CN107814564B - A method for batch preparation of low-cost carbon-coated titanium phosphate compounds - Google Patents
A method for batch preparation of low-cost carbon-coated titanium phosphate compounds Download PDFInfo
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- CN107814564B CN107814564B CN201610821504.9A CN201610821504A CN107814564B CN 107814564 B CN107814564 B CN 107814564B CN 201610821504 A CN201610821504 A CN 201610821504A CN 107814564 B CN107814564 B CN 107814564B
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 79
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims abstract description 47
- JUWGUJSXVOBPHP-UHFFFAOYSA-B titanium(4+);tetraphosphate Chemical class [Ti+4].[Ti+4].[Ti+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O JUWGUJSXVOBPHP-UHFFFAOYSA-B 0.000 title abstract description 11
- 238000002360 preparation method Methods 0.000 title abstract description 4
- 239000000843 powder Substances 0.000 claims abstract description 57
- -1 titanium phosphate compound Chemical class 0.000 claims abstract description 38
- 238000000498 ball milling Methods 0.000 claims abstract description 32
- 239000002002 slurry Substances 0.000 claims abstract description 31
- 239000002243 precursor Substances 0.000 claims abstract description 19
- 239000010936 titanium Substances 0.000 claims abstract description 19
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 238000001694 spray drying Methods 0.000 claims abstract description 17
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 14
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 14
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 13
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 13
- 239000011574 phosphorus Substances 0.000 claims abstract description 13
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 13
- 238000010532 solid phase synthesis reaction Methods 0.000 claims abstract description 11
- 239000011812 mixed powder Substances 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 32
- 238000005245 sintering Methods 0.000 claims description 20
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000002270 dispersing agent Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 8
- 229910002804 graphite Inorganic materials 0.000 claims description 7
- 239000010439 graphite Substances 0.000 claims description 7
- 239000004408 titanium dioxide Substances 0.000 claims description 7
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims description 6
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims description 6
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 6
- 235000019837 monoammonium phosphate Nutrition 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000002518 antifoaming agent Substances 0.000 claims description 5
- 239000012298 atmosphere Substances 0.000 claims description 5
- 239000012046 mixed solvent Substances 0.000 claims description 5
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 4
- 229920002125 Sokalan® Polymers 0.000 claims description 4
- 238000006481 deamination reaction Methods 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 229910052744 lithium Inorganic materials 0.000 claims description 4
- 239000004584 polyacrylic acid Substances 0.000 claims description 4
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims description 4
- 235000019982 sodium hexametaphosphate Nutrition 0.000 claims description 4
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims description 4
- 239000004254 Ammonium phosphate Substances 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 229910000148 ammonium phosphate Inorganic materials 0.000 claims description 3
- 235000019289 ammonium phosphates Nutrition 0.000 claims description 3
- 229910000388 diammonium phosphate Inorganic materials 0.000 claims description 3
- 235000019838 diammonium phosphate Nutrition 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-M dihydrogenphosphate Chemical compound OP(O)([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-M 0.000 claims description 3
- 235000021323 fish oil Nutrition 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 230000001681 protective effect Effects 0.000 claims description 3
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 claims description 3
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- 229910000288 alkali metal carbonate Inorganic materials 0.000 claims description 2
- 150000008041 alkali metal carbonates Chemical group 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 2
- 235000004443 Ricinus communis Nutrition 0.000 claims 1
- 239000006229 carbon black Substances 0.000 claims 1
- 239000013530 defoamer Substances 0.000 claims 1
- 229910021385 hard carbon Inorganic materials 0.000 claims 1
- 235000006408 oxalic acid Nutrition 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000008159 sesame oil Substances 0.000 claims 1
- 235000011803 sesame oil Nutrition 0.000 claims 1
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 4
- 239000002245 particle Substances 0.000 description 13
- 239000011734 sodium Substances 0.000 description 10
- 239000000919 ceramic Substances 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 229910052700 potassium Inorganic materials 0.000 description 9
- 229910052708 sodium Inorganic materials 0.000 description 9
- 238000002156 mixing Methods 0.000 description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 7
- 239000011591 potassium Substances 0.000 description 7
- 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 description 6
- 238000009826 distribution Methods 0.000 description 6
- 238000003746 solid phase reaction Methods 0.000 description 6
- 239000011149 active material Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 239000012071 phase Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 239000011261 inert gas Substances 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- 229910001413 alkali metal ion Inorganic materials 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000004359 castor oil Substances 0.000 description 3
- 235000019438 castor oil Nutrition 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 3
- 238000005469 granulation Methods 0.000 description 3
- 230000003179 granulation Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000009830 intercalation Methods 0.000 description 3
- SNKMVYBWZDHJHE-UHFFFAOYSA-M lithium;dihydrogen phosphate Chemical compound [Li+].OP(O)([O-])=O SNKMVYBWZDHJHE-UHFFFAOYSA-M 0.000 description 3
- 239000012299 nitrogen atmosphere Substances 0.000 description 3
- 230000002441 reversible effect Effects 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- 229910001415 sodium ion Inorganic materials 0.000 description 3
- 239000002228 NASICON Substances 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000006230 acetylene black Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000001479 atomic absorption spectroscopy Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 230000002687 intercalation Effects 0.000 description 2
- 239000010416 ion conductor Substances 0.000 description 2
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 2
- 229910052808 lithium carbonate Inorganic materials 0.000 description 2
- IIPYXGDZVMZOAP-UHFFFAOYSA-N lithium nitrate Chemical compound [Li+].[O-][N+]([O-])=O IIPYXGDZVMZOAP-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009831 deintercalation Methods 0.000 description 1
- YNQRWVCLAIUHHI-UHFFFAOYSA-L dilithium;oxalate Chemical compound [Li+].[Li+].[O-]C(=O)C([O-])=O YNQRWVCLAIUHHI-UHFFFAOYSA-L 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
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Abstract
本发明涉及一种低成本碳包覆的磷酸钛化合物批量制备的方法,所述磷酸钛化合物的化学式为MxTi2(PO4)3,其中M选自碱金属中的至少一种,x=1~1.05,所述方法包括:步骤 1)以化学计量比的碱金属源、磷源、钛源和碳源为原料,湿法球磨制得浆料;步骤 2)将所述浆料用离心式喷雾干燥的方法得到碳包覆的磷酸钛化合物前驱体混合粉体;步骤 3)将所述前驱体混合粉体采用固相合成方法烧结得到碳包覆的磷酸钛化合物粉体。本发明工艺简单、成本低,可广泛应用于大规模生产磷酸钛化合物。
The invention relates to a method for batch preparation of a low-cost carbon-coated titanium phosphate compound, wherein the chemical formula of the titanium phosphate compound is M x Ti 2 (PO 4 ) 3 , wherein M is selected from at least one of alkali metals, x = 1 to 1.05, the method includes: step 1) using alkali metal source, phosphorus source, titanium source and carbon source in stoichiometric ratio as raw materials, wet ball milling to prepare slurry; step 2) using the slurry with The carbon-coated titanium phosphate compound precursor mixed powder is obtained by a centrifugal spray drying method; step 3) the precursor mixed powder is sintered by a solid-phase synthesis method to obtain a carbon-coated titanium phosphate compound powder. The invention has simple process and low cost, and can be widely used in large-scale production of titanium phosphate compounds.
Description
技术领域technical field
本发明涉及一种适于批量制备碳包覆的磷酸钛化合物陶瓷粉体的方法,具体涉及一种采用含碳前驱物以及多种物相成分的前驱体进行球磨混料,喷雾干燥造粒,通过高温固相合成反应方法制备碳包覆的磷酸钛化合物粉体,属于离子导电陶瓷材料领域。The invention relates to a method suitable for batch preparation of carbon-coated titanium phosphate compound ceramic powders, in particular to a method for ball-milling mixing, spray-drying and granulating by using carbon-containing precursors and precursors of various phase components, The carbon-coated titanium phosphate compound powder is prepared by a high-temperature solid-phase synthesis reaction method, and belongs to the field of ion conductive ceramic materials.
背景技术Background technique
磷酸钛化合物是一种典型的NASICON结构,其拥有较大的隧道尺寸能允许碱金属离子自由迁移。它是一种快离子导体,具有高离子传导性和较小的电子传导,具有极好的热稳定性,是一种重要的碱金属离子电池电极材料。以NaTi2(PO4)3为例,在1mol/LNa2SO4溶液中,NaTi2(PO4)3在-0.82V(vs.Ag/AgCl)处有一对十分对称的氧化还原峰,说明钠离子在-0.82V能发生可逆嵌脱反应。这一反应电势区间略高于水的析氢电位,这一较负的阳极电势不仅充分的利用了水的析氢电势窗口有利于提高电池的工作电压,还确保了在正常的嵌脱钠反应过程中不会发生析氢副反应。充放电曲线显示,NaTi2(PO4)3在-0.82V处有平稳的充放电平台,可逆容量为120mAh/g,相当于两个钠离子的脱嵌容量。得益于NaTi2(PO4)3材料的快离子导体结构,对其在100C的高倍率下进行充放电仍能释放70%的可逆比容量,因此可以作为高功率负极材料。MxTi2(PO4)3经过碳包覆处理后,不仅材料的电子电导率改善了,活性物质利用率也会得到明显的提高了,由于避免了电解液与材料表面的直接接触,可以有效的防止副反应的发生,从而大大提高其循环稳定性。Titanium phosphate compound is a typical NASICON structure, and its large tunnel size allows free migration of alkali metal ions. It is a fast ionic conductor with high ionic conductivity and small electronic conduction, excellent thermal stability, and is an important electrode material for alkali metal ion batteries. Taking NaTi 2 (PO 4 ) 3 as an example, in 1mol/L Na 2 SO 4 solution, NaTi 2 (PO 4 ) 3 has a pair of very symmetrical redox peaks at -0.82V (vs. Ag/AgCl), indicating that Na ions can undergo reversible intercalation and deintercalation reactions at -0.82V. This reaction potential range is slightly higher than the hydrogen evolution potential of water. This relatively negative anode potential not only makes full use of the hydrogen evolution potential window of water, which is beneficial to improve the working voltage of the battery, but also ensures that during the normal intercalation and de-sodium reaction process Hydrogen evolution side reaction does not occur. The charge-discharge curve shows that NaTi 2 (PO 4 ) 3 has a stable charge-discharge plateau at -0.82V, and the reversible capacity is 120mAh/g, which is equivalent to the de-intercalation capacity of two sodium ions. Benefiting from the fast ionic conductor structure of NaTi 2 (PO 4 ) 3 material, it can still release 70% of the reversible specific capacity when charged and discharged at a high rate of 100C, so it can be used as a high-power anode material. After carbon coating treatment of M x Ti 2 (PO 4 ) 3 , not only the electronic conductivity of the material is improved, but also the utilization rate of active material is also significantly improved. Since the direct contact between the electrolyte and the material surface is avoided, it can be It can effectively prevent the occurrence of side reactions, thereby greatly improving its cycle stability.
目前,制备碳包覆的磷酸钛化合物的方法主要有微波加热合成法、水热法、溶胶凝胶法等[J.Mater.Chem.A,2015,3,12089-12096]。通常相较于传统的固相合成法,这些方法制备的粉体纯度较高,性能优异,但生产工艺复杂,设备较多,难以实现大规模生产,尤其是进行碳包覆时候需要多次热处理和研磨,成本较高,不能满足降低电池成本的要求。传统的固相合成法也有本身的缺陷,比如由于粉体混合不均造成的副反应多,产品不纯等。At present, the methods for preparing carbon-coated titanium phosphate compounds mainly include microwave heating synthesis method, hydrothermal method, sol-gel method, etc. [J.Mater.Chem.A,2015,3,12089-12096]. Usually, compared with the traditional solid-phase synthesis method, the powder prepared by these methods has higher purity and excellent performance, but the production process is complex and the equipment is more, which makes it difficult to achieve large-scale production, especially when carbon coating requires multiple heat treatments And grinding, the cost is high, can not meet the requirements of reducing battery cost. The traditional solid-phase synthesis method also has its own defects, such as many side reactions caused by uneven mixing of powders and impure products.
发明内容SUMMARY OF THE INVENTION
针对上述问题,本发明的目的在于提供一种能制备高纯度的碳包覆的磷酸钛化合物且工艺简单、成本低、能大规模生产的方法。In view of the above problems, the purpose of the present invention is to provide a method capable of preparing high-purity carbon-coated titanium phosphate compound with simple process, low cost and large-scale production.
本发明提供一种制备碳包覆磷酸钛化合物的方法,所述磷酸钛化合物的化学式为MxTi2(PO4)3,其中M选自碱金属中的至少一种,x=1~1.05,所述方法包括:The present invention provides a method for preparing a carbon-coated titanium phosphate compound, wherein the chemical formula of the titanium phosphate compound is M x Ti 2 (PO 4 ) 3 , wherein M is selected from at least one of alkali metals, and x=1-1.05 , the method includes:
步骤1)以化学计量比的碱金属源、磷源、钛源和碳源(优选为无机碳源)为原料,湿法球磨制得浆料;Step 1) using alkali metal source, phosphorus source, titanium source and carbon source (preferably inorganic carbon source) in stoichiometric ratio as raw materials, wet ball milling to prepare slurry;
步骤2)将所述浆料用离心式喷雾干燥的方法得到碳包覆的磷酸钛化合物前驱体混合粉体;Step 2) obtaining carbon-coated titanium phosphate compound precursor mixed powder by centrifugal spray drying of the slurry;
步骤3)将所述前驱体混合粉体采用固相合成方法烧结得到碳包覆的磷酸钛化合物粉体。Step 3) Sintering the precursor mixed powder by a solid-phase synthesis method to obtain a carbon-coated titanium phosphate compound powder.
本发明区别于传统的固相合成法,采用球磨制作浆料联合喷雾干燥造粒的方式,使得到的粉体颗粒成球形,使得磷酸钛化合物前驱体混合均匀且使得磷酸钛化合物易被碳包覆,得到的粉体再进行高温固相反应批量制备碳包覆的磷酸钛化合物,尤其可避免传统固相反应中的因为混料不均造成的高温反应成分不均匀,粉体烧结中出现其他晶相杂质的问题。本发明得到的产品纯度高,既可以很好地提高材料的导电性,极大地提高了材料的电化学性能,而且工艺简单、成本低,可广泛应用于大规模生产磷酸钛化合物。Different from the traditional solid phase synthesis method, the present invention adopts the method of making slurry by ball milling and spray drying and granulation, so that the obtained powder particles are spherical, so that the precursor of the titanium phosphate compound is mixed evenly and the titanium phosphate compound is easily coated with carbon. The obtained powder is then subjected to a high-temperature solid-phase reaction to prepare carbon-coated titanium phosphate compounds in batches, especially to avoid the uneven high-temperature reaction components caused by uneven mixing in the traditional solid-phase reaction, and other occurrences in powder sintering. crystal phase impurities. The product obtained by the invention has high purity, can well improve the electrical conductivity of the material, greatly improves the electrochemical performance of the material, has simple process and low cost, and can be widely used in large-scale production of titanium phosphate compounds.
较佳地,步骤1)中,湿法球磨的溶剂为水、或者水和乙醇的混合溶剂,在所述混合溶剂中乙醇的含量为0~10wt.%。本发明选用廉价易得、对环境无害的水(优选为去离子水)作为主要溶剂,可以降低成本且环境友好。Preferably, in step 1), the solvent of wet ball milling is water or a mixed solvent of water and ethanol, and the content of ethanol in the mixed solvent is 0-10 wt.%. The present invention selects cheap, easily available, environmentally friendly water (preferably deionized water) as the main solvent, which can reduce costs and is environmentally friendly.
较佳地,步骤1)中,碳源的含量为0~20wt.%。优选地,所述碳源在加入球磨机之前用含有羟基官能团有机溶剂预处理增强浸湿性。根据本发明,可以使得磷酸钛化合物前驱体混合更均匀且使得磷酸钛化合物更易被碳包覆。Preferably, in step 1), the content of the carbon source is 0-20 wt.%. Preferably, the carbon source is pretreated with an organic solvent containing hydroxyl functional groups to enhance wettability prior to addition to the ball mill. According to the present invention, the titanium phosphate compound precursor can be mixed more uniformly and the titanium phosphate compound can be more easily coated with carbon.
较佳地,步骤1)包括:将碱金属源、钛源和磷源按照(1-1.05):2:3的摩尔比混合,将混合的原料倒入球磨桶中,按照固含量10-50wt.%加入去离子水,以50~300转/分钟的转速球磨1~5小时得到第一浆料;以及在所得的第一浆料中加入碳源,以50~300转/分钟的转速混合球磨1~5小时。Preferably, step 1) includes: mixing the alkali metal source, the titanium source and the phosphorus source according to the molar ratio of (1-1.05):2:3, pouring the mixed raw materials into the ball mill barrel, and according to the solid content of 10-50wt % Add deionized water, and ball mill at 50-300 r/min for 1-5 hours to obtain the first slurry; and add carbon source to the obtained first slurry, and mix at 50-300 r/min Ball mill for 1 to 5 hours.
本发明通过分步球磨方法可以获得具有一定黏度和粒径的浆料,相较于一步球磨,可以混料更加均匀,而且由于每种粉体的初始粒径不同,分步球磨可以使最终得到的浆料粉体粒径分布可控。In the present invention, the slurry with a certain viscosity and particle size can be obtained by the step-by-step ball milling method. Compared with the one-step ball milling, the material can be mixed more uniformly, and because the initial particle size of each powder is different, the step-by-step ball milling can make the final product The particle size distribution of the slurry powder is controllable.
较佳地,步骤1)中,还加入消泡剂和/或分散剂。优选地,所述消泡剂为高级醇,所述高级醇的添加量为粉体的0.5~5wt.%,所述分散剂的添加量为粉体的0.5~5wt.%。优选地,所述分散剂选自聚丙烯酸、六偏磷酸钠、聚乙二醇、鱼油和蓖麻油中的任意一种或几种。Preferably, in step 1), a defoaming agent and/or a dispersing agent are also added. Preferably, the defoaming agent is a higher alcohol, the addition amount of the higher alcohol is 0.5-5 wt.% of the powder, and the addition amount of the dispersant is 0.5-5 wt.% of the powder. Preferably, the dispersing agent is selected from any one or more of polyacrylic acid, sodium hexametaphosphate, polyethylene glycol, fish oil and castor oil.
较佳地,步骤1)中,所述碱金属源为碱金属的碳酸盐、氢氧化物、草酸盐、醋酸盐、磷酸二氢盐和硝酸盐中的任意一种;Preferably, in step 1), the alkali metal source is any one of alkali metal carbonate, hydroxide, oxalate, acetate, dihydrogen phosphate and nitrate;
所述钛源为二氧化钛、偏钛酸、钛酸、四氯化钛任意的一种;The titanium source is any one of titanium dioxide, metatitanic acid, titanic acid and titanium tetrachloride;
所述磷源为磷酸二氢锂、磷酸二氢铵、磷酸氢二铵和磷酸铵中的任意一种;The phosphorus source is any one of lithium dihydrogen phosphate, ammonium dihydrogen phosphate, diammonium hydrogen phosphate and ammonium phosphate;
所述碳源为石墨、活性炭、乙炔黑、石墨烯等其中的任意一种或几种。The carbon source is any one or more of graphite, activated carbon, acetylene black, graphene and the like.
较佳地,步骤1)中,所得浆料的固含量为20~60wt.%。Preferably, in step 1), the solid content of the obtained slurry is 20-60 wt.%.
较佳地,步骤2)中,使用离心式喷雾干燥设备,控制进风温度100~240℃,优选200~240℃,出风温度80~110℃,优选100~110℃,离心速率10000~20000转/分,优选12000~15000转/分。通过如上所述控制离心式喷雾干燥设备的工艺参数,可以得到尺寸分布更为均匀的球形颗粒。Preferably, in step 2), centrifugal spray drying equipment is used to control the inlet air temperature to be 100-240°C, preferably 200-240°C, the outlet air temperature to be 80-110°C, preferably 100-110°C, and the centrifugal speed to be 10000-20000°C. RPM, preferably 12000-15000 RPM. By controlling the process parameters of the centrifugal spray drying equipment as described above, spherical particles with more uniform size distribution can be obtained.
较佳地,步骤3)中,所述烧结是在氮气或者氩气的保护性气氛下于600~1000℃保温1~24小时。根据本发明,可以得到晶相纯度高的碳包覆的磷酸钛化合物陶瓷粉体。Preferably, in step 3), the sintering is carried out under a protective atmosphere of nitrogen or argon at 600-1000° C. for 1-24 hours. According to the present invention, a carbon-coated titanium phosphate compound ceramic powder with high crystal phase purity can be obtained.
较佳地,步骤3)中,在升温至烧结温度之前,于200~400℃(例如200~350℃或250~400℃)恒温1~3小时进行脱氨反应。Preferably, in step 3), before heating up to the sintering temperature, the deamination reaction is carried out at a constant temperature of 200-400°C (eg, 200-350°C or 250-400°C) for 1-3 hours.
本发明采用球磨混合,喷雾干燥的方法,通过高温固相反应,得到碳包覆的磷酸钛化合物陶瓷粉体。本发明与现有技术相比,具有以下优点和有益效果:The present invention adopts the method of ball milling mixing and spray drying, and obtains carbon-coated titanium phosphate compound ceramic powder through high-temperature solid-phase reaction. Compared with the prior art, the present invention has the following advantages and beneficial effects:
1、通过喷雾干燥,可以实现石墨等活性材料的碳包覆,提高材料的导电性,极大的提高材料的电化学性能;1. Through spray drying, carbon coating of graphite and other active materials can be achieved, the electrical conductivity of the material can be improved, and the electrochemical performance of the material can be greatly improved;
2、通过喷雾干燥,可以得到尺寸分布均匀的颗粒,有利于提高粉体材料的烧结性能;2. Through spray drying, particles with uniform size distribution can be obtained, which is beneficial to improve the sintering performance of powder materials;
3、固相法合成的具有NASICON结构的碳包覆的碱金属离子电极材料,有较好的电化学性能,合成工艺简单、易控制,价格便宜,可以应用于储能设备、后备电源、储备电源等;3. The carbon-coated alkali metal ion electrode material with NASICON structure synthesized by solid-phase method has good electrochemical performance, simple synthesis process, easy control and low price, and can be used in energy storage equipment, backup power supply, storage power supply, etc.;
4、本发明合成周期短、原料廉价、工艺简单、易于控制,具有显著的实用价值和良好的应用前景。4. The invention has the advantages of short synthesis period, cheap raw materials, simple process and easy control, and has significant practical value and good application prospect.
附图说明Description of drawings
图1是根据本发明一实施方式的批量生产磷酸钛化合物的流程图;1 is a flow chart of mass production of titanium phosphate compounds according to an embodiment of the present invention;
图2是本发明一实施例烧结后的粉体SEM图;2 is a SEM image of the powder after sintering according to an embodiment of the present invention;
图3是本发明一实施例烧结后的粉体粒度分布图;3 is a particle size distribution diagram of powder after sintering according to an embodiment of the present invention;
图4本发明一实施例烧结后的粉体XRD图。FIG. 4 is an XRD pattern of the powder after sintering according to an embodiment of the present invention.
具体实施方式Detailed ways
以下结合附图和下述实施方式进一步说明本发明,应理解,附图及下述实施方式仅用于说明本发明,而非限制本发明。The present invention will be further described below with reference to the accompanying drawings and the following embodiments. It should be understood that the accompanying drawings and the following embodiments are only used to illustrate the present invention, but not to limit the present invention.
本发明提出一种碳包覆的磷酸钛化合物MxTi2(PO4)3(M=Na,Li,K等,其中x=1~1.05)低成本批量制备方法。通过球磨分散,离心喷雾干燥造粒的方法使制备的粉体成球形,使得磷酸钛化合物前驱体混合均匀,而且易被碳包覆,得到的粉体再进行高温固相反应方法批量制备碳包覆的磷酸钛化合物。图1示出根据本发明一实施方式的批量生产磷酸钛化合物的流程图。以下,参照图1,具体说明生产磷酸钛化合物的方法。The present invention provides a low-cost batch preparation method of carbon-coated titanium phosphate compound M x Ti 2 (PO 4 ) 3 (M=Na, Li, K, etc., wherein x=1-1.05). By ball milling dispersion, centrifugal spray drying and granulation, the prepared powder is spherical, so that the precursor of titanium phosphate compound is evenly mixed and easily coated with carbon. The obtained powder is then subjected to high temperature solid-phase reaction method to prepare carbon coating Coated titanium phosphate compound. FIG. 1 shows a flow chart of mass production of titanium phosphate compounds according to an embodiment of the present invention. Hereinafter, referring to FIG. 1 , a method for producing a titanium phosphate compound will be specifically described.
首先,进行球磨混料。本发明中,原料可包含碱金属源、磷源、钛源和碳源。各原料可采用粉体。本发明对原料粉体的纯度没有过高的要求,可使用工业级的原料。各原料可采用现有方法合成或商业购买。First, ball mill compounding is performed. In the present invention, the raw material may contain an alkali metal source, a phosphorus source, a titanium source and a carbon source. Powder can be used for each raw material. The present invention does not have too high requirements on the purity of the raw material powder, and industrial-grade raw materials can be used. Each raw material can be synthesized by existing methods or purchased commercially.
作为碱金属源,包括但不限于碳酸锂(钠,钾)、氢氧化锂(钠,钾)、草酸锂(钠,钾)、醋酸锂(钠,钾)、磷酸二氢锂(钠,钾)或硝酸锂(钠,钾)中的任一种或几种。As an alkali metal source, including but not limited to lithium carbonate (sodium, potassium), lithium hydroxide (sodium, potassium), lithium oxalate (sodium, potassium), lithium acetate (sodium, potassium), lithium dihydrogen phosphate (sodium, potassium) ) or any one or more of lithium nitrate (sodium, potassium).
作为磷源,包括但不限于磷酸二氢锂、磷酸二氢铵、磷酸氢二铵或磷酸铵中的任一种或几种。The phosphorus source includes, but is not limited to, any one or more of lithium dihydrogen phosphate, ammonium dihydrogen phosphate, diammonium hydrogen phosphate or ammonium phosphate.
作为钛源,包括但不限于二氧化钛、偏钛酸、钛酸、四氯化钛中的任一种或几种。其中二氧化钛可为金红石、锐钛矿、板钛矿三种型态中的任一种或几种。The titanium source includes but is not limited to any one or more of titanium dioxide, metatitanic acid, titanic acid, and titanium tetrachloride. Wherein the titanium dioxide can be any one or several of the three types of rutile, anatase and brookite.
作为碳源,优选为无机碳源,包括但不限于石墨、活性炭、乙炔黑、石墨烯中的任一种或几种。The carbon source is preferably an inorganic carbon source, including but not limited to any one or more of graphite, activated carbon, acetylene black, and graphene.
碱金属源、磷源、钛源按照磷酸钛化合物化学计量式MxTi2(PO4)3(M=Na,Li,K等,其中x=1~1.05)配比。Alkali metal source, phosphorus source and titanium source are proportioned according to the stoichiometric formula of titanium phosphate compound M x Ti 2 (PO 4 ) 3 (M=Na, Li, K, etc., wherein x=1-1.05).
碳源的含量可为0~50wt.%,优选为10~20wt.%。另外,碳源在加入球磨机之前可用乙醇或其他含有羟基官能团有机溶剂预处理增强浸湿性。The content of the carbon source may be 0-50 wt.%, preferably 10-20 wt.%. In addition, the carbon source can be pretreated with ethanol or other organic solvent containing hydroxyl functional groups to enhance wettability before adding to the ball mill.
球磨时可选用廉价易得、对环境无害的去离子水作为主要溶剂。也可以使用水和乙醇的混合溶剂。其中乙醇含量优选为0~20wt.%。Deionized water, which is cheap, easy to obtain and environmentally friendly, can be used as the main solvent during ball milling. A mixed solvent of water and ethanol can also be used. The ethanol content is preferably 0-20 wt.%.
球磨时,还可以加入少量高级醇(优选C7~C9醇)作为消泡剂。另外,还可以加入少量分散剂,分散剂的添加量可为粉体的0.5wt.%~5wt.%。作为分散剂,包括但不限于聚丙烯酸,六偏磷酸钠,聚乙二醇,鱼油,蓖麻油其中的一种或者几种。During ball milling, a small amount of higher alcohol (preferably C7-C9 alcohol) can also be added as a defoaming agent. In addition, a small amount of dispersant can also be added, and the added amount of the dispersant can be 0.5wt.% to 5wt.% of the powder. As a dispersing agent, it includes but is not limited to one or more of polyacrylic acid, sodium hexametaphosphate, polyethylene glycol, fish oil, and castor oil.
本发明中,球磨混料可采用分步球磨法。在一个示例中,包括:将碱金属源、磷源、钛源与溶剂混合后进行球磨的第一球磨步骤;和再加入碳源进一步球磨的第二球磨步骤。在第一球磨步骤中,粉体的的总质量与溶剂和磨球的质量比可为(10~50):(50~90):(10~30)。转速可为50~300转/分钟,球磨时间可为1~5小时。在第二球磨步骤中,转速可为50~300转/分钟,球磨时间可为1~5小时。In the present invention, the ball-milling mixture can adopt a step-by-step ball milling method. In one example, it includes: a first ball milling step of mixing an alkali metal source, a phosphorus source, and a titanium source with a solvent and then ball milling; and a second ball milling step of adding a carbon source for further ball milling. In the first ball milling step, the mass ratio of the total mass of the powder to the solvent and the grinding ball may be (10-50):(50-90):(10-30). The rotation speed can be 50-300 rpm, and the ball milling time can be 1-5 hours. In the second ball milling step, the rotational speed may be 50-300 rpm, and the ball-milling time may be 1-5 hours.
球磨混料所得的浆料的固含量控制在0~60wt.%,优选地,控制在20~30wt.%。浆料的粒径为1~10μm。The solid content of the slurry obtained by ball milling is controlled at 0-60 wt.%, preferably, at 20-30 wt.%. The particle size of the slurry is 1 to 10 μm.
接着,将所得浆料用离心式喷雾干燥机进行造粒,得到碳包覆的磷酸钛化合物前驱体混合粉体。可以使用离心式喷雾干燥设备,控制进风温度100~240℃,优选200~240℃,出风温度80~110℃,优选100~110℃,离心速率10000~20000转/分,优选10000~15000转/分。Next, the obtained slurry was granulated with a centrifugal spray dryer to obtain a carbon-coated titanium phosphate compound precursor mixed powder. Centrifugal spray drying equipment can be used to control the inlet air temperature 100-240°C, preferably 200-240°C, the outlet air temperature 80-110°C, preferably 100-110°C, and the centrifugal speed 10000-20000 rpm, preferably 10000-15000 rev/min.
将经过造粒的粉体进一步采用传统的固相合成方法,使用气氛炉高温烧结得到碳包覆的磷酸钛化合物粉体。可以先在中低温(例如250~400℃)进行脱氨反应,再于650~1000℃(优选650~950℃)保持1~24h(例如10h)恒温烧结。烧结时,可以使用惰性气体作为烧结炉保护气体,例如使用气氛可与是氩气、氮气中的一种或几种。The granulated powder is further sintered by a traditional solid-phase synthesis method and sintered at a high temperature in an atmosphere furnace to obtain a carbon-coated titanium phosphate compound powder. The deamination reaction can be carried out at medium and low temperature (for example, 250-400° C.), and then sintered at a constant temperature of 650-1000° C. (preferably 650-950° C.) for 1-24 hours (for example, 10 hours). During sintering, an inert gas can be used as the protective gas in the sintering furnace, for example, the atmosphere can be one or more of argon and nitrogen.
本发明使用几种特定的原料,通过分步球磨方法获得具有一定黏度和粒径的浆料。通过对浆料的进一步喷雾干燥处理,得到混合均匀,分散良好的前驱体粉体,在特定的烧结条件下进行固相反应合成碳包覆的磷酸钛化合物粉体。本发明工艺简单、成本低,球磨均匀,粉体分散度好。采用离心式喷雾干燥方式得到的粉体颗粒成球形,使得磷酸钛化合物易被碳包覆,尤其可避免传统固相反应中的因为混料不均造成的高温反应成分不均匀,粉体烧结中出现其他晶相杂质。此发明适用于批量生产碳包覆的磷酸钛化合物。本发明关键点在于,区别于传统的固相合成法,采用球磨制作浆料联合喷雾干燥造粒的方式,得到的粉体颗粒成球形,使得磷酸钛化合物易被碳包覆,成功的制备碳包覆的磷酸钛化合物粉体,采用高温固相合成方法,使用气氛炉,先在中低温进行脱氨反应,在一定温度保持一段时间,得到晶相纯度高的碳包覆的磷酸钛化合物陶瓷粉体。The invention uses several specific raw materials to obtain slurry with a certain viscosity and particle size through a step-by-step ball milling method. Through further spray drying treatment of the slurry, the precursor powder with uniform mixing and good dispersion is obtained, and the carbon-coated titanium phosphate compound powder is synthesized by solid-phase reaction under specific sintering conditions. The invention has the advantages of simple process, low cost, uniform ball milling and good powder dispersion. The powder particles obtained by the centrifugal spray drying method are spherical, so that the titanium phosphate compound is easily coated with carbon, which can especially avoid the uneven high-temperature reaction components caused by uneven mixing in the traditional solid-phase reaction. Other crystalline phase impurities appear. This invention is suitable for mass production of carbon-coated titanium phosphate compounds. The key point of the present invention is that, different from the traditional solid-phase synthesis method, the method of making slurry by ball milling and spray drying granulation is adopted, and the obtained powder particles are spherical, so that the titanium phosphate compound is easily coated with carbon, and carbon is successfully prepared. The coated titanium phosphate compound powder adopts a high-temperature solid-phase synthesis method and uses an atmosphere furnace to perform deamination reaction at a medium and low temperature, and maintain it at a certain temperature for a period of time to obtain a carbon-coated titanium phosphate compound ceramic with high crystal phase purity. powder.
图2、3示出本发明一个实施例所制备的碳包覆的磷酸钛化合物粉体的SEM图和粒度分布图,可以看出粒径大小在1~10μm左右,制备的粉体分散均匀,碳包覆性好。图4示出本发明一个实施例所制备的碳包覆的磷酸钛化合物粉体的XRD图,结果显示烧结后的陶瓷粉体晶体纯度较高,无杂峰,结合原子吸收光谱法测得碳包覆的磷酸钛化合物含量95-99.9%,优选99.9%。2 and 3 show the SEM image and particle size distribution diagram of the carbon-coated titanium phosphate compound powder prepared by an embodiment of the present invention, it can be seen that the particle size is about 1-10 μm, and the prepared powder is uniformly dispersed. Good carbon coating. FIG. 4 shows the XRD pattern of the carbon-coated titanium phosphate compound powder prepared by an embodiment of the present invention. The results show that the sintered ceramic powder has a relatively high crystal purity and no impurity peaks. Combined with atomic absorption spectrometry, carbon is measured by atomic absorption spectrometry. The content of the coated titanium phosphate compound is 95-99.9%, preferably 99.9%.
下面进一步例举实施例以详细说明本发明。同样应理解,以下实施例只用于对本发明进行进一步说明,不能理解为对本发明保护范围的限制,本领域的技术人员根据本发明的上述内容作出的一些非本质的改进和调整均属于本发明的保护范围。下述示例具体的工艺参数等也仅是合适范围中的一个示例,即本领域技术人员可以通过本文的说明做合适的范围内选择,而并非要限定于下文示例的具体数值。The following further examples are given to illustrate the present invention in detail. It should also be understood that the following examples are only used to further illustrate the present invention, and should not be construed as limiting the protection scope of the present invention. Some non-essential improvements and adjustments made by those skilled in the art according to the above content of the present invention belong to the present invention. scope of protection. The specific process parameters and the like in the following examples are only an example of a suitable range, that is, those skilled in the art can make selections within the suitable range through the description herein, and are not intended to be limited to the specific numerical values exemplified below.
实施例1Example 1
将碳酸钠、磷酸二氢氨铵、二氧化钛粉体为原料,钠、钛、磷的含量按摩尔比1:2:3加入乙醇和水(1:10)的混合液中,原料粉体与乙醇和水的混合液的质量比为30:70。选取聚丙烯酸作为分散剂,分散剂的添加量为粉体的1wt.%,通过粗磨机高速200转/分钟球磨2h获得均匀的浆料。继续加入通过乙醇预处理的活性物质石墨20wt.%),进一步以200转/分钟转速球磨2h后倒出浆料。将得到的浆料采用喷雾干燥方法,设定进风温度220℃,出风温度110℃,离心转速12000转/分,收集得到的球形粉体前驱物。将前驱物放入惰性气体填充烧结炉,在750℃氮气气氛下烧结10h后即可获得碳包覆的磷酸钛化合物陶瓷粉体。其SEM图、粒度分布图和XRD图可分别参见图2~4。Sodium carbonate, ammonium dihydrogen phosphate, and titanium dioxide powder are used as raw materials. The mass ratio of the mixture with water is 30:70. Polyacrylic acid was selected as the dispersant, and the addition amount of the dispersant was 1 wt. % of the powder, and a uniform slurry was obtained by ball milling at a high speed of 200 rpm in a coarse mill for 2 hours. Continue to add the active material graphite pretreated by ethanol 20wt.%), further ball mill at 200 r/min for 2 h, and then pour out the slurry. The obtained slurry was spray-dried, and the inlet air temperature was set at 220° C., the outlet air temperature was 110° C., and the centrifugal speed was 12,000 rpm, and the obtained spherical powder precursor was collected. The precursor is put into an inert gas filled sintering furnace, and carbon-coated titanium phosphate ceramic powder can be obtained after sintering in a nitrogen atmosphere at 750°C for 10 hours. The SEM image, particle size distribution image and XRD image can be seen in Figures 2-4, respectively.
实施例2Example 2
将碳酸锂、磷酸二氢氨铵、二氧化钛粉体为原料,锂、钛、磷的含量按摩尔比1:2:3加入乙醇和水(1:10)的混合液中,原料粉体与乙醇和水的混合液的质量比为30:70。选取六偏磷酸钠作为分散剂,分散剂的添加量为粉体的1wt.%,通过粗磨机高速200转/分钟球磨2h获得均匀的浆料。继续加入通过乙醇预处理的活性物质石墨20wt.%),进一步以200转/分钟转速球磨2h后倒出浆料。将得到的浆料采用喷雾干燥方法,设定进风温度220℃,出风温度110℃,离心转速15000转/分,收集得到的球形粉体前驱物。将前驱物放入惰性气体填充烧结炉,在750℃氮气气氛下烧结10h后即可获得碳包覆的磷酸钛化合物陶瓷粉体。Lithium carbonate, ammonium dihydrogen phosphate, and titanium dioxide powder are used as raw materials, and the content of lithium, titanium, and phosphorus is added to a mixture of ethanol and water (1:10) in a molar ratio of 1:2:3, and the raw material powder is mixed with ethanol. The mass ratio of the mixture with water is 30:70. Sodium hexametaphosphate was selected as the dispersant, and the addition amount of the dispersant was 1 wt.% of the powder, and a uniform slurry was obtained by ball milling at a high speed of 200 rpm in a coarse mill for 2 hours. Continue to add the active material graphite pretreated by ethanol 20wt.%), further ball mill at 200 r/min for 2 h, and then pour out the slurry. The obtained slurry is spray-dried, the inlet air temperature is set to 220°C, the outlet air temperature is 110°C, and the centrifugal rotation speed is 15,000 rpm, and the obtained spherical powder precursor is collected. The precursor is put into an inert gas filled sintering furnace, and carbon-coated titanium phosphate ceramic powder can be obtained after sintering in a nitrogen atmosphere at 750°C for 10 hours.
实施例3Example 3
将碳酸钠、磷酸二氢氨铵、二氧化钛粉体为原料,钾、钛、磷的含量按摩尔比1:2:3加入乙醇和水(1:10)的混合液中,原料粉体与乙醇和水的混合液的质量比为20:80。选取蓖麻油作为分散剂,分散剂的添加量为粉体的1wt.%,通过粗磨机高速200转/分钟球磨2h获得均匀的浆料。继续加入通过乙醇预处理的活性物质石墨20wt.%),进一步以200转/分钟转速球磨2h后倒出浆料。将得到的浆料采用喷雾干燥方法,设定进风温度220℃,出风温度110℃,离心转速17000转/分,收集得到的球形粉体前驱物。将前驱物放入惰性气体填充烧结炉,在750℃氮气气氛下烧结10h后即可获得碳包覆的磷酸钛化合物陶瓷粉体。Sodium carbonate, ammonium dihydrogen phosphate, and titanium dioxide powder are used as raw materials, and the contents of potassium, titanium and phosphorus are added to the mixture of ethanol and water (1:10) in a molar ratio of 1:2:3, and the raw material powder is mixed with ethanol. The mass ratio of the mixture with water is 20:80. Castor oil was selected as the dispersant, and the addition amount of the dispersant was 1 wt.% of the powder, and a uniform slurry was obtained by ball milling at a high speed of 200 rpm in a coarse mill for 2 hours. Continue to add the active material graphite pretreated by ethanol 20wt.%), further ball mill at 200 r/min for 2 h, and then pour out the slurry. The obtained slurry was spray-dried, and the inlet air temperature was set at 220° C., the outlet air temperature was 110° C., and the centrifugal speed was 17,000 rpm, and the obtained spherical powder precursor was collected. The precursor is put into an inert gas filled sintering furnace, and carbon-coated titanium phosphate ceramic powder can be obtained after sintering in a nitrogen atmosphere at 750°C for 10 hours.
产业应用性:本发明的方法降低了碳包覆的磷酸钛化合物陶瓷粉生产成本,提高了生产的粉体纯度和性能,为水系钠离子电极的商业化生产奠定基础。Industrial applicability: The method of the present invention reduces the production cost of carbon-coated titanium phosphate compound ceramic powder, improves the purity and performance of the produced powder, and lays a foundation for the commercial production of aqueous sodium ion electrodes.
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