CN1260118C - Preparation for metal sulfide - Google Patents
Preparation for metal sulfide Download PDFInfo
- Publication number
- CN1260118C CN1260118C CN 200410060903 CN200410060903A CN1260118C CN 1260118 C CN1260118 C CN 1260118C CN 200410060903 CN200410060903 CN 200410060903 CN 200410060903 A CN200410060903 A CN 200410060903A CN 1260118 C CN1260118 C CN 1260118C
- Authority
- CN
- China
- Prior art keywords
- metal
- sulfide
- sulfur
- elemental sulfur
- organic solvent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 229910052976 metal sulfide Inorganic materials 0.000 title claims abstract description 50
- 238000002360 preparation method Methods 0.000 title claims description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 61
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000002184 metal Substances 0.000 claims abstract description 50
- 238000000034 method Methods 0.000 claims abstract description 34
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 239000003960 organic solvent Substances 0.000 claims abstract description 18
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000002131 composite material Substances 0.000 claims abstract description 10
- 229910052717 sulfur Inorganic materials 0.000 claims description 23
- 239000011593 sulfur Substances 0.000 claims description 23
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 229910052723 transition metal Inorganic materials 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 5
- 239000000956 alloy Substances 0.000 claims description 4
- 229910045601 alloy Inorganic materials 0.000 claims description 4
- 239000002608 ionic liquid Substances 0.000 claims description 2
- 150000002576 ketones Chemical class 0.000 claims description 2
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 1
- 150000001348 alkyl chlorides Chemical class 0.000 claims 1
- 239000011164 primary particle Substances 0.000 claims 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims 1
- 239000000843 powder Substances 0.000 abstract description 18
- 239000002994 raw material Substances 0.000 abstract description 15
- 239000000463 material Substances 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000003054 catalyst Substances 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract description 4
- 239000002341 toxic gas Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 2
- 230000002349 favourable effect Effects 0.000 abstract 1
- 230000002194 synthesizing effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 31
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 24
- 150000004763 sulfides Chemical class 0.000 description 10
- 238000002441 X-ray diffraction Methods 0.000 description 9
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 238000002149 energy-dispersive X-ray emission spectroscopy Methods 0.000 description 6
- 238000004729 solvothermal method Methods 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 238000000151 deposition Methods 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- -1 sulfides of Fe Chemical class 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 238000001027 hydrothermal synthesis Methods 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000005486 sulfidation Methods 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- LGXVIGDEPROXKC-UHFFFAOYSA-N 1,1-dichloroethene Chemical group ClC(Cl)=C LGXVIGDEPROXKC-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- QVYYOKWPCQYKEY-UHFFFAOYSA-N [Fe].[Co] Chemical compound [Fe].[Co] QVYYOKWPCQYKEY-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- 229960001701 chloroform Drugs 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007323 disproportionation reaction Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910001510 metal chloride Inorganic materials 0.000 description 1
- 229910001960 metal nitrate Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000011027 product recovery Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 150000003222 pyridines Chemical class 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Carbon And Carbon Compounds (AREA)
- Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种金属硫化物的制备方法。The invention relates to a method for preparing metal sulfides.
背景技术Background technique
许多金属硫化物表现出优异的光电、热电、电磁以及半导体等物理性能,在物理电、磁器件中具有广泛的用途。同样,许多金属硫化物(如Mo、W等的硫化物)在化学中具有优异的催化性能;另外,一些硫化物(如Fe、Co、Ni的硫化物)还可用作中低温电池的正负极材料。但由于受到合成方法的限制,硫化物材料很难进行批量生产。Many metal sulfides exhibit excellent photoelectric, thermoelectric, electromagnetic and semiconducting physical properties, and have a wide range of uses in physical electrical and magnetic devices. Similarly, many metal sulfides (such as sulfides of Mo, W, etc.) have excellent catalytic properties in chemistry; in addition, some sulfides (such as sulfides of Fe, Co, Ni) can also be used as positive catalysts for medium and low temperature batteries. Negative material. However, due to the limitations of the synthesis method, sulfide materials are difficult to mass-produce.
一般来说,金属硫化物可由金属单质和硫一起混合反应进行制备。许多情况下,由于低温下固固反应难以发生,硫化物(如许多过渡金属硫化物)的制备一般在较高的温度下进行。其反应过程为:Generally speaking, metal sulfides can be prepared by mixing and reacting elemental metal and sulfur together. In many cases, the preparation of sulfides (such as many transition metal sulfides) is generally carried out at higher temperatures because solidification reactions are difficult to occur at low temperatures. Its reaction process is:
为避免被氧气氧化,反应器需密封。由于高温下硫蒸气具有强烈腐蚀性,一般只能采用石英反应器。该方法中,一般在真空环境下将反应物密封到石英反应器内在进行高温灼烧。由于,一方面,高温下硫蒸气压过高;另一方面,金属与硫蒸气的反应过程非常剧烈,往往呈爆炸式,而石英并非良好的耐压材料,因而该方法具有很大危险性。操作复杂和潜在的巨大的危险性使得该方法不适宜金属硫化物的批量生产。To avoid oxidation by oxygen, the reactor needs to be sealed. Due to the strong corrosiveness of sulfur vapor at high temperatures, generally only quartz reactors can be used. In this method, the reactant is generally sealed in a quartz reactor in a vacuum environment and burned at a high temperature. Because, on the one hand, the sulfur vapor pressure is too high at high temperature; on the other hand, the reaction process between metal and sulfur vapor is very violent and often explosive, and quartz is not a good pressure-resistant material, so this method is very dangerous. The complicated operation and huge potential danger make this method unsuitable for mass production of metal sulfides.
蒸气压较低容易被还原的硫化物取代单质硫有时被用来制备稳定性更好的硫化物(如公开号为CN:1086493A的专利所述)可以降低硫化反应对反应器材料的要求,但显然带来了制备方法的复杂化,并导致产物中引入不必要的金属杂质元素。Vapor pressure is lower and easily reduced sulfide replaces elemental sulfur and is sometimes used to prepare sulfide with better stability (as described in the patent of CN: 1086493A), which can reduce the requirement of sulfidation reaction on the reactor material, but Obviously, the preparation method is complicated, and unnecessary metal impurity elements are introduced into the product.
将金属氧化物、金属盐在200~500℃的硫化氢中硫化可以获得预期产物;一些金属硫化物可以通过金属的水溶性盐与硫的水溶性盐在水相中沉积制备,但许多情况下产物往往是非晶态且易含有OH基,将这种产物作为前驱物在高温硫化氢气体中处理有可能得到各种硫化物及复合硫化物(Inorganic Chemistry,42,1764(2003))。这些方法合成的产物结晶性往往较差,且涉及到有毒气体H2S的大量使用。类似的方法还有在300℃以上将金属盐与Na2S2等反应制备金属硫化物,产物与副产品混合在一起形成固融体(J.Chem.SoC.DaltonTrans.,12,1872(2001)。此外还包括极为相近的氯化物法(Inorganic Chemistry,20,2631(1981))、硫酸盐法(Inorganic Chemistry,23,872(1984))等硫化物制备方法。The desired product can be obtained by vulcanizing metal oxides and metal salts in hydrogen sulfide at 200-500 ° C; some metal sulfides can be prepared by depositing water-soluble salts of metals and water-soluble salts of sulfur in aqueous phase, but in many cases The product is often amorphous and easily contains OH groups. It is possible to obtain various sulfides and complex sulfides by treating this product as a precursor in high-temperature hydrogen sulfide gas (Inorganic Chemistry, 42, 1764 (2003)). The products synthesized by these methods are often poor in crystallinity, and involve a large amount of toxic gas H 2 S to be used. A similar method is to prepare metal sulfides by reacting metal salts with Na 2 S 2 etc. above 300°C, and the products and by-products are mixed together to form a solid solution (J.Chem.SoC.DaltonTrans., 12, 1872 (2001) In addition, it also includes the very similar chloride method (Inorganic Chemistry, 20, 2631 (1981)), sulfate method (Inorganic Chemistry, 23, 872 (1984)) and other sulfide preparation methods.
含硫的金属有机化合物热分解法(J.Solid State chem.,101,115(1992);109,70(1994))也是制备少量硫化物的常用方法,显然具有原料昂贵等诸多缺点。Thermal decomposition of sulfur-containing metal-organic compounds (J. Solid State chem., 101, 115 (1992); 109, 70 (1994)) is also a common method for preparing a small amount of sulfide, which obviously has many disadvantages such as expensive raw materials.
作为催化剂及电池材料,硫铁矿性硫化物(FeS2、CoS2等)的制备采用了一种称为水热法的方法。例如特开昭59-183831的方法以七水硫酸亚铁、硫化钠、硫为原料水热法合成了FeS2。类似地,文献(北京科技大学学报,18(1),69(1996))以七水硫酸亚铁、硫代硫酸钠、硫在去离子水中于200℃水热合成FeS2,发现反应受PH值影响较大而不宜控制,且产物回收率较低。采用水溶液法制备金属硫化物的一个不利因素是金属硫化物易于发生水解。As catalysts and battery materials, pyrite sulfides (FeS 2 , CoS 2 , etc.) are produced using a method called hydrothermal method. For example, the method of JP-A-59-183831 synthesized FeS 2 by hydrothermal method using ferrous sulfate heptahydrate, sodium sulfide and sulfur as raw materials. Similarly, the literature (Journal of Beijing University of Science and Technology, 18(1), 69(1996)) synthesized FeS 2 by ferrous sulfate heptahydrate, sodium thiosulfate and sulfur in deionized water at 200°C, and found that the reaction was affected by pH The value has a great influence and should not be controlled, and the product recovery rate is low. One disadvantage of the aqueous solution method for preparing metal sulfides is that metal sulfides are prone to hydrolysis.
与此相对应,溶剂热法也被用来制备金属硫化物。文献(J.Solid State Chem.,146,484(1999))报道了一种方法,以金属硝酸盐、氯化物盐或者硫酸盐与过量S为原料,在有机溶剂中于120℃溶剂热反应制备了多种单一金属元素的过渡金属硫化物。该反应利用硫的歧化反应实现金属元素的硫化,但同时也导致SCl2等有毒气体的大量生成。文献(Mater.Chem.Phys.,66(1),97(2000))报道以无水金属氯化物与Na2S3在有机溶剂中于180℃溶剂热法制备了FeS2、CoS2,该法中原料不易获得。Correspondingly, the solvothermal method has also been used to prepare metal sulfides. The literature (J.Solid State Chem., 146, 484 (1999)) reported a method, using metal nitrate, chloride salt or sulfate and excess S as raw materials, in an organic solvent at 120 ℃ solvothermal reaction preparation Transition metal sulfides of a variety of single metal elements. This reaction utilizes the disproportionation reaction of sulfur to realize the sulfidation of metal elements, but at the same time it also leads to the generation of a large amount of toxic gases such as SCl 2 . Literature (Mater.Chem.Phys., 66(1), 97(2000)) reported that FeS 2 and CoS 2 were prepared by solvothermal method of anhydrous metal chloride and Na 2 S 3 in an organic solvent at 180°C. Raw materials are not easy to obtain in France.
室温条件下,比如,铜粉与固态的硫粉混合几乎不会发生反应;但若将硫溶于丙酮,则可与金属铜反应生成Cu2S。显然,溶解于有机溶剂可以提高S的反应活性,但一方面,在常温常压下,这种固液相反应很难进行完全,不易获得高纯产物;另一方面许多硫铁矿型硫化物(FeS2、CoS2、NiS2等)在常温常压下根本无法通过该方法生成,因而,常规条件下不太可能用这种方法来大量制备金属硫化物。At room temperature, for example, mixing copper powder with solid sulfur powder hardly reacts; but if sulfur is dissolved in acetone, it can react with metallic copper to form Cu 2 S. Obviously, dissolving in an organic solvent can increase the reactivity of S, but on the one hand, at normal temperature and pressure, this solid-liquid phase reaction is difficult to complete, and it is difficult to obtain high-purity products; on the other hand, many pyrite-type sulfides (FeS 2 , CoS 2 , NiS 2 , etc.) cannot be produced by this method at normal temperature and pressure. Therefore, it is impossible to use this method to prepare a large amount of metal sulfides under normal conditions.
发明内容:Invention content:
本发明的目的是提供一种金属硫化物的制备方法,该方法简单、生产成本低、环境相对友好且利于批量生产。The purpose of the present invention is to provide a method for preparing metal sulfides, which is simple, low in production cost, relatively friendly to the environment and conducive to mass production.
本发明提供的技术方案是:金属硫化物的制备方法,将单质硫与金属(Me)或者金属低硫化物(MeSx)一起置于在有机溶剂中,通过溶剂热法使所述的组分在100~500℃、20~800个大气压下反应6~120小时,制备金属硫化物MeSy(其中y>0,0<x<y)。其中,金属低硫化物是指与目标产物金属硫化物相比,其硫的化学计量比含量低。本发明所述的“金属(Me)”可以只含单一金属元素,也可以是两种及以上金属元素的组合物。如金属可以包括单质、合金、金属混合物等,而金属硫化物可以是只有一种金属元素的硫化物,也可以是包含两种及以上金属元素的复合金属硫化物。金属硫化物是指金属与硫以键合作用组成的金属含硫物。The technical scheme provided by the invention is: the preparation method of metal sulfide, elemental sulfur and metal (Me) or metal subsulfide (MeS x ) are placed in an organic solvent, and the components are made by solvothermal method React at 100-500° C. and 20-800 atmospheres for 6-120 hours to prepare metal sulfide MeS y (where y>0, 0<x<y). Among them, the metal low sulfide means that the stoichiometric content of sulfur is lower than that of the target metal sulfide. The "metal (Me)" mentioned in the present invention may only contain a single metal element, or may be a combination of two or more metal elements. For example, metals can include simple substances, alloys, metal mixtures, etc., while metal sulfides can be sulfides with only one metal element, or composite metal sulfides containing two or more metal elements. Metal sulfides refer to metal sulfides composed of metal and sulfur through bonding.
所述金属包含至少一种及以上过渡金属元素。The metal contains at least one or more transition metal elements.
上述金属或者金属低硫化物的基本粒子粒径小于50微米。The basic particle size of the above-mentioned metal or metal subsulfide is less than 50 microns.
所用的有机溶剂可以是氯烷烃类(如三氯甲烷、四氯化碳等)、氯烯烃类(如二氯乙烯)、含苯环类(如苯、甲苯等)、含硫有机溶剂(如二硫化碳等)以及各种醚类、酮类、醇类、甘油类、吡啶类、离子液体类中的至少一种。The organic solvent used can be chloralkane (such as trichloromethane, carbon tetrachloride etc.), chloroalkene (such as dichloroethylene), containing benzene ring class (such as benzene, toluene etc.), sulfur-containing organic solvent (such as carbon disulfide, etc.) and at least one of various ethers, ketones, alcohols, glycerol, pyridines, and ionic liquids.
上述原料中硫的加入量为刚好生成MeSy或者过量,优选单质硫的加入量为化学反应量的1.01~1.03倍。The added amount of sulfur in the above raw materials is just enough to form MeS y or in excess, preferably the added amount of elemental sulfur is 1.01-1.03 times of the chemical reaction amount.
其中所述的通过溶剂热法进行反应的时间不超过5天。The time for carrying out the reaction by the solvothermal method described therein is no more than 5 days.
所制备的硫化物MeSy包括含有过渡金属元素的硫化物催化剂以及硫铁矿型的过渡金属二硫化物。The prepared sulfide MeS y includes a sulfide catalyst containing transition metal elements and a pyrite-type transition metal dichalcogenide.
与现有技术相比,本发明主要是利用一定温度压力下溶解硫的高反应活性,与金属或者金属低硫化物直接发生加成发应,从而在较为温和的环境下制备一些功能性的金属硫化物材料。本发明方法具有:实施过程的危险性相对金属与硫单质的直接高温合成法而言显著降低;不涉及有毒气体的大量使用或者生成;原材料成本低且易于获得;生产工艺简单、反应条件易于控制;利于金属硫化物材料的批量生产等明显优势。本发明可用来制备只含有单一金属元素的金属硫化物或者包含多种金属元素组成的复合金属硫化物。Compared with the prior art, the present invention mainly uses the high reactivity of dissolved sulfur at a certain temperature and pressure to directly react with metals or metal low sulfides, thereby preparing some functional metals in a milder environment. Sulfide material. The method of the present invention has the following advantages: compared with the direct high-temperature synthesis method of metal and sulfur, the risk of the implementation process is significantly reduced; it does not involve the use or generation of toxic gases in large quantities; the cost of raw materials is low and easy to obtain; the production process is simple and the reaction conditions are easy to control ; Conducive to the mass production of metal sulfide materials and other obvious advantages. The invention can be used to prepare metal sulfides containing only a single metal element or composite metal sulfides composed of multiple metal elements.
附图说明Description of drawings
附图是采用本发明方法制备的几种金属硫化物的X射线分析曲线。其中(a)SnS、(b)NiS2、(c)CoS2、(d)FeS2、(e)Fe0.7Co0.3S2。Accompanying drawing is the X-ray analysis curve of several metal sulfides prepared by the inventive method. Among them (a) SnS, (b) NiS 2 , (c) CoS 2 , (d) FeS 2 , (e) Fe 0.7 Co 0.3 S 2 .
具体实施方式Detailed ways
本发明中用来制备金属硫化物的原料包括金属组分和单质硫,其中金属组分在本发明中定义为可以是金属单质、合金、金属混合物等,也可以是比目标产物含硫量低的易于制备的其他形式的金属硫化物以及复合金属硫化物。将金属组分粉末与单质硫以及能溶解硫的有机溶剂一起置于高压反应釜内,在100~500℃的温度范围内加热,加热期间,对反应釜内的物质施加1~800个大气压的压力,通过该溶剂热反应,金属硫化物或者复合金属硫化物就会相对容易的产生。The raw materials used to prepare metal sulfides in the present invention include metal components and elemental sulfur, wherein the metal components are defined in the present invention as metal elements, alloys, metal mixtures, etc., and can also be lower than the target product sulfur content Other forms of metal sulfides and complex metal sulfides are readily prepared. Put the metal component powder together with elemental sulfur and an organic solvent capable of dissolving sulfur in a high-pressure reactor, and heat it in the temperature range of 100-500 ° C. During the heating period, 1-800 atmospheres of pressure are applied to the contents of the reactor. Pressure, through the solvothermal reaction, metal sulfides or composite metal sulfides are relatively easy to produce.
在反应釜加料时,金属组分粉末与单质硫不必均匀混合。由于有机溶剂可以溶解硫,在反应开始后,有机溶剂将硫运输到需要的地方从而可保障单质硫的按需供给。这种硫的供给方式类似血液中氧的供给,具有高效和均匀性。When feeding the reactor, the metal component powder and the elemental sulfur do not have to be uniformly mixed. Since the organic solvent can dissolve sulfur, after the reaction starts, the organic solvent transports the sulfur to the place where it is needed, thus ensuring the on-demand supply of elemental sulfur. This supply of sulfur is similar to the supply of oxygen in the blood, with high efficiency and uniformity.
反应过程相当于一种加热加压下的固液相反应,一方面,加热加压的溶解硫具有很高的反应活性,可以直接与金属组分发生反应生成目标产物,另一方面,加热加压的环境有利于硫的固相扩散从而实现金属组分粉末的完全硫化。采用更小尺寸(小于50微米)的金属组分粉末及延长反应时间都有利于获得高纯的目标金属硫化物。整个反应时间视目标产物及原料性质不同而有所差异,一般不超过5天。The reaction process is equivalent to a solid-liquid phase reaction under heat and pressure. On the one hand, the dissolved sulfur under heat and pressure has high reactivity and can directly react with metal components to form the target product. The pressurized environment is conducive to the solid-phase diffusion of sulfur to achieve complete vulcanization of the metal component powder. The use of metal component powders with a smaller size (less than 50 microns) and prolonged reaction time are beneficial to obtaining high-purity target metal sulfides. The entire reaction time varies depending on the properties of the target product and raw materials, and generally does not exceed 5 days.
金属硫化物在有机溶剂中一般不溶解,不水解,因而在反应器中以固体的形式存在,易于实现产物分离。本发明制备的产物为金属硫化物粉末,其基本粒子尺寸一般小于5微米,可直接用作催化剂或者电池材料。本发明在制备金属硫化物时单质硫有时适当过量,过量的硫一般溶解在有机溶剂中,过滤即可除去。但由于产物比表面积太大,易吸附少量有机溶剂及单质硫,因此,产物一般要用二硫化碳等溶剂洗涤以除去其中残存的有机溶剂及单质硫。Metal sulfides are generally insoluble in organic solvents and are not hydrolyzed, so they exist in the form of solids in the reactor, which is easy to achieve product separation. The product prepared by the invention is metal sulfide powder, the basic particle size of which is generally less than 5 microns, and can be directly used as catalyst or battery material. In the present invention, when preparing metal sulfides, the elemental sulfur is sometimes appropriately excessive, and the excess sulfur is generally dissolved in an organic solvent and can be removed by filtration. However, due to the large specific surface area of the product, it is easy to absorb a small amount of organic solvent and elemental sulfur. Therefore, the product is generally washed with a solvent such as carbon disulfide to remove the remaining organic solvent and elemental sulfur.
在制备复合金属硫化物时,若以金属为原料,则原料中各种金属元素之间必须高度分散,比如使用合金粉末或者分散非常均匀的金属粉末混合物作为金属组分原料。When preparing composite metal sulfides, if metal is used as the raw material, the various metal elements in the raw material must be highly dispersed, for example, alloy powder or a very uniformly dispersed metal powder mixture is used as the metal component raw material.
另一种方式是高度分散的含硫量低复合硫化物作为制备复合金属硫化物的金属组分原料。特别的,比如,制备FexCo(1-x)S2(0<x<1)时,可以通过水溶液共沉积的方法获得高分散的复合金属一硫化物FexCo(1-x)S(0<x<1)作为金属组分原料。虽然,有结果表明这种水溶液共沉积法制备的FexCo(1-x)S(0<x<1)中可能含有少量的羟基,但实验结果表明这并不影响目标产物的制备。Another way is to use highly dispersed composite sulfides with low sulfur content as the metal component raw materials for preparing composite metal sulfides. In particular, for example, when preparing FexCo (1-x) S2 (0<x<1), highly dispersed composite metal-sulfide FexCo (1-x) S can be obtained by co-deposition in aqueous solution (0<x<1) as the metal component raw material. Although some results show that the FexCo (1-x) S (0<x<1) prepared by this aqueous co-deposition method may contain a small amount of hydroxyl groups, the experimental results show that this does not affect the preparation of the target product.
由于本发明在原料加入到高压釜中时可以采用紧密固态颗粒堆积的方式,因而可以提高单釜反应产量。本发明方法可以用来进行金属硫化物的批量生产。Since the present invention can adopt the compact solid particle packing mode when the raw materials are added into the autoclave, the single-pot reaction output can be improved. The method of the invention can be used for mass production of metal sulfides.
下面对本发明的实施例进行详细描述。Embodiments of the present invention are described in detail below.
实例1:将单质铜粉与单质硫按原子比2∶1共16克置于30ml高压反应釜内,加入丙酮至反应器的90%,将反应釜在20个大气压下110℃恒温3天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到Cu2S 15.3克,X射线分析结果表明产物为Cu2S。Example 1: Place 16 grams of elemental copper powder and elemental sulfur in an atomic ratio of 2:1 in a 30ml autoclave, add acetone to 90% of the reactor, and keep the reactor at 110°C for 3 days at 20 atmospheres. After natural cooling, the product powder was taken out by filtration, washed with carbon disulfide, and dried to obtain 15.3 g of Cu 2 S. X-ray analysis showed that the product was Cu 2 S.
实例2:将单质Sn粉与单质硫按原子比1∶1.03共12.8克置于30ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约300个大气压下在220℃恒温3天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到SnS 12.2克,X射线分析结果表明产物为SnS。Example 2: Put 12.8 grams of elemental Sn powder and elemental sulfur in an atomic ratio of 1:1.03 in a 30ml autoclave, and add toluene to 90% of the reactor. The reaction kettle was kept at a constant temperature of 220°C for 3 days under about 300 atmospheres. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 12.2 grams of SnS. X-ray analysis results showed that the product was SnS.
实例3:将10克金属镍粉与11.3克单质硫置于50ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约300个大气压220℃恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到NiS2 20.2克,X射线及EDX分析表明产物为NiS2。Example 3: 10 grams of metal nickel powder and 11.3 grams of elemental sulfur were placed in a 50 ml autoclave, and toluene was added to reach 90% of the reactor. The reaction kettle was kept at about 300 atmospheres at 220°C for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 20.2 g of NiS 2 . X-ray and EDX analysis showed that the product was NiS 2 .
实例4:将NiCl2.6H2O与Na2S.9H2O溶于水溶液制备得到NiS黑色沉淀,过滤、干燥得自制NiS。将36.9克自制的NiS粉与13.3克的单质硫置于100ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约200个大气压180℃恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到NiS2 47.8克,X射线及EDX分析表明产物为NiS2。Example 4: NiS black precipitate was obtained by dissolving NiCl 2 .6H 2 O and Na 2 S.9H 2 O in aqueous solution, which was filtered and dried to obtain self-made NiS. 36.9 grams of self-made NiS powder and 13.3 grams of elemental sulfur were placed in a 100ml autoclave, and toluene was added to 90% of the reactor. The reaction kettle was kept at about 200 atmospheres at 180°C for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 47.8 g of NiS 2 . X-ray and EDX analysis showed that the product was NiS 2 .
实例5:按实例3中的方法制备CoS。将14.7克CoS与5.3克的单质硫置于100ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约400个大气压250℃恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到CoS2 18.4克,X射线及EDX分析表明产物为CoS2。Example 5: Prepare CoS according to the method in Example 3. 14.7 g of CoS and 5.3 g of elemental sulfur were placed in a 100 ml autoclave, and toluene was added to 90% of the reactor. The reaction kettle was kept at a constant temperature of 250°C at about 400 atmospheres for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 18.4 g of CoS 2 . X-ray and EDX analysis showed that the product was CoS 2 .
实例6:按实例3中的方法制备CoS。将14.7克CoS与5.3克的单质硫置于100ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约800个大气压180℃恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到CoS2 18.4克,X射线及EDX分析表明产物为CoS2。Example 6: CoS was prepared according to the method in Example 3. 14.7 g of CoS and 5.3 g of elemental sulfur were placed in a 100 ml autoclave, and toluene was added to 90% of the reactor. The reaction kettle was kept at about 800 atmospheres at 180°C for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 18.4 g of CoS 2 . X-ray and EDX analysis showed that the product was CoS 2 .
实例7:按实例3中的方法制备FeS(由于FeS易氧化,制备时应采取适当的惰性气体保护措施)。将21.4克FeS与8.0克的单质硫置于50ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约300个大气压恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到FeS2 27.7克,X射线及EDX分析表明产物为FeS2。。Example 7: Prepare FeS according to the method in Example 3 (because FeS is easily oxidized, appropriate inert gas protection measures should be taken during preparation). 21.4 g of FeS and 8.0 g of elemental sulfur were placed in a 50 ml autoclave, and toluene was added to 90% of the reactor. The reaction kettle was kept at a constant temperature of about 300 atmospheres for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 27.7 g of FeS 2 . X-ray and EDX analysis showed that the product was FeS 2 . .
实例8:采用水溶液共沉积的方法制备Fe0.7Co0.3S,将10克Fe0.7Co0.3S与3.7克的单质硫置于30ml高压反应釜内,加入甲苯至反应器的90%。将反应釜在约400个大气压250℃恒温5天,自然冷却后过滤取出产物粉末,用二硫化碳洗涤、干燥,得到Fe0.7Co0.3S2复合硫化物12.5克,其X射线分析表明产物为硫铁矿结构,EDX分析表明铁钴计量比为2.33±0.05。Example 8: Preparation of Fe 0.7 Co 0.3 S by co-deposition in aqueous solution, 10 grams of Fe 0.7 Co 0.3 S and 3.7 grams of elemental sulfur were placed in a 30 ml autoclave, and toluene was added to 90% of the reactor. The reaction kettle was kept at a constant temperature of 250°C at about 400 atmospheres for 5 days. After natural cooling, the product powder was filtered out, washed with carbon disulfide, and dried to obtain 12.5 grams of Fe 0.7 Co 0.3 S 2 composite sulfide. The X-ray analysis showed that the product was sulfur iron Ore structure, EDX analysis shows that the iron-cobalt stoichiometric ratio is 2.33±0.05.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410060903 CN1260118C (en) | 2004-09-24 | 2004-09-24 | Preparation for metal sulfide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410060903 CN1260118C (en) | 2004-09-24 | 2004-09-24 | Preparation for metal sulfide |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1613750A CN1613750A (en) | 2005-05-11 |
CN1260118C true CN1260118C (en) | 2006-06-21 |
Family
ID=34764377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200410060903 Expired - Fee Related CN1260118C (en) | 2004-09-24 | 2004-09-24 | Preparation for metal sulfide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1260118C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101786650B (en) * | 2010-02-08 | 2011-11-02 | 许昌学院 | Chemical method for in situ synthesis of platy silver sulphide nano crystal photoelectric film at low temperature |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100436327C (en) * | 2006-09-29 | 2008-11-26 | 华侨大学 | Prepn process transition metal sulfide intercalated lithium |
CN101792931B (en) * | 2010-03-24 | 2012-07-25 | 南开大学 | Metal sulfide single crystal material and preparation method |
CN101857276A (en) * | 2010-06-21 | 2010-10-13 | 中国科学院苏州纳米技术与纳米仿生研究所 | A kind of preparation method of universal nano metal sulfide |
CN102642874B (en) * | 2012-04-27 | 2013-08-14 | 中南大学 | Ferrous disulfide semiconductor film preparation method |
CN103066254B (en) * | 2012-12-26 | 2015-05-27 | 浙江工业大学 | Sulfur/carbon composite material and application thereof |
CN103950890B (en) * | 2014-05-19 | 2015-08-19 | 合肥工业大学 | A kind of FeS 2the preparation method of pyrite microballoon and application thereof |
CN104495972B (en) * | 2014-12-08 | 2016-08-17 | 湖南科技大学 | The application of sulfuration arsenous |
PE20181344A1 (en) * | 2015-12-27 | 2018-08-21 | Metoxs Pte Ltd | SYSTEM FOR GENERATING H2S IN AN ALKALINE MEDIUM AND METHOD FOR USING THE SAME |
WO2018172813A2 (en) | 2017-03-21 | 2018-09-27 | The Petroleum Institute | Mechano-thermal preparation of zinc sulfide nanoparticles |
CN108190845A (en) * | 2018-01-31 | 2018-06-22 | 湖南省正源储能材料与器件研究所 | A kind of method for preparing lithium sulfide |
CN110589776B (en) * | 2019-10-28 | 2022-11-08 | 南昌航空大学 | A kind of method for synthesizing magnesium sulfide by mechanical ball milling |
CN110980815A (en) * | 2019-12-09 | 2020-04-10 | 吉林大学 | Method for preparing pyrite type iron disulfide by high-temperature high-pressure one-step chemical method |
CN112755960B (en) * | 2020-12-30 | 2023-04-28 | 四川省冶金地质勘查局六0五大队 | Sulfur-modified biochar, preparation method thereof, recyclable sulfur-modified biochar material and application |
CN114368775A (en) * | 2021-12-20 | 2022-04-19 | 江苏大学 | A kind of room temperature rapid preparation method of transition metal sulfide |
-
2004
- 2004-09-24 CN CN 200410060903 patent/CN1260118C/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101786650B (en) * | 2010-02-08 | 2011-11-02 | 许昌学院 | Chemical method for in situ synthesis of platy silver sulphide nano crystal photoelectric film at low temperature |
Also Published As
Publication number | Publication date |
---|---|
CN1613750A (en) | 2005-05-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1260118C (en) | Preparation for metal sulfide | |
Sui et al. | Low temperature synthesis of Cu2O crystals: shape evolution and growth mechanism | |
Lei et al. | Preparation of α-Mn2O3 and MnO from thermal decomposition of MnCO3 and control of morphology | |
JP5038389B2 (en) | Method for producing transition metal oxide nanoparticles | |
CN103143370B (en) | Preparation method of sulfide/graphene composite nano material | |
Li et al. | Effects of temperature on indium tin oxide particles synthesized by co-precipitation | |
CN110586117B (en) | A kind of Co3O4/CuMoO4 composite and its preparation method and application | |
Gaur et al. | Synthesis of SnS2 nanoparticles and their application as photocatalysts for the reduction of Cr (VI) | |
CN102633297A (en) | Preparation method of general-purpose multi-metal sulfide nano-material | |
CN112619648B (en) | Copper-cobalt-based catalyst for organic sulfur hydrolysis removal and preparation method thereof | |
Zhang et al. | Electroless-hydrothermal construction of nickel bridged nickel sulfide@ mesoporous carbon nitride hybrids for highly efficient noble metal-free photocatalytic H2 production | |
CN1289405C (en) | Wet chemical process of preparing low-dimensional nano nickel sulfide crystal | |
CN111036249A (en) | A kind of FexP/Mn0.3Cd0.7S composite photocatalyst and its preparation method and application | |
CN101823769A (en) | Method for preparing ternary FexCo1-xS2 powder | |
Parvizian et al. | Precursor chemistry of metal nitride nanocrystals | |
Jiang et al. | Review of different series of MOF/gC 3 N 4 composites for photocatalytic hydrogen production and CO 2 reduction | |
JPS6362446B2 (en) | ||
JP2011256090A (en) | Iron sulfide and method for producing the same | |
Yang et al. | Molten salt-mediated surface reconstruction induced orientation-growth of 1D/2D heterostructure for high-sensitivity H2S gas sensing | |
CN101376492A (en) | Preparation of transient metal chalcogenide compound | |
Li et al. | Solvothermal synthesis to NiE2 (E= Se, Te) nanorods at low temperature | |
CN101186346A (en) | Low-temperature solid-phase synthesis method of hexagonal nickel sulfide submicron crystals | |
Tarutani et al. | Thermal conversion of nanocrystalline metal hydroxide salts to metal carbides, pnictides, chalcogenides, and Halides | |
Sareen et al. | Synthesis and structural characterization of Cd (II) complexes based on acetylene dicarboxylate: A 1-D polymer as a precursor to CdO nanoparticles | |
Sriram et al. | Low‐Temperature Chemical Approaches for Synthesizing Sulfides and Nitrides of Reactive Transition Metals |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |