CN110880606A - A kind of preparation method of high-purity vanadyl sulfate - Google Patents
A kind of preparation method of high-purity vanadyl sulfate Download PDFInfo
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- CN110880606A CN110880606A CN201911060998.3A CN201911060998A CN110880606A CN 110880606 A CN110880606 A CN 110880606A CN 201911060998 A CN201911060998 A CN 201911060998A CN 110880606 A CN110880606 A CN 110880606A
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- vanadyl sulfate
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- UUUGYDOQQLOJQA-UHFFFAOYSA-L vanadyl sulfate Chemical compound [V+2]=O.[O-]S([O-])(=O)=O UUUGYDOQQLOJQA-UHFFFAOYSA-L 0.000 title claims abstract description 35
- 229940041260 vanadyl sulfate Drugs 0.000 title claims abstract description 35
- 229910000352 vanadyl sulfate Inorganic materials 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 229910052720 vanadium Inorganic materials 0.000 claims abstract description 77
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims abstract description 76
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000002994 raw material Substances 0.000 claims abstract description 18
- 238000002386 leaching Methods 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 15
- 229930013930 alkaloid Natural products 0.000 claims abstract description 13
- 150000003797 alkaloid derivatives Chemical class 0.000 claims abstract description 12
- 239000013078 crystal Substances 0.000 claims abstract description 10
- 238000002425 crystallisation Methods 0.000 claims abstract description 8
- 230000008025 crystallization Effects 0.000 claims abstract description 8
- 238000001556 precipitation Methods 0.000 claims abstract description 6
- 239000002244 precipitate Substances 0.000 claims abstract description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 10
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 9
- ZFXYFBGIUFBOJW-UHFFFAOYSA-N theophylline Chemical compound O=C1N(C)C(=O)N(C)C2=C1NC=N2 ZFXYFBGIUFBOJW-UHFFFAOYSA-N 0.000 claims description 8
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 6
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 230000001376 precipitating effect Effects 0.000 claims description 5
- 229930003347 Atropine Natural products 0.000 claims description 4
- RKUNBYITZUJHSG-UHFFFAOYSA-N Hyosciamin-hydrochlorid Natural products CN1C(C2)CCC1CC2OC(=O)C(CO)C1=CC=CC=C1 RKUNBYITZUJHSG-UHFFFAOYSA-N 0.000 claims description 4
- RKUNBYITZUJHSG-SPUOUPEWSA-N atropine Chemical compound O([C@H]1C[C@H]2CC[C@@H](C1)N2C)C(=O)C(CO)C1=CC=CC=C1 RKUNBYITZUJHSG-SPUOUPEWSA-N 0.000 claims description 4
- 229960000396 atropine Drugs 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 229960000278 theophylline Drugs 0.000 claims description 4
- 235000021513 Cinchona Nutrition 0.000 claims description 3
- 241000157855 Cinchona Species 0.000 claims description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 3
- YBHILYKTIRIUTE-UHFFFAOYSA-N berberine Chemical compound C1=C2CC[N+]3=CC4=C(OC)C(OC)=CC=C4C=C3C2=CC2=C1OCO2 YBHILYKTIRIUTE-UHFFFAOYSA-N 0.000 claims description 3
- 229940093265 berberine Drugs 0.000 claims description 3
- QISXPYZVZJBNDM-UHFFFAOYSA-N berberine Natural products COc1ccc2C=C3N(Cc2c1OC)C=Cc4cc5OCOc5cc34 QISXPYZVZJBNDM-UHFFFAOYSA-N 0.000 claims description 3
- 238000006386 neutralization reaction Methods 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 3
- 229910052708 sodium Inorganic materials 0.000 claims description 3
- 239000011734 sodium Substances 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- IYRMWMYZSQPJKC-UHFFFAOYSA-N kaempferol Chemical compound C1=CC(O)=CC=C1C1=C(O)C(=O)C2=C(O)C=C(O)C=C2O1 IYRMWMYZSQPJKC-UHFFFAOYSA-N 0.000 claims 2
- UBSCDKPKWHYZNX-UHFFFAOYSA-N Demethoxycapillarisin Natural products C1=CC(O)=CC=C1OC1=CC(=O)C2=C(O)C=C(O)C=C2O1 UBSCDKPKWHYZNX-UHFFFAOYSA-N 0.000 claims 1
- 150000001298 alcohols Chemical group 0.000 claims 1
- 229940072645 coumadin Drugs 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- MWDZOUNAPSSOEL-UHFFFAOYSA-N kaempferol Natural products OC1=C(C(=O)c2cc(O)cc(O)c2O1)c3ccc(O)cc3 MWDZOUNAPSSOEL-UHFFFAOYSA-N 0.000 claims 1
- 235000008777 kaempferol Nutrition 0.000 claims 1
- UXOUKMQIEVGVLY-UHFFFAOYSA-N morin Natural products OC1=CC(O)=CC(C2=C(C(=O)C3=C(O)C=C(O)C=C3O2)O)=C1 UXOUKMQIEVGVLY-UHFFFAOYSA-N 0.000 claims 1
- PJVWKTKQMONHTI-UHFFFAOYSA-N warfarin Chemical compound OC=1C2=CC=CC=C2OC(=O)C=1C(CC(=O)C)C1=CC=CC=C1 PJVWKTKQMONHTI-UHFFFAOYSA-N 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000000243 solution Substances 0.000 abstract description 40
- 239000002699 waste material Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004146 energy storage Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 238000000605 extraction Methods 0.000 abstract description 2
- 239000007864 aqueous solution Substances 0.000 abstract 1
- KZNFRTXTQCISLO-UHFFFAOYSA-N oxovanadium;sulfuric acid Chemical compound [V]=O.OS(O)(=O)=O KZNFRTXTQCISLO-UHFFFAOYSA-N 0.000 abstract 1
- 230000008901 benefit Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 229910001456 vanadium ion Inorganic materials 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 229940022682 acetone Drugs 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 125000003158 alcohol group Chemical group 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- -1 halofugin Chemical compound 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- GOLORTLGFDVFDW-UHFFFAOYSA-N 3-(1h-benzimidazol-2-yl)-7-(diethylamino)chromen-2-one Chemical compound C1=CC=C2NC(C3=CC4=CC=C(C=C4OC3=O)N(CC)CC)=NC2=C1 GOLORTLGFDVFDW-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical class [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000257465 Echinoidea Species 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 241000765309 Vanadis Species 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000010883 coal ash Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- ZYGHJZDHTFUPRJ-UHFFFAOYSA-N coumarin Chemical compound C1=CC=C2OC(=O)C=CC2=C1 ZYGHJZDHTFUPRJ-UHFFFAOYSA-N 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- RYZCLUQMCYZBJQ-UHFFFAOYSA-H lead(2+);dicarbonate;dihydroxide Chemical compound [OH-].[OH-].[Pb+2].[Pb+2].[Pb+2].[O-]C([O-])=O.[O-]C([O-])=O RYZCLUQMCYZBJQ-UHFFFAOYSA-H 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000003870 refractory metal Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 150000003682 vanadium compounds Chemical class 0.000 description 1
- 125000005287 vanadyl group Chemical group 0.000 description 1
- 239000010969 white metal Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Materials Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
本发明涉及液流电池储能技术领域,且公开了一种高纯硫酸氧钒的制备方法,具体为以碱性含钒浸出液和失衡3.5价溶液为原料,互配中和溶液中的三价钒,直至溶液钒呈4价,使用生物碱类调节剂调节溶液ph值至中性,并促进溶液中四价钒析出,将析出物反溶入硫酸水溶液中,引入有机沉淀剂,使得硫酸氧钒在新溶液体系中加速结晶,得出的晶体纯度高。该高纯硫酸氧钒的制备方法,通过以碱性含钒浸出液、失衡3.5价钒溶液为主要原料,便于实现从废料中提取出高纯硫酸氧钒,有效的实现了废物再利用的效果,使其原料更加容易获得,通过采用生物碱类调节剂和有机沉淀剂对其进行加工,便于采用更为科学简练的制备方法。The invention relates to the technical field of flow battery energy storage, and discloses a preparation method of high-purity vanadyl sulfate. Vanadium, until the solution vanadium is 4-valent, use an alkaloid regulator to adjust the pH value of the solution to neutrality, and promote the precipitation of tetravalent vanadium in the solution, the precipitate is reversely dissolved into the sulfuric acid aqueous solution, and an organic precipitant is introduced to make the sulfuric acid oxygen Vanadium accelerates crystallization in the new solution system, and the resulting crystals are of high purity. The preparation method of high-purity vanadyl sulfate uses alkaline vanadium-containing leaching solution and unbalanced 3.5-valent vanadium solution as main raw materials, which facilitates extraction of high-purity vanadyl sulfate from waste, and effectively achieves the effect of waste recycling. The raw materials are more easily obtained, and a more scientific and concise preparation method is facilitated by using an alkaloid regulator and an organic precipitant to process it.
Description
技术领域technical field
本发明涉及液流电池储能技术领域,具体为一种高纯硫酸氧钒的制备方法。The invention relates to the technical field of liquid flow battery energy storage, in particular to a preparation method of high-purity vanadyl sulfate.
背景技术Background technique
钒的元素符号为V,银白色金属,在元素周期表中属VB族,原子序数23,原子量50.9414,体心立方晶体,常见化合价为+5、+4、+3、+2,钒的熔点很高,常与铌、钽、钨和钼并称为难熔金属,有延展性、质坚硬和无磁性,具有耐盐酸和硫酸的本领,并且在耐气、耐盐和耐水腐蚀的性能要比大多数不锈钢好,室温下致密状态的金属钒较稳定,不与空气、水和碱作用,也能耐稀酸,钒先后被两次发现,第一次是在1801年由墨西哥城的矿物学教授节烈里瓦发现的,他发现它在亚钒酸盐样本中,这个样本就是Pb5(VO4)3Cl,由于这种新元素的盐溶液在加热时呈现鲜艳的红色,所以被取名为“爱丽特罗尼”,即“红色”的意思,并将这种物品送到巴黎,然而,法国化学家推断它是一种被污染的铬矿石,所以没有被人们公认,第二次发现是在1830年,瑞典化学家塞夫斯特伦在研究斯马兰矿区的铁矿时,用酸溶解铁,在残渣中发现了钒,因为钒的化合物的颜色五颜六色,十分漂亮,所以就用古希腊神话中一位叫凡娜迪丝“Vanadis”的美丽女神的名字给这种新元素起名叫“Vanadium”,中文按其译音定名为钒,塞夫斯特伦、维勒和贝采里乌斯等人都曾研究过钒,确认钒的存在,但他们始终没有分离出单质钒,后来到了1830年写佛寺特勒木在由瑞典铁矿石提炼出的铁中发现了它,并肯定这是一种新元素称之为钒,他能够证明它是一种新的元素,并因此击败了一位与他竞争的化学家,来自在锡马潘(墨西哥)的沃勒,他也在对另一种钒矿石进行研究,钒的踪迹遍布全世界,在地壳中,钒的含量并不少,平均在两万个原子中,就有一个钒原子,比铜、锡、锌和镍的含量都多,但钒的分布太分散了,几乎没有含量较多的矿床,在海水中,在海胆等海洋生物体内,在磁铁矿中,在多种沥青矿物和煤灰中,在落到地球的陨石和太阳的光谱线中,人们都发现了钒的踪影。钒是地球上广泛分布的微量元素,其含量约占地壳构成的0.02%,获取相对容易。The element symbol of vanadium is V, a silver-white metal, belonging to the VB group in the periodic table, atomic number 23, atomic weight 50.9414, body-centered cubic crystal, common valences are +5, +4, +3, +2, the melting point of vanadium Very high, often referred to as refractory metals together with niobium, tantalum, tungsten and molybdenum, it is ductile, hard and non-magnetic, has the ability to resist hydrochloric acid and sulfuric acid, and is more resistant to gas, salt and water than corrosion resistance. Most stainless steels are good, and the metal vanadium in the dense state is relatively stable at room temperature. It does not react with air, water and alkali, and it is also resistant to dilute acids. Vanadium has been discovered twice, the first time was in 1801 by a professor of mineralogy in Mexico City. Jie Liwa found it in a sample of vanadite, which is Pb 5 (VO 4 ) 3 Cl, named because the salt solution of this new element turns bright red when heated "Eriteroni", which means "red", and sent this item to Paris, however, French chemists deduced that it was a contaminated chrome ore, so it was not recognized, and the second discovery was In 1830, when the Swedish chemist Sevstrom was studying the iron ore in the Smalan mining area, he dissolved iron with acid and found vanadium in the residue. Because the color of vanadium compounds is colorful and very beautiful, the ancient Greek The name of a beautiful goddess named Vanadis "Vanadis" in mythology named this new element "Vanadium", and the Chinese named it vanadium according to its transliteration, Sefström, Ville and Berzelius. Others have studied vanadium and confirmed the existence of vanadium, but they have never separated elemental vanadium. Later, in 1830, they wrote that Buddhist temple Telem found it in iron extracted from Swedish iron ore, and affirmed that it was A new element called vanadium, and he was able to show that it was a new element and thus beat a competing chemist from Waller in Simapan (Mexico), who was also working on another A kind of vanadium ore is studied, and traces of vanadium are all over the world. In the earth's crust, the content of vanadium is not much. On average, there is one vanadium atom in 20,000 atoms, which is more than copper, tin, zinc and nickel. In seawater, in marine organisms such as sea urchins, in magnetite, in various bituminous minerals and coal ash, in the Traces of vanadium have been found in the spectral lines of meteorites and the sun. Vanadium is a widely distributed trace element on the earth, its content accounts for about 0.02% of the crust, and it is relatively easy to obtain.
目前,钒是重要的稀有金属,在催化剂、合金、电池和先进材料等方面有着重要的应用,其中,全钒氧化还原液流电池作为钒的一项新应用领域,越来越受到广泛应用,与传统的蓄电池相比,具有可快速、大容量充放电和自放电率低和电池结构简单等特点,它是满足风能和太阳能等新型能源大规模储能的理想电源形式,作为电池活性物质的电解液而言,正极电解液由四价与五价钒离子及硫酸的混合溶液组成,负极电解液由二价与三价钒离子及硫酸的混合溶液组成,电池充电后,正极物质为五价钒离子硫酸溶液,负极为二价钒离子硫酸溶液,电池放电后,正负极分别为四价及三价钒离子硫酸溶液,硫酸氧钒作为电解液的主体物质,其纯度直接影响电解液性能,并且作为一种稳定存在的钒物质,其在医药、化工和国防等领域都有突出的作用,且从废料中提取出高纯硫酸氧钒就尤为可行,其耗能少,原料易得,是一种很有前景的技术领域。At present, vanadium is an important rare metal and has important applications in catalysts, alloys, batteries and advanced materials. Among them, all-vanadium redox flow batteries, as a new application field of vanadium, are more and more widely used. Compared with traditional batteries, it has the characteristics of fast, large-capacity charge and discharge, low self-discharge rate and simple battery structure. It is an ideal power source for large-scale energy storage of new energy such as wind energy and solar energy. As far as the electrolyte is concerned, the positive electrolyte is composed of a mixed solution of tetravalent and pentavalent vanadium ions and sulfuric acid, and the negative electrolyte is composed of a mixed solution of bivalent and trivalent vanadium ions and sulfuric acid. After the battery is charged, the positive electrode material is pentavalent. Vanadium ion sulfuric acid solution, the negative electrode is divalent vanadium ion sulfuric acid solution, after the battery is discharged, the positive and negative electrodes are tetravalent and trivalent vanadium ion sulfuric acid solution respectively, vanadyl sulfate is the main substance of the electrolyte, and its purity directly affects the performance of the electrolyte , and as a stably existing vanadium substance, it has a prominent role in the fields of medicine, chemical industry and national defense, and it is particularly feasible to extract high-purity vanadyl sulfate from waste, which consumes less energy and is easy to obtain raw materials. It is a promising technology field.
然而目前在生产过程中,需要利用蒸馏等常规手段,对其进行提炼生产,耗费大量的能源,原料的获取较为麻烦,提高了其生产成本,降低了其经济效益,故而提出一种高纯硫酸氧钒的制备方法解决上述问题。However, in the current production process, it is necessary to use conventional means such as distillation to refine and produce it, which consumes a lot of energy, and the acquisition of raw materials is troublesome, which increases its production cost and reduces its economic benefits. Therefore, a high-purity sulfuric acid is proposed. The preparation method of vanadyl solves the above problems.
发明内容SUMMARY OF THE INVENTION
(一)解决的技术问题(1) Technical problems solved
针对现有技术的不足,本发明提供了一种高纯硫酸氧钒的制备方法,具备方法简单、原料易得、能耗低、所得产品纯度高和有较高的经济效益等优点,解决了需要利用蒸馏等常规手段,对其进行提炼生产,耗费大量的能源,原料的获取较为麻烦,提高了其生产成本,降低了其经济效益的问题。Aiming at the deficiencies of the prior art, the present invention provides a preparation method of high-purity vanadyl sulfate, which has the advantages of simple method, easy-to-obtain raw materials, low energy consumption, high purity of the obtained product and higher economic benefits, etc. It needs to use conventional means such as distillation to refine and produce it, which consumes a lot of energy, and the acquisition of raw materials is troublesome, which increases its production cost and reduces its economic benefits.
(二)技术方案(2) Technical solutions
为实现上述方法简单、原料易得、能耗低、所得产品纯度高和有较高的经济效益目的,本发明提供如下技术方案:一种高纯硫酸氧钒的制备方法,包括以下的原料:钒矿、失衡3.5价钒溶液、生物碱类调节剂和有机沉淀剂。In order to realize that the above-mentioned method is simple, the raw materials are easy to obtain, the energy consumption is low, the obtained product has high purity and higher economic benefits, the present invention provides the following technical scheme: a preparation method of high-purity vanadyl sulfate, comprising the following raw materials: Vanadium ore, unbalanced 3.5-valent vanadium solution, alkaloid regulator and organic precipitant.
本发明要解决的另一技术问题是提供一种高纯硫酸氧钒的制备方法,包括以下步骤:Another technical problem to be solved by the present invention is to provide a kind of preparation method of high-purity vanadyl sulfate, comprising the following steps:
1)制备碱性含钒浸出液,通过将钒矿钠化焙烧和浸出的传统工艺,得到碱性含钒浸出液;1) prepare an alkaline vanadium-containing leachate, and obtain an alkaline vanadium-containing leachate by the traditional process of sodium roasting and leaching of vanadium ore;
2)混合制备,将碱性含钒浸出液和失衡3.5价钒溶液进行互配,互配中和溶液中的三价钒,直至溶液钒呈4价;2) mixed preparation, the alkaline vanadium-containing leaching solution and the unbalanced 3.5-valent vanadium solution are mutually matched, and the trivalent vanadium in the neutralization solution is matched with each other until the solution vanadium is 4-valent;
3)调节PH值,使用生物碱类调节剂调节上述制备的溶液ph值至中性,并促进溶液中四价钒析出;3) adjust the pH value, use the alkaloid regulator to adjust the pH value of the solution prepared above to neutrality, and promote the precipitation of tetravalent vanadium in the solution;
4)结晶,将上述析出物反溶入硫酸水溶液中,引入有机沉淀剂,使得硫酸氧钒在新溶液体系中加速结晶。4) Crystallization, the above-mentioned precipitates are reversely dissolved into an aqueous sulfuric acid solution, and an organic precipitant is introduced to accelerate the crystallization of vanadyl sulfate in the new solution system.
优选的,所述步骤1)中的碱性含钒浸出液的钒以+5价形式存在,其PH值的范围在8-12之间,且含钒量为20-45g/升。Preferably, the vanadium of the alkaline vanadium-containing leachate in the step 1) exists in the form of +5 valence, the pH value of which is in the range of 8-12, and the vanadium content is 20-45 g/liter.
优选的,所述生物碱类调节剂为阿托品、常山碱、茶碱、古豆碱、金鸡纳和黄连素中的一种或两种以上,复配有机溶剂为氯仿、甲酰胺和丙酮其中的一种。Preferably, the alkaloid regulator is one or more of atropine, halofugin, theophylline, coumarin, cinchona and berberine, and the compounded organic solvent is chloroform, formamide and acetone. A sort of.
优选的,所述有机沉淀剂为醇类物,如乙醇、乙二醇和甘油的其中一种。Preferably, the organic precipitant is an alcohol, such as one of ethanol, ethylene glycol and glycerol.
优选的,所述步骤4)引有入机沉淀剂后,将物料静止于恒温恒湿环境中,少许时间,析出硫酸氧钒晶体。Preferably, after the introduction of the organic precipitating agent in the step 4), the material is kept still in a constant temperature and humidity environment, and vanadyl sulfate crystals are precipitated for a short period of time.
优选的,所述重结晶晶体经过水洗和过滤,得到高纯硫酸氧钒。Preferably, the recrystallized crystals are washed with water and filtered to obtain high-purity vanadyl sulfate.
(三)有益效果(3) Beneficial effects
与现有技术相比,本发明提供了一种高纯硫酸氧钒的制备方法,具备以下有益效果:Compared with the prior art, the present invention provides a preparation method of high-purity vanadyl sulfate, which has the following beneficial effects:
该高纯硫酸氧钒的制备方法,通过以碱性含钒浸出液、失衡3.5价钒溶液为主要原料,便于实现从废料中提取出高纯硫酸氧钒,有效的实现了废物再利用的效果,使其原料更加容易获得,通过采用生物碱类调节剂和有机沉淀剂对其进行加工,便于采用更为科学简练的制备方法,摒弃原有的蒸馏等常规手段,从而实现了节省能源的效果,通过本制备方法简单有效,便于工业大规模的进行生产,可有效的回收废液中大部分的钒,同时本方法工艺钒损失率低,经济效益显著,故而达到了方法简单、原料易得、能耗低、所得产品纯度高和有较高的经济效益的目的。The preparation method of high-purity vanadyl sulfate uses alkaline vanadium-containing leaching solution and unbalanced 3.5-valent vanadium solution as main raw materials, which facilitates extraction of high-purity vanadyl sulfate from waste, and effectively achieves the effect of waste recycling. It makes its raw materials easier to obtain. By using alkaloid regulators and organic precipitants to process it, it is convenient to adopt a more scientific and concise preparation method, and to abandon the original conventional methods such as distillation, thereby achieving the effect of saving energy. The preparation method is simple and effective, convenient for industrial large-scale production, and can effectively recover most of the vanadium in the waste liquid. At the same time, the method has low loss rate of vanadium and significant economic benefits, so the method is simple, the raw materials are easy to obtain, the The purpose of low energy consumption, high purity of the obtained product and higher economic benefits.
具体实施方式Detailed ways
下面将结合本发明的实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
一种高纯硫酸氧钒的制备方法,包括以下的原料:钒矿、失衡3.5价钒溶液、生物碱类调节剂和有机沉淀剂。A method for preparing high-purity vanadyl sulfate, comprising the following raw materials: vanadium ore, an unbalanced 3.5-valent vanadium solution, an alkaloid regulator and an organic precipitant.
一种高纯硫酸氧钒的制备方法,其特征在于,包括以下步骤:A kind of preparation method of high-purity vanadyl sulfate, is characterized in that, comprises the following steps:
1)制备碱性含钒浸出液,通过将钒矿钠化焙烧和浸出的传统工艺,得到碱性含钒浸出液,碱性含钒浸出液的钒以+5价形式存在,其PH值的范围在8-12之间,且含钒量为20-45g/升;1) prepare an alkaline vanadium-containing leaching solution, obtain an alkaline vanadium-containing leaching solution by the traditional process of sodium roasting and leaching of vanadium ore, and the vanadium of the alkaline vanadium-containing leaching solution exists in the form of +5 valence, and the scope of its pH value is 8 -12, and the vanadium content is 20-45g/liter;
2)混合制备,将碱性含钒浸出液和失衡3.5价钒溶液进行互配,互配中和溶液中的三价钒,直至溶液钒呈4价;2) mixed preparation, the alkaline vanadium-containing leaching solution and the unbalanced 3.5-valent vanadium solution are mutually matched, and the trivalent vanadium in the neutralization solution is matched with each other until the solution vanadium is 4-valent;
3)调节PH值,使用生物碱类调节剂调节上述制备的溶液ph值至中性,生物碱类调节剂为阿托品、常山碱、茶碱、古豆碱、金鸡纳和黄连素中的一种或两种以上,复配有机溶剂为氯仿、甲酰胺和丙酮其中的一种,并促进溶液中四价钒析出;3) adjust pH value, use alkaloid regulator to regulate the solution pH value of above-mentioned preparation to neutrality, and alkaloid regulator is a kind of in atropine, halofugin, theophylline, coumarine, cinchona and berberine Or more than two, the compound organic solvent is one of chloroform, formamide and acetone, and promotes the precipitation of tetravalent vanadium in the solution;
4)结晶,将上述析出物反溶入硫酸水溶液中,引入有机沉淀剂,使得硫酸氧钒在新溶液体系中加速结晶,有机沉淀剂为醇类物,如乙醇、乙二醇和甘油的其中一种,引有入机沉淀剂后,将物料静止于恒温恒湿环境中,少许时间,析出硫酸氧钒晶体,重结晶晶体经过水洗和过滤,得到高纯硫酸氧钒。4) crystallization, the above-mentioned precipitate is reversely dissolved in the aqueous sulfuric acid solution, and an organic precipitating agent is introduced, so that vanadyl sulfate accelerates crystallization in the new solution system, and the organic precipitating agent is an alcohol, such as one of ethanol, ethylene glycol and glycerin. After introducing the organic precipitant, the material is kept in a constant temperature and humidity environment for a short time to precipitate vanadyl sulfate crystals, and the recrystallized crystals are washed with water and filtered to obtain high-purity vanadyl sulfate.
实验例:Experimental example:
已知钒浓度2.8mol/L失效电解液1升,以及含钒浸出液28克/升5升,互混,搅拌,加入阿托品、茶碱与丙酮的混合调节剂,调节ph值为7,静置,得硫酸氧钒粗结晶,回溶于硫酸水溶液中,加入过量甘油,在恒温恒湿环境下静置结晶,得到610克硫酸氧钒结晶,钒回收率89%。Known vanadium concentration 2.8mol/L 1 liter of failed electrolyte, and vanadium-containing leaching solution 28 g/L 5 liters, mix with each other, stir, add a mixed regulator of atropine, theophylline and acetone, adjust the pH value to 7, let stand , to obtain crude vanadyl sulfate crystals, redissolve them in aqueous sulfuric acid solution, add excess glycerin, and stand for crystallization under constant temperature and humidity environment to obtain 610 grams of vanadyl sulfate crystals, and the recovery rate of vanadium is 89%.
实施例结果表明,本发明以碱性含钒浸出液和失衡3.5价溶液为原料,最终得到高纯硫酸氧钒。The results of the examples show that the present invention takes the alkaline vanadium-containing leaching solution and the unbalanced 3.5-valent solution as raw materials, and finally obtains high-purity vanadyl sulfate.
本发明的有益效果是:通过以碱性含钒浸出液、失衡3.5价钒溶液为主要原料,便于实现从废料中提取出高纯硫酸氧钒,有效的实现了废物再利用的效果,使其原料更加容易获得,通过采用生物碱类调节剂和有机沉淀剂对其进行加工,便于采用更为科学简练的制备方法,摒弃原有的蒸馏等常规手段,从而实现了节省能源的效果,通过本制备方法简单有效,便于工业大规模的进行生产,可有效的回收废液中大部分的钒,同时本方法工艺钒损失率低,经济效益显著,故而达到了方法简单、原料易得、能耗低、所得产品纯度高和有较高的经济效益的目的,解决了需要利用蒸馏等常规手段,对其进行提炼生产,耗费大量的能源,原料的获取较为麻烦,提高了其生产成本,降低了其经济效益的问题。The beneficial effects of the invention are as follows: by using the alkaline vanadium-containing leaching solution and the unbalanced 3.5-valent vanadium solution as the main raw materials, it is convenient to extract high-purity vanadyl sulfate from the waste, effectively realize the effect of recycling the waste, and make its raw materials It is easier to obtain, and by using alkaloid regulators and organic precipitants to process it, it is convenient to adopt a more scientific and concise preparation method, and to abandon the original conventional methods such as distillation, thereby realizing the effect of saving energy. The method is simple and effective, convenient for industrial large-scale production, and can effectively recover most of the vanadium in the waste liquid. At the same time, the method has a low loss rate of vanadium and significant economic benefits, so that the method is simple, the raw materials are readily available, and the energy consumption is low. , the purpose of high purity and higher economic benefit of the obtained product solves the need to use conventional means such as distillation to refine and produce it, consumes a lot of energy, and the acquisition of raw materials is more troublesome, which improves its production cost and reduces its cost. question of economic efficiency.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.
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