;
3rd, add ammoniacal liquor after high-purity ammonium paratungstate (APT) adds, stir and obtain reaction soln;
4th, described reaction soln is placed in container for evaporation and concentrates, the concentrated concentrated solution obtained carries out drying and obtains presoma in drying plant at 150-160 DEG C;
5th, presoma is pulverized in grinding plant, puts into the crucible being connected with oxygen subsequently and heat-treat, finally obtain Tungsten oxide 99.999 (WO
3) nanometer powder;
The purity of wherein said high-purity ammonium paratungstate (APT) is greater than 99.9wt%, and the add-on of described citric acid solution is calculated as 1.5 with ammonium paratungstate (APT) and the mol ratio of citric acid; The concentration of described ammoniacal liquor is 30%; Described stirring velocity is 180-200r/min; During described thermal treatment, calculate the flow of oxygen for 55ml/min with every g presoma, temperature is 520 DEG C, and the time is 1.2-1.5h; The particle diameter of described powder is 20-50nm, and is primary particle.
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|---|---|---|---|
| CN201310252868.6A CN103303979B (en) | 2013-06-24 | 2013-06-24 | Tungsten oxide (WO3) nanopowder prepared by pyrolysing method |
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|---|---|---|---|
| CN201310252868.6A CN103303979B (en) | 2013-06-24 | 2013-06-24 | Tungsten oxide (WO3) nanopowder prepared by pyrolysing method |
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| CN103303979B true CN103303979B (en) | 2015-07-22 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109641753A (en) * | 2016-09-15 | 2019-04-16 | H.C.施塔克钨业股份有限公司 | Novel tungsten-carbide powder and its preparation |
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|---|---|---|---|---|
| CN110563043B (en) * | 2019-09-29 | 2021-11-26 | 上海交通大学 | Method for preparing carbon film coated tungsten oxide nanospheres in one step by hydrothermal method and application thereof |
| CN113912125B (en) * | 2021-11-05 | 2023-08-04 | 赣州海盛钨业股份有限公司 | Calcination process for preparing high specific surface area low residual ammonia yellow tungsten oxide |
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| CN101381106B (en) * | 2007-09-05 | 2011-05-11 | 西南交通大学 | Method for preparing nano tungsten trioxide powder |
| CN101407339A (en) * | 2007-10-12 | 2009-04-15 | 新疆大学 | Method for synthesizing quadrangle tungsten oxide nano-powder |
| CN102485380B (en) * | 2010-12-06 | 2013-06-19 | 北京有色金属研究总院 | Preparation method of submicron nearly spherical tungsten powder |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109641753A (en) * | 2016-09-15 | 2019-04-16 | H.C.施塔克钨业股份有限公司 | Novel tungsten-carbide powder and its preparation |
| CN109641753B (en) * | 2016-09-15 | 2022-12-02 | H.C.施塔克钨业股份有限公司 | Tungsten carbide powder and preparation thereof |
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| ASS | Succession or assignment of patent right |
Owner name: ZHU LANYING Free format text: FORMER OWNER: LIU YAJING Effective date: 20150612 |
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Effective date of registration: 20150612 Address after: Yinzhou District Lianfeng road 315175 Zhejiang city of Ningbo Province, No. 886 Applicant after: Zhu Lanying Address before: 315100, No. 50, Heng Dong Road, Heng Gang Town, Yinzhou District, Zhejiang, Ningbo Applicant before: Liu Yajing |
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Effective date of registration: 20170117 Address after: Park No. 185 Pudong New Area road 201210 Mianyang Shanghai 2 C-5 Patentee after: Guoan (Shanghai) soil repair technology Co., Ltd. Address before: Yinzhou District Lianfeng road 315175 Zhejiang city of Ningbo Province, No. 886 Patentee before: Zhu Lanying |
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