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CN105710383A - Method for preparing Cu powder by reducing CuO by adopting glycerinum - Google Patents

Method for preparing Cu powder by reducing CuO by adopting glycerinum Download PDF

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Publication number
CN105710383A
CN105710383A CN201610292183.8A CN201610292183A CN105710383A CN 105710383 A CN105710383 A CN 105710383A CN 201610292183 A CN201610292183 A CN 201610292183A CN 105710383 A CN105710383 A CN 105710383A
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China
Prior art keywords
reactor
glycerol
cuo
reaction
powder
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Pending
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CN201610292183.8A
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Chinese (zh)
Inventor
王凤文
杨书运
多佳
傅扬
姚国栋
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Anhui Agricultural University AHAU
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Anhui Agricultural University AHAU
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Priority to CN201610292183.8A priority Critical patent/CN105710383A/en
Publication of CN105710383A publication Critical patent/CN105710383A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/16Making metallic powder or suspensions thereof using chemical processes
    • B22F9/18Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
    • B22F9/20Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from solid metal compounds

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

The invention discloses a method for preparing Cu powder by reducing CuO by adopting glycerinum. The method is characterized in that glycerinum which is a byproduct of biodiesel is used as a reducing agent; and under an alkaline condition of 250 DEG C, copper oxide is reduced to prepare pure copper powder. The method comprises the specific steps of A, adding CuO and alkali into a reactor, then adding a fixed amount of glycerinum solution, sealing the reactor, and keeping the pressure in the reactor at 3.9 MPa; B, putting the reactor into a high-temperature drying oven with the temperature of 200 to 250 DEG C for reaction for 1.5 to 4.0 hours; C, after the reaction is completed, cooling the reactor under a natural state to end the reaction; and D, opening the reactor, and collecting solid-phase products obtained in the reaction. The method is simple and feasible and is high in operability; in the whole preparation process, the environment cannot be polluted; the problem of environment pollution in the process of preparing copper by the conventional method is well solved; and furthermore, glycerinum can be also converted into a chemical engineering product such as organic acid with high additional value, and resource utilization of wastes is realized.

Description

The method that a kind of glycerol reduction CuO prepares Cu powder
Technical field
The present invention relates to technical field of chemistry, a kind of glycerol reduction CuO prepares the side of Cu powder Method.
Background technology
Copper powder is a kind of important chemical materials, because it has the conduction of excellence, the spy such as corrosion-resistant, nonmagnetic Point, is widely used in multiple fields such as metallurgy, chemical industry, medicine, biology, superconduction and environmental protection.System at present The method of standby copper powder mainly has atomization, oxidation-reduction method and electrolysis etc..Wherein, electrolysis produces Copper powder have that clean surface, formability be good, green strength high, at some higher-end businesses or special Industry has the effect that can not be substituted.But, the existing preparation method of copper powder there is also some shortcomings, such as: Electrolysis has the shortcomings such as big, the technological process length of electrolyte intractability after production cost height, impurity enriched; Atomization prepares copper powder, and to there is formability poor, the shortcoming that apparent density is higher;Oxidation-reduction method prepares copper powder work Skill is the harshest to the requirement of the equipment of production and operator, and production cost is high, and copper powder needs before application Carry out extremely complex anti-oxidant treatment.
Summary of the invention
It is an object of the invention to the method that a kind of glycerol reduction CuO prepares Cu powder, the letter of the method production technology Single, with low cost, whole operating process environmentally safe, it is possible to prepare that purity is high, particle diameter is little, point Dissipate the copper powder that property is good.
The present invention solves technical problem and adopts the following technical scheme that
The method that a kind of glycerol reduction CuO prepares Cu powder, its feature is, with biological diesel oil byproduct Glycerol is as reducing agent, and under the conditions of the alkalescence of 200-250 DEG C, reductive copper oxide prepares copper.
Further, the concretely comprising the following steps of described method:
CuO and alkali are added in reactor, is subsequently adding quantitative glycerite, seal reactor;
B, reactor is put in 200 DEG C of-250 DEG C of high temperature ovens reaction 1.5-4.0h, and keep reactor intrinsic pressure Strong is 1.5-3.9MPa;
Reactor is cooled down with stopped reaction after terminating by C, reaction in its natural state;
D, open reactor, collect solid product after reaction.
Further, described glycerol: CuO mol ratio is 2-3mol:5-10mol.
Further, described glycerol: CuO mol ratio is 2mol:5mol.
Further, described alkali is selected from NaOH, KOH, Ca (OH)2In any one.
Further, described step B for putting into reaction 1.5h in 250 DEG C of high temperature ovens by reactor.
Further, the molar concentration of the reactant glycerol that described step A is sealed in reactor is 0.5mol/L, Alkali molar concentration is 0.1mol/L.
Compared with the prior art, the present invention has the beneficial effect that:
1, the inventive method simple possible, workable, in whole preparation process, environment is not resulted in Polluting, well solution transmission method controlling is for the problem of environmental pollution during copper, and glycerol can also The chemical products such as the organic acid changing into high added value, are simultaneously achieved the recycling of garbage.
2, the copper powder purity that prepared by the inventive method is high, particle diameter is little, good dispersion.
Accompanying drawing explanation
Fig. 1 is the inventive method process chart.
Fig. 2 is the solid product XRD figure spectrum that the embodiment of the present invention 5 obtains.
Fig. 3 is the solid product XRD figure spectrum that the embodiment of the present invention 3 obtains
Fig. 4 is that the inventive method prepares copper powder size analysis chart.
Fig. 5 is commercially available copper powder (200 mesh) granularmetric analysis figure.
Detailed description of the invention
By specific embodiment, technical solution of the present invention is further explained explanation below in conjunction with accompanying drawing.
Embodiment
Using biological diesel oil byproduct glycerin as reducing agent, utilize Teflon reactor (manufacturer: Wu Xinan Fang Jinggong company limited), under the alkaline water heat condition of 250 DEG C, reductive copper oxide prepares copper.Tool Body step is as follows:
(1) inject in 100ml volumetric flask with prunus mume (sieb.) sieb.et zucc. Teller ten thousand/balance precise glycerol 9.210g, Add distilled water and be settled to 100ml;Obtain the glycerite of molar concentration 1.0mol/L.
(2) King is joined with prunus mume (sieb.) sieb.et zucc. Teller a certain amount of CuO and NaOH of ten thousand/balance precise In the Teflon inner bag of reactor, then with liquid-transfering gun, the 1.0mol/L glycerite prepared in advance is moved Take and a certain amount of join in Teflon inner bag, inner bag is put in King shell of reactor, spring leaf on pad And build the lid of reactor;With bench vice fixed plastics king's reactor, rapidly reactor is sealed;
(3) the King reactor of good seal is put in baking oven that (reactor is put into front oven temperature and risen to instead Answer temperature) react, and start timing;During reaction, in keeping reactor, there is certain pressure.
(4) after reaction certain time, baking oven is opened, with clamp, King reactor is taken out, at natural shape Cool down with stopped reaction under state.
(5) after King reactor cooled, open reactor, collect the solid product obtained with qualitative filter paper Copper powder.
(6), after copper powder natural air drying collection obtained, load in sample bottle, carry out XRD to analysis room and divide Analysis and laser particle size analysis.
Table 1 prepares the embodiment of copper powder for this employing said method
Glycerol in table 1, the molar concentration of alkali refer to the reaction density of glycerol in reactor, alkali.
As a example by embodiment 3 and 5, as Figure 2-3, can by gained solid phase sample is carried out XRD analysis Knowing, embodiment 5 gained solid product only has copper simple substance, does not has other any metallicses, illustrates that copper powder is pure Spend the highest.And embodiment 3 gained solid product is in addition to copper simple substance, possibly together with CuO, Cu2O, purity is relatively Embodiment 5 is poor.
By gained copper powder and certain copper powder commercial are carried out particle diameter contrast, result see Fig. 4,5, the present embodiment 5 The various target particle size of gained copper powder and surface area index are superior to buy copper powder, illustrate to use glycerol oxygen reduction Change the copper method for copper powder, it is possible to prepare high-quality copper powder.Additionally, the inventive method simple possible, can Strong operability, in whole preparation process, does not results in pollution to environment, well solves transmission method controlling standby Problem of environmental pollution during copper, and glycerol can also change into the chemical industry such as the organic acid of high added value Product, is simultaneously achieved the recycling of garbage.

Claims (7)

1. the method that a glycerol reduction CuO prepares Cu powder, it is characterised in that with biodiesel byproduct Thing glycerol is as reducing agent, and under the conditions of the alkalescence of 200 DEG C-250 DEG C, reductive copper oxide prepares copper.
The method that a kind of glycerol the most according to claim 1 reduction CuO prepares Cu powder, its feature exists In, concretely comprising the following steps of described method:
A, CuO and alkali are added in reactor, be subsequently adding quantitative glycerite, seal reactor;
B, reactor is put in 200 DEG C of-250 DEG C of high temperature ovens reaction 1.5-4.0h;And keep reactor intrinsic pressure Strong is 1.5-3.9MPa.
Reactor is cooled down with stopped reaction after terminating by C, reaction in its natural state;
D, open reactor, collect solid product after reaction.
The method that a kind of glycerol the most according to claim 2 reduction CuO prepares Cu powder, its feature exists In, described glycerol: CuO mol ratio is 2-3mol:5-10mol.
The method that a kind of glycerol the most according to claim 3 reduction CuO prepares Cu powder, its feature exists In, described glycerol: CuO mol ratio is 2mol:5mol.
5. the method preparing Cu powder according to a kind of glycerol reduction CuO described in Claims 2 or 3, it is special Levying and be, described alkali is selected from NaOH, KOH, Ca (OH)2In any one.
6. the method preparing Cu powder according to a kind of glycerol reduction CuO described in Claims 2 or 3, it is special Levying and be, described step B for putting into reaction 1.5h in 250 DEG C of high temperature ovens by reactor.
7. the method preparing Cu powder according to a kind of glycerol reduction CuO described in claim requirement 2 or 3, It is characterized in that, the molar concentration of the reactant glycerol that described step A is sealed in reactor is 0.5mol/L, Alkali molar concentration is 0.1mol/L.
CN201610292183.8A 2016-04-30 2016-04-30 Method for preparing Cu powder by reducing CuO by adopting glycerinum Pending CN105710383A (en)

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Application Number Priority Date Filing Date Title
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110976901A (en) * 2019-12-31 2020-04-10 湘潭大学 Preparation method of nano copper powder

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6447801A (en) * 1987-08-13 1989-02-22 Daido Steel Co Ltd Production of fine metal powder
CN1082468A (en) * 1993-06-05 1994-02-23 范玉东 Superfine cupper powder and technology of preparing thereof
US6436167B1 (en) * 1996-05-13 2002-08-20 The United States Of America As Represented By The Secretary Of The Navy Synthesis of nanostructured composite particles using a polyol process
WO2006076611A3 (en) * 2005-01-14 2007-03-01 Cabot Corp Production of metal nanoparticles
JP4120007B2 (en) * 2003-01-21 2008-07-16 ラサ工業株式会社 Method for producing copper powder
CN101302148A (en) * 2008-06-24 2008-11-12 同济大学 Method for producing aminic acid by glycerin water thermal reduction of CO2
CN103014216A (en) * 2013-01-08 2013-04-03 中南大学 Reduction method of iron compound in iron-containing material
CN105458295A (en) * 2016-02-01 2016-04-06 中国科学院深圳先进技术研究院 Multi-hole micrometer copper ball and preparation method thereof

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6447801A (en) * 1987-08-13 1989-02-22 Daido Steel Co Ltd Production of fine metal powder
CN1082468A (en) * 1993-06-05 1994-02-23 范玉东 Superfine cupper powder and technology of preparing thereof
US6436167B1 (en) * 1996-05-13 2002-08-20 The United States Of America As Represented By The Secretary Of The Navy Synthesis of nanostructured composite particles using a polyol process
JP4120007B2 (en) * 2003-01-21 2008-07-16 ラサ工業株式会社 Method for producing copper powder
WO2006076611A3 (en) * 2005-01-14 2007-03-01 Cabot Corp Production of metal nanoparticles
CN101302148A (en) * 2008-06-24 2008-11-12 同济大学 Method for producing aminic acid by glycerin water thermal reduction of CO2
CN103014216A (en) * 2013-01-08 2013-04-03 中南大学 Reduction method of iron compound in iron-containing material
CN105458295A (en) * 2016-02-01 2016-04-06 中国科学院深圳先进技术研究院 Multi-hole micrometer copper ball and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110976901A (en) * 2019-12-31 2020-04-10 湘潭大学 Preparation method of nano copper powder

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