CN102180522A - Controllable preparation method of nano magnetic iron oxide with narrow particle size distribution - Google Patents

Controllable preparation method of nano magnetic iron oxide with narrow particle size distribution Download PDF

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CN102180522A
CN102180522A CN 201110075659 CN201110075659A CN102180522A CN 102180522 A CN102180522 A CN 102180522A CN 201110075659 CN201110075659 CN 201110075659 CN 201110075659 A CN201110075659 A CN 201110075659A CN 102180522 A CN102180522 A CN 102180522A
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iron oxide
size distribution
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magnetic iron
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CN102180522B (en
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于成龙
郝欣
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SHAANXI HONGJU ELECTRONIC TECHNOLOGY Co Ltd
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SHAANXI HONGJU ELECTRONIC TECHNOLOGY Co Ltd
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Abstract

The invention provides a controllable preparation method of nano magnetic iron oxide with narrow particle size distribution. By using the method, the nucleation process of the iron oxide can be controlled and the distribution of the prepared nano powder particle size is extremely narrow. The method comprises the following steps: carrying out ultrasound treatment in a high-concentration NaOH solution so as to form a Fe[CH3(CH2)7CH=CH(CH2)7COO]n micelle, thereby effectively protecting the aggregation and precipitation of Fe<2+>; adding hydrazine hydrate so as to inhibit oxidation of Fe<2+> and form extremely good dispersion under the condition of hydrothermal; and diluting the obtain transparent concentrated base solution so as to slowly form a Fe(OH)x[CH3(CH2)7CH=CH(CH2)7COO]2-x (x is larger than 0 and less than 2) gel micelle, then oxidizing and dehydrating so as to form FeO(OH)y[CH3(CH2)7CH-CH(CH2)7COO]1-y (y is more than 0 and less than 1), and finally sintering at the atmosphere of mixing Ar and H2 for removing surface organics and water, so as to form gamma-Fe2O3.

Description

A kind of controllable method for preparing of narrow size distribution nano magnetic iron oxide
[technical field]
The invention belongs to wet chemistry method and prepare the nano-powder technical field, be specifically related to a kind of preparation method of nano magnetic iron oxide.
[background technology]
Nano magnetic iron oxide (γ-Fe 2O 3) be important magneticsubstance, crossing aspects such as heat cure in the tumour of energy storage, electrochemical sensor, alternating magnetic field all has important use.The PREPARATION OF NANO FERRIC OXIDE method of having reported at present all can obtain nano particle, but still can not obtain satisfactory result aspect particle size and the nucleating growth controllability.As, Li Yuehuas etc. are with Fe 3O 4Be raw material, prepared γ-Fe by air oxidation process 2O 3, but its particle diameter is bigger, and distribution range is very wide, between 30-400nm.Chinese patent is announced CN100436334C number and has been reported that a kind of is the feedstock production magnetic Fe with converter slag 2O 3Method.By slag is ground, pickling is leached and is made FeSO 4Solution then with obtaining precipitation after the alkaline purification, adds crystal seed at last and forms γ-Fe through high temperature crystallization 2O 3Though method can obtain high-purity powder, but still owing to obtain by intermediate processing, nucleation process is uncontrollable, and the particle diameter of acquisition is bigger.In addition, also need to add crystal seed.
Reference:
Li Yuehua, etc. nanometer γ-Fe 2O 3The preparation of particle and magnetic behavior thereof, functional materials, 2007,38 (supplementary issue): 1981-1983.
Liu Chengjun, etc. a kind of preparation method who is used to make the high purity magnetic material nano ferric oxide, Chinese invention patent, CN100436334C, 2007.
[summary of the invention]
The preparation method who the purpose of this invention is to provide a kind of narrow size distribution nano-magnetic ferric oxide has solved nucleation and the uncontrollable problem of growth, and the nanoparticle size of preparation distributes very narrow.
To achieve these goals, the present invention adopts following technical scheme:
A kind of controllable method for preparing of narrow size distribution nano magnetic iron oxide may further comprise the steps:
1) with FeSO 47H 2O and NaOH are dissolved in respectively in the equal-volume distilled water, and it is 0.5~5 * 10 that the dissolving back forms concentration -3The FeSO of mol/L 4Solution and concentration are the NaOH solution of 10~14mol/L;
2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process is up to obtaining transparent solution;
3) in the clear solution that step 2 obtains, add sodium oleate and form mixing solutions, control oleic acid root and FeSO 4Mol ratio be 0.83~1.5;
4) with the mixing solutions of step 3, ultra-sonic dispersion is to oleic acid root and Fe 2+Formed the grey micella;
5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 42.5%~5% of solution and the used distilled water volume of NaOH solution sum; Supersound process forms the grey spherical particle to forming a large amount of grey micellas after the grey micella is reunited then;
6) solution that step 5 is obtained moves in the Teflon water heating kettle, and packing ratio is 20%~60%, is incubated 24~48 hours down at 140~180 ℃; The heating back forms clear solution;
7) clear solution that step 6 is obtained with distilled water diluting after, place the air at room temperature slow oxidation, generate colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x, slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y
8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter the centrifugal settling, vacuum-drying obtains nanometer Fe O (OH) y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder;
9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder calcination is removed the residual organic matter on surface, obtains γ-Fe 2O 3Powder;
0<x<2,0<y<1 wherein.
The frequency of supersound process described in ultra-sonic dispersion described in supersound process, the step 4 and the step 5 is 39.48~44.52kHz described in the step 2.
The time of ultra-sonic dispersion is 5 minutes in the step 4, and the time of supersound process is 30~60 minutes in the step 5.
Temperature rise rate when heating in the step 6 is 10 ℃/min.
Clear solution is 1: 20 with the Dilution ratio that distilled water diluting adopted in the step 7.
The clear solution that in the step 7 step 6 is obtained with distilled water diluting after, the time that places the air at room temperature slow oxidation is 24~48 hours.
Vacuum drying condition is in the step 8: 50 ℃ of temperature, 22~50 hours time.
The incinerating condition is in the step 9: at 95%Ar+5H 2Calcined 20~40 minutes in 480~500 ℃ in the % atmosphere.
Compared with prior art, the present invention has the following advantages: the nucleation process that the inventive method can controlled oxidation iron, the particle diameter of nanometer powder of preparation distributes very narrow, at 16nm between the 21nm.Form Fe[CH by supersound process in high density NaOH solution 3(CH 2) 7CH=CH (CH 2) 7COO] nMicella, and then protect Fe effectively 2+Gathering and precipitation.Add hydrazine hydrate in the process and suppress Fe 2+Oxidation forms fabulous dispersion then under hydrothermal condition.The transparent concentrated alkali solution that obtains slowly forms Fe (OH) through the dilution back x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2) gel strands, oxidation and dehydration form nanometer Fe O (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) is at last at Ar and H 2Mixed atmosphere under sintering remove surface organic matter and surface-moisture forms nanometer γ-Fe 2O 3
[description of drawings]
Fig. 1 is preparation technology's schema;
Fig. 2 is the X-ray diffraction spectrogram of embodiment 4 preparation powders;
Fig. 3 is the transmission electron microscope picture of embodiment 1 preparation powder;
Fig. 4 is the size distribution figure of embodiment 3 preparation powders.
[embodiment]
The present invention is described in detail below in conjunction with the drawings and specific embodiments.
First part: the step that the inventive method is complete is described.
See also shown in Figure 1ly, the present invention mainly may further comprise the steps:
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in respectively in isopyknic distilled water, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 0.5~5 * 10 with NaOH concentration -3Mol/L and 10~14mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the concentrated NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 39.48~44.52kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 0.83~1.5.
(4) with the mixing solutions of step 3, ultra-sonic dispersion is after 5 minutes, oleic acid root and Fe 2+Formed the grey micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 39.48~44.52kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in step 4, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 42.5%~5% of solution and the used distilled water volume of NaOH solution sum; Supersound process is 30~60 minutes then, forms a large amount of grey micellas, forms the grey spherical particle after the grey micella is reunited.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 20%~60%, is incubated 24~48 hours down at 140~180 ℃, and temperature rise rate is 10 ℃/min.
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 24~48 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 22~50 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder is at 95%Ar+5H 2After 20~40 minutes, remove the residual organic matter on surface in 480~500 ℃ of calcinings in the % atmosphere, obtain γ-Fe 2O 3Powder.
Second section:
Can control nucleation and process of growth fully by this method, and then the control reaction process.Reaction process can be write as:
Fe 2++x(OH) -+(2-x)[CH 3(CH 2) 7CH=CH(CH 2) 7COO] -
Figure BDA0000052459950000061
(1)
Fe 2+(OH) x[CH 3(CH 2) 7CH=CH(CH 2) 7COO] 2-x
Fe 2+(OH) x[CH 3(CH 2) 7CH=CH(CH 2) 7COO] 2-x
Figure BDA0000052459950000062
(2)
Fe 3+O(OH) y[CH 3(CH 2) 7CH=CH(CH 2) 7COO] 1-y
Fe 3+O(OH) y[CH 3(CH 2) 7CH=CH(CH 2) 7COO] 1-y
(3)
Figure BDA0000052459950000063
Third part:
Enumerate various embodiment
Embodiment 1
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in 50ml distilled water respectively, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 0.5 * 10 with NaOH concentration -3Mol/L and 10mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 40kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 1.
(4) with the mixing solutions of step 3, ultra-sonic dispersion is after 5 minutes, oleic acid root and Fe 2+Formed micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 40kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 42.5% of solution and the used distilled water volume of NaOH solution sum, i.e. 2.5ml, supersound process is 30 minutes then, forms a large amount of grey micellas, and the grey micella back of reuniting forms the grey spherical particle.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 20%, is incubated 24 hours down at 140 ℃, and temperature rise rate is 10 ℃/min; The heating back forms clear solution;
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 24 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 22 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder is at 95%Ar+5H 2After 20 minutes, remove the residual organic matter on surface in 480 ℃ of calcinings in the % atmosphere, obtaining the particle median size is γ-Fe of 16nm 2O 3Powder.
Embodiment 2
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in 50ml distilled water respectively, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 5 * 10 with NaOH concentration -3Mol/L and 14mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 42kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of aqueous solution sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 1.5.
(4) with the mixing solutions of step 3, ultra-sonic dispersion is after 5 minutes, oleic acid root and Fe 2+Formed micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 42kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 45% of solution and the used distilled water volume of NaOH solution sum, i.e. 5ml, supersound process is 60 minutes then, forms a large amount of grey micellas, and the grey micella back of reuniting forms the grey spherical particle.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 60%, is incubated 48 hours down at 180 ℃, and temperature rise rate is 10 ℃/min; The heating back forms clear solution;
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 48 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 50 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder is at 95%Ar+5H 2After 40 minutes, remove the residual organic matter on surface in 500 ℃ of calcinings in the % atmosphere, obtaining the particle median size is γ-Fe of 19nm 2O 3Powder.
Embodiment 3
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in 50ml distilled water respectively, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 1.5 * 10 with NaOH concentration -3Mol/L and 12mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 42kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 1.07.
(4) with the mixing solutions of step 3, ultra-sonic dispersion is after 5 minutes, oleic acid root and Fe 2+Formed micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 42kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 43% of solution and the used distilled water volume of NaOH solution sum, i.e. 3ml, supersound process is 60 minutes then, forms a large amount of grey micellas, and the grey micella back of reuniting forms the grey spherical particle.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 50%, is incubated 24 hours down at 160 ℃, and temperature rise rate is 10 ℃/min.The heating back forms clear solution;
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 36 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 26 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder is at 95%Ar+5H 2After 30 minutes, remove the residual organic matter on surface in 500 ℃ of calcinings in the % atmosphere, obtaining the particle median size is γ-Fe of 18.5nm 2O 3Powder.
Embodiment 4
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in 50ml distilled water respectively, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 3 * 10 with NaOH concentration -3Mol/L and 13mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 44kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 1.17.
(4) with the mixing solutions of step 3, ultra-sonic dispersion formed the grey micella after 5 minutes, showed oleic acid root and Fe 2+Formed micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 44kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 42.5% of solution and the used distilled water volume of NaOH solution sum, i.e. 2.5ml, supersound process is 30 minutes then, forms a large amount of grey micellas, and the grey micella back of reuniting forms the grey spherical particle.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 60%, is incubated 20 hours down at 180 ℃, and temperature rise rate is 10 ℃/min; The heating back forms clear solution;
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 24 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 30 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder is at 95%Ar+5H 2After 30 minutes, remove the residual organic matter on surface in 510 ℃ of calcinings in the % atmosphere, obtaining the particle median size is γ-Fe of 19.6nm 2O 3Powder.
Embodiment 5
(1) with a certain amount of FeSO 47H 2O and NaOH are dissolved in 50ml distilled water respectively, and the dissolving back forms clear solution, FeSO in the solution 4Be respectively 3.0 * 10 with NaOH concentration -3Mol/L and 11.5mol/L.
(2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process can not form precipitation up to obtaining transparent solution in this step.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 44.52kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(3) a certain amount of sodium oleate is added in the clear solution of step 2 acquisition control oleic acid root and FeSO 4Mol ratio be 0.83.
(4) with the mixing solutions of step 3, ultra-sonic dispersion is after 5 minutes, oleic acid root and Fe 2+Formed micella.Supersound process is carried out (model: 5510J-MT, output rating: 135W, operating frequency: 44.52kHz) in the ultrasonic generator that U.S. Brason Ultrasonics Corporation produces.
(5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 45% of solution and the used distilled water volume of NaOH solution sum, i.e. 5ml, supersound process is 55 minutes then, forms a large amount of grey micellas, and the grey micella back of reuniting forms the grey spherical particle.
(6) solution that step 5 is obtained moves into the Teflon water heating kettle, and packing ratio is 60%, is incubated 10 hours down at 180 ℃, and temperature rise rate is 10 ℃/min; The heating back forms clear solution.
(7) clear solution that step 6 is obtained with distilled water diluting after (ratio of dilution is 1: 20), place the air at room temperature slow oxidation, the time is 35 hours, generates colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x(0<x<2), slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1).
(8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter (0<y<1) centrifugal settling,, obtain nanometer Fe O (OH) 50 ℃ of following vacuum-dryings 24 hours y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder.
(9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y(0<y<1) powder is at 95%Ar+5H 2After 30 minutes, remove the residual organic matter on surface in 505 ℃ of calcinings in the % atmosphere, obtaining particle diameter is γ-Fe of 21nm 2O 3Powder.
The 4th part:
See also shown in Figure 2ly, be the nanometer γ-Fe of embodiment 4 preparations 2O 3X ray diffracting spectrum, X ray test is the result show, the nano-powder perfect crystalline of preparation is the γ-Fe of cubic phase 2O 3See also shown in Figure 3ly, be the nanometer γ-Fe of embodiment 1 preparation 2O 3Transmission electron microscope picture, as can be seen from the figure, the nano particle diameter of the inventive method preparation distributes very narrow, between 16nm to 21nm.See also shown in Figure 4ly, be the nanometer γ-Fe of embodiment 3 preparations 2O 3Size distribution figure, size distribution is very narrow as can be seen, between 16.0nm to 20nm, mainly concentrates between the 17.0nm to 19.5nm.

Claims (8)

1. the controllable method for preparing of a narrow size distribution nano magnetic iron oxide is characterized in that, may further comprise the steps:
1) with FeSO 47H 2O and NaOH are dissolved in respectively in the equal-volume distilled water, and it is 0.5~5 * 10 that the dissolving back forms concentration -3The FeSO of mol/L 4Solution and concentration are the NaOH solution of 10~14mol/L;
2) FeSO that step 1 is disposed 4Solution is dissolved in the NaOH solution of step 1 configuration, and supersound process is up to obtaining transparent solution;
3) in the clear solution that step 2 obtains, add sodium oleate and form mixing solutions, control oleic acid root and FeSO 4Mol ratio be 0.83~1.5;
4) with the mixing solutions of step 3, ultra-sonic dispersion is to oleic acid root and Fe 2+Formed the grey micella;
5) add hydrazine hydrate in the mixing solutions that step 4 forms, the volume that adds hydrazine hydrate is to dispose FeSO in the step 1 42.5%~5% of solution and the used distilled water volume of NaOH solution sum; Supersound process forms the grey spherical particle to forming a large amount of grey micellas after the grey micella is reunited then;
6) solution that step 5 is obtained moves in the Teflon water heating kettle, and packing ratio is 20%~60%, is incubated 24~48 hours down at 140~180 ℃; The heating back forms clear solution;
7) clear solution that step 6 is obtained with distilled water diluting after, place the air at room temperature slow oxidation, generate colloid Fe (OH) x[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 2-x, slow oxidation and dehydration generate FeO (OH) then y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-y
8) FeO (OH) that step 7 is prepared y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yAfter the centrifugal settling, vacuum-drying obtains nanometer Fe O (OH) y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder;
9) with the nanometer Fe O (OH) of step 8 y[CH 3(CH 2) 7CH=CH (CH 2) 7COO] 1-yPowder calcination is removed the residual organic matter on surface, obtains γ-Fe 2O 3Powder;
0<x<2,0<y<1 wherein.
2. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide, it is characterized in that: the frequency of supersound process described in ultra-sonic dispersion described in supersound process, the step 4 and the step 5 is 39.48~44.52kHz described in the step 2.
3. as the controllable method for preparing of a kind of narrow size distribution nano magnetic iron oxide as described in the claim 2, it is characterized in that: the time of ultra-sonic dispersion is 5 minutes in the step 4, and the time of supersound process is 30~60 minutes in the step 5.
4. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide is characterized in that: the temperature rise rate in the step 6 during heating is 10 ℃/min.
5. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide, it is characterized in that: clear solution is 1: 20 with the Dilution ratio that distilled water diluting adopted in the step 7.
6. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide is characterized in that: the clear solution that in the step 7 step 6 is obtained with distilled water diluting after, the time that places the air at room temperature slow oxidation is 24~48 hours.
7. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide is characterized in that, vacuum drying condition is in the step 8: 50 ℃ of temperature, 22~50 hours time.
8. a kind of according to claim 1 controllable method for preparing of narrow size distribution nano magnetic iron oxide is characterized in that, the incinerating condition is in the step 9: at 95%Ar+5H 2Calcined 20~40 minutes in 480~500 ℃ in the % atmosphere.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103084147A (en) * 2011-11-08 2013-05-08 纳科石油化工有限公司 Iron oxide magnetic nano particle, preparation method and application method thereof in desulfurization
CN103204550A (en) * 2013-04-12 2013-07-17 陕西科技大学 Controllable preparation method of micron-order Fe2O3
CN105749864A (en) * 2016-04-13 2016-07-13 西安近代化学研究所 Preparation method of high-specific-area magnetic adsorbent or magnetic catalyst support

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4512906A (en) * 1981-10-16 1985-04-23 Central Glass Company Limited Wet process for preparing ferrites of magnetoplumbite structure in fine particle form
CN101003388A (en) * 2006-12-30 2007-07-25 中国科学技术大学 Method for preparing Nano cube of hematite
CN101269843A (en) * 2008-05-06 2008-09-24 华东理工大学 Method for preparing iron oxide nano-wire

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4512906A (en) * 1981-10-16 1985-04-23 Central Glass Company Limited Wet process for preparing ferrites of magnetoplumbite structure in fine particle form
CN101003388A (en) * 2006-12-30 2007-07-25 中国科学技术大学 Method for preparing Nano cube of hematite
CN101269843A (en) * 2008-05-06 2008-09-24 华东理工大学 Method for preparing iron oxide nano-wire

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103084147A (en) * 2011-11-08 2013-05-08 纳科石油化工有限公司 Iron oxide magnetic nano particle, preparation method and application method thereof in desulfurization
CN103084147B (en) * 2011-11-08 2015-02-25 纳科石油化工有限公司 Iron oxide magnetic nano particle, preparation method and application method thereof in desulfurization
CN103204550A (en) * 2013-04-12 2013-07-17 陕西科技大学 Controllable preparation method of micron-order Fe2O3
CN105749864A (en) * 2016-04-13 2016-07-13 西安近代化学研究所 Preparation method of high-specific-area magnetic adsorbent or magnetic catalyst support
CN105749864B (en) * 2016-04-13 2018-10-12 西安近代化学研究所 A kind of preparation method of high-specific surface area magnetic adsorbent or magnetic catalyst carrier

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