CN109879327B - Preparation of Fe by using metal oxide as catalyst3O4Method (2) - Google Patents

Preparation of Fe by using metal oxide as catalyst3O4Method (2) Download PDF

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CN109879327B
CN109879327B CN201910074047.5A CN201910074047A CN109879327B CN 109879327 B CN109879327 B CN 109879327B CN 201910074047 A CN201910074047 A CN 201910074047A CN 109879327 B CN109879327 B CN 109879327B
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邵斌
杨棋棋
周兴超
熊易
曾文
马毅龙
孙建春
陈登明
郭东林
李春红
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Chongqing University of Science and Technology
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Abstract

Preparation of Fe by using metal oxide catalyst3O4The method comprises the following steps: to Fe2+Adding metal M oxide powder into the solution, dispersing, adding an alkali solution to obtain a mixed solution, and carrying outHydrothermal reaction to obtain the product containing Fe3O4Suspension of the particles, separating the product Fe3O4(ii) a The metal M oxide is CuO or Cu2O, CoO or Co3O4At least one of (1). Compared with the traditional preparation method, the method utilizes CuO, Cu2O, CoO and Co3O4Etc. as catalyst, no need of adding oxidant, and under alkaline condition making Fe be separated from Fe2+One-step synthesis of high-purity micron-sized single-crystal octahedron Fe by using salt solution3O4The preparation method has the advantages of simple process, high efficiency, rapidness and low cost.

Description

Preparation of Fe by using metal oxide as catalyst3O4Method (2)
Technical Field
The invention relates to a preparation method of an iron compound, in particular to a method for preparing Fe by using metal oxide catalysis3O4The method of (1).
Background
China pickling millions of tons of iron oxide every year, resulting in a large Fe content2+The acid pickling waste liquid of (1). The Steel industry Water pollutant discharge Standard (GB 13456.2012) U specifies that the total iron content is less than 10 mg/L. However, in general steel pickling waste liquid, Fe is present at a concentration of more than 100g/L2+Ions cannot be directly discharged, and need to be subjected to harmless treatment. But discharged as waste liquid, a large amount of Fe2+Is wastedIt not only causes huge environmental burden, but also is an economic loss. Thus, Fe in the waste liquid2 +Conversion to economically valuable products is an urgent need.
Preparation of Fe by using pickling waste liquor as raw material3O4Is a method for recovering Fe2+The pathway of (1). Due to the higher Fe content, Fe3O4Can be directly smelted to make iron, and has application in the fields of pigment, magnetic material, medical biology, catalysis and the like, and has higher value. It has been newly discovered that single crystal octahedron of Fe3O4Has important function in the field of fuel cells.
In a conventional hydrothermal or coprecipitation process, by Fe2+Direct preparation of Fe by ion starting3O4Usually, an oxidant is needed, or a certain proportion of Fe is added3+And (3) salt. To obtain pure phase Fe3O4Supply amount of oxidizing agent and Fe2+With Fe3+The ratio of (a) to (b) needs to be closely regulated. If Fe cannot be controlled2+Oxidation of ions, FeOOH, Fe in the product2O3And the like, the post-treatment is difficult, and the economic cost is greatly increased. Thus, the conventional method is in actual Fe2+The difficulty in recovery is high.
The inventors found in previous studies that Fe was transformed into2+Adding Cu into the solution2+、Ni2+And Co2+Etc. can efficiently produce high-purity Fe3O4This method greatly simplifies the production process as compared with the conventional method, as described in patent document CN 108751262 a. Subsequent studies have further explored Cu2+、Ni2+And Co2+Salts of the same in the preparation of Fe3O4The novel preparation method is provided on the basis of the mechanism of (1).
Disclosure of Invention
In order to solve the technical problems, the invention provides a method for preparing Fe with simple process, high yield and high product purity3O4The method of (1).
The technical scheme is as follows:
catalysis by metal oxideChemical preparation of Fe3O4The key point of the method is that the method comprises the following steps:
to Fe2+Adding metal M oxide powder into the solution, dispersing, adding an alkali solution to obtain a mixed solution, and carrying out hydrothermal reaction on the mixed solution to obtain the Fe-containing iron oxide3O4Suspension of the particles, separating the product Fe3O4
The metal M oxide is CuO or Cu2O, CoO or Co3O4At least one of (1).
Preferably, the atomic percentage of the M element in the metal M oxide powder to the metal element in the mixed solution is M/(M + Fe) ═ 0.1 to 50 at.%.
Preferably, the atomic percentage of the M element in the metal M oxide powder to the metal element in the mixed solution is M/(M + Fe) ═ 1 to 10 at.%.
Preferably, the hydrothermal reaction is carried out at a temperature of 100 to 200 ℃.
Preferably, the hydrothermal reaction is carried out at a temperature of 120 to 150 ℃.
Preferably, the hydrothermal reaction time is 0.5-48 h.
According to a preferable technical scheme, the hydrothermal reaction time is 4-6 h.
Preferably, Fe is used as the main component2+Fe in solution2+The concentration of (b) is 0.01-5 mol/L.
Preferably, OH in the alkali solution is-The concentration of (b) is 0.2-8 mol/L.
Drawings
FIG. 1 is an X-ray diffraction (XRD) pattern of a sample prepared in a comparative example;
FIG. 2 is a sample XRD pattern prepared according to some of the examples, wherein: (a) example 8; (b) example 9 (top) and example 5 (bottom); (c) example 10; (d) example 11;
FIG. 3 is a typical Scanning Electron Microscope (SEM) picture and Energy Dispersive Spectroscopy (EDS) scan of a sample prepared with copper oxide as a catalyst.
Detailed Description
The invention is further illustrated by the following examples and figures.
(I) Fe3O4Preparation of
Preparation of Fe by using metal oxide catalyst3O4The method comprises the following steps:
to Fe2+Adding oxide powder of metal M into the solution and dispersing, wherein the addition amount is that M/(M + Fe) is 0.1-50 at%, calculated by the atomic percentage of M element in the metal M oxide powder and the total metal elements in the mixed suspension;
then stirring and adding an alkali solution to obtain a mixed solution, and carrying out hydrothermal reaction on the mixed solution to obtain the Fe-containing iron3O4Suspension of the particles, separating the product Fe3O4
The oxide of the metal M is CuO or Cu2O, CoO or Co3O4One or a combination of several of them. The product can be separated by centrifugation, filter membrane filtration, magnetic filtration and other modes, and when CuO or CuO is used as a catalyst, the CuO or CuO can be conveniently removed by magnetic filtration due to the non-magnetism.
The amounts of reactants, concentrations and reaction conditions of examples 1 to 20 and comparative examples are shown in Table 1, wherein the powder of the oxide of the metal M was added as a catalyst in each example, while the oxide of the metal M was not added in the comparative example, and the remaining steps were not changed. Wherein the hydrothermal reaction is carried out in a reaction kettle at the temperature of 100-200 ℃ for 0.5-48 h. It was found that the reaction time can be suitably shortened as the reaction temperature is higher, and the amount of the oxide powder of the metal M to be added can be suitably reduced. Therefore, the amount of the oxide powder catalyst to which the metal M is added can be adjusted according to the predetermined reaction temperature and time.
Said Fe2+The solution may be inorganic salt such as ferrous chloride and ferrous sulfate, or mixed salt thereof, or organic salt such as citrate and acetate, or mixed salt thereof. Fe2+Fe in solution2+The concentration of (b) is 0.01-5 mol/L.
The alkaline solution can be common inorganic alkali such as NaOH, KOH, LiOH and the like, and can also be organic alkali such as ammonia water, Polyethyleneimine (PEI) and the like; in addition, an inorganic base may be used in combination with an organic base, and when PEI is used, it may serve as both a dispersant to help disperse the metal oxide in the reaction system and itself as an alkaline agent. OH in alkaline solution-The concentration of (A) or the theoretical concentration of complete ionization is 0.2-8 mol/L. All reagents were purchased from Shanghai Aladdin Biotechnology Ltd.
Specifically, taking example 5 as an example, Fe was prepared3O4The process comprises the following steps:
preparing a reaction reagent: 0.02mol of FeSO is taken4Dissolving in 100ml water, preparing 0.2M ferrous sulfate solution for standby; dissolving 0.1mol of NaOH in 100ml of water, and preparing 1M NaOH solution for later use; taking CuO powder for later use.
Preparation of Fe3O4The process is as follows: 20ml of FeSO is taken4Adding the solution into a hydrothermal reaction kettle, then adding 0.03mmol of CuO powder, stirring and dispersing, and then dropwise adding 10ml of NaOH solution while stirring. And (3) sealing the hydrothermal reaction kettle, putting the hydrothermal reaction kettle into a constant-temperature oven, reacting for 1h at 120 ℃, and cooling to room temperature to obtain black suspension.
After the reaction is finished, filtering and separating solid particles from the black suspension by using a magnetic filter, washing and drying to obtain a product Fe3O4
The experimental process of the comparative example is similar, but the CuO powder is not added in the ferrous sulfate solution, the reaction is carried out for 4 hours at 150 ℃ after the NaOH solution is added, the product after the reaction is green, and the product is quickly oxidized to orange in the collecting process.
TABLE 1 reactants and reaction conditions for the different examples and comparative examples
Figure BDA0001958174660000041
Figure BDA0001958174660000051
Note: OH-The concentration is the OH present in the alkaline solution-And potentially theoretically ionizable OH-Concentration of (e.g. NH in aqueous ammonia solution)3·H2The concentration of O.
(II) product characterization
X-ray diffraction (XRD) analysis, Scanning Electron Microscope (SEM) analysis and energy spectrum analyzer (EDS) elemental analysis are common crystal characterization methods, wherein an XRD spectrum can reflect the crystal structure of a test sample, the appearance of the sample can be visually observed by means of the SEM, and the content of the elemental composition of the sample can be detected by the aid of the EDS.
Typical XRD patterns of the samples prepared by the above method are shown in fig. 1 and 2. FIG. 1 shows a sample prepared in a comparative example, from which it can be seen that the product is substantially FeOOH. Fe (OH) which is presumed to be green after the reaction is completed based on the color change of the product during the reaction2It rapidly oxidizes to orange-colored FeOOH during collection.
In fig. 2, XRD patterns of samples prepared by the following preparation methods are shown, respectively: (a) example 8; (b) example 9 (top) and example 5 (bottom); (c) example 10; (d) example 11. Known by a map, Fe can be prepared under various process conditions3O4And (4) crystals. With CuO, Cu2O is catalyst, and the product is Fe3O4The purity is high. With CoO and Co3O4The product obtained by separation contains trace impurities as a catalyst.
Comparison of the samples obtained in the comparative example and the examples shows that small amounts of CuO and Cu are added2O, CoO or Co3O4The powder enters a reaction system, namely the Fe under the alkaline condition can be changed2+In the direction of reaction of (2) to produce Fe3O4The orientation of the crystals proceeds, indicating the catalytic action of these several oxide powders. Compared with the traditional preparation method, the method has the advantages of simple preparation process, no need of strictly controlling the reaction system to be an oxidizing or reducing atmosphere, and strong adaptability to reaction conditions.
A typical SEM photograph of the sample was taken (a)And EDS spectra (b, c, d, e) are shown in FIG. 3, which sample was prepared by the method of example 5. In FIG. 3, (b), (c), and (d) are the area views of the elements O, Fe, and Cu, respectively, and the bright portions in the views represent the distribution regions of the respective elements. As can be seen, Fe was produced3O4The particles are octahedral single crystals, and the size of the particles is in the range of hundreds of nanometers to microns. The elemental analysis results showed that the product had a very low Cu content, with Cu/(Cu + Fe) ═ 0.63 at.%.
Has the advantages that: compared with the traditional preparation method, the method utilizes CuO and Cu2O、CoO、Co3O4Etc. as catalyst, no need of adding oxidant, and under alkaline condition making Fe be separated from Fe2+One-step synthesis of high-purity micron-sized single-crystal octahedron Fe by using salt solution3O4The preparation method has the advantages of simple process, high efficiency, rapidness and low cost. In addition, CuO and Cu2O, etc. are not magnetic, but Fe3O4Is a paramagnetic material, and can obtain Fe through magnetic recovery and separation in large-scale application3O4Therefore, the method has good industrial application prospect and is a harmless and recycling treatment method for the industrial steel pickling waste liquid.
Finally, it should be noted that the above-mentioned description is only a preferred embodiment of the present invention, and those skilled in the art can make various similar representations without departing from the spirit and scope of the present invention.

Claims (4)

1. Preparation of Fe by using metal oxide as catalyst3O4The method is characterized by comprising the following steps:
to Fe2+Adding metal M oxide powder into the solution, dispersing, adding an alkali solution to obtain a mixed solution, and carrying out hydrothermal reaction on the mixed solution to obtain the Fe-containing iron oxide3O4Suspension of the particles, separating the product Fe3O4
The metal M oxide is CuO or Cu2O, CoO or Co3O4At least one of;
the atomic percentage of the M element in the metal M oxide powder to the metal element in the mixed solution is M/(M + Fe) = 0.1-50 at.%;
the temperature of the hydrothermal reaction is 80-300 ℃;
the hydrothermal reaction time is 0.5-48 h;
the alkali solution is an inorganic alkali solution or an organic alkali solution or a mixed solution of the inorganic alkali solution and the organic alkali solution, wherein the inorganic alkali solution is one of a NaOH solution, a KOH solution, a LiOH solution or ammonia water, and the organic alkali solution is a Polyethyleneimine (PEI) solution;
said Fe2+Fe in solution2+The concentration of (A) is 0.01-5 mol/L;
OH in the alkali solution-The concentration of (b) is 0.2-8 mol/L.
2. The method for preparing Fe by using metal oxide catalysis as claimed in claim 13O4The method of (2), characterized by: the atomic percentage of the M element in the metal M oxide powder to the metal element in the mixed solution is M/(M + Fe) = 1-10 at.%.
3. The method for preparing Fe by using metal oxide catalysis as claimed in claim 13O4The method of (2), characterized by: the temperature of the hydrothermal reaction is 120-150 ℃.
4. The method for preparing Fe by using metal oxide catalysis as claimed in claim 13O4The method of (2), characterized by: the hydrothermal reaction time is 4-6 h.
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CN1167504C (en) * 2002-04-24 2004-09-22 北京化工大学 Magnetic superfine solid acid catalyst in double-shell structure and its prepn process
CN101445277B (en) * 2008-11-14 2011-05-25 东北大学 Nano-crystalline Fe3O4 particles with high absorption capacity and preparation method thereof
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CN103030169B (en) * 2012-12-26 2015-07-15 中北大学 Shape-controlled preparation method of nanometer copper oxide
CN108375574B (en) * 2018-02-01 2020-11-20 上海工程技术大学 Ferroferric oxide supported nickel-loaded carbonized layer nanotube and preparation method and application thereof
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