CN106984261A - A kind of CoFe2O4/ N/C hollow nano-spheres and its preparation and application - Google Patents

A kind of CoFe2O4/ N/C hollow nano-spheres and its preparation and application Download PDF

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CN106984261A
CN106984261A CN201710344173.9A CN201710344173A CN106984261A CN 106984261 A CN106984261 A CN 106984261A CN 201710344173 A CN201710344173 A CN 201710344173A CN 106984261 A CN106984261 A CN 106984261A
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cofe
nanosphere
spheres
sio
hollow nano
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曾滔
俞明东
张海燕
何志桥
宋爽
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Zhejiang University of Technology ZJUT
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Zhejiang University of Technology ZJUT
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/24Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0259Compounds of N, P, As, Sb, Bi
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
    • B01J20/28009Magnetic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28016Particle form
    • B01J20/28021Hollow particles, e.g. hollow spheres, microspheres or cenospheres
    • B01J35/33
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/308Dyes; Colorants; Fluorescent agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/34Organic compounds containing oxygen
    • C02F2101/345Phenols
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/36Organic compounds containing halogen

Abstract

The invention discloses a kind of CoFe2O4/ N/C hollow nano-spheres and its preparation and application, the nanosphere is with SiO2Nanosphere is template, dopamine is generated polymeric shell layer in template with cobalt, iron metal ion complexing under conditions of pH8 9, is formed after carbonization annealing and be loaded with CoFe2O4The nitrogen-doped carbon material of metal nanoparticle, finally removes SiO with highly basic2Template is prepared into CoFe2O4/ N/C hollow nano-spheres.The present invention is with SiO2Nanoparticle, with larger specific surface area and porosity, improves the CoFe that shell is loaded to sacrifice the N/C matrix hollow-core constructions made by template2O4The distribution of nano metal particles, enhances the absorption to Organic Pollutants in Wastewater and catalytic activity, has widened using pH scopes, and is recycled because its magnetic is recyclable, economizes on resources.

Description

A kind of CoFe2O4/ N/C hollow nano-spheres and its preparation and application
(1) technical field
The present invention relates to wastewater treatment and environmental catalysis technical field, and in particular to a kind of CoFe2O4/ N/C hollow nano-spheres The preparation method and application of the heterogeneous class fenton catalyst of type.
(2) background technology
High-level oxidation technology can overcome traditional handicraft to be difficult to effectively handle difficult degradation as a kind of new water technology The problem of organic matter, thus be widely studied.In recent years, based on potentiometric titrations (SO4 ●-) high-level oxidation technology turn into new Study hotspot, compared to OH, SO4 ●-With longer half-life period, which enhance the contact between free radical and pollutant, have Beneficial to its degraded to pollutant.Meanwhile, SO4 ●-Have and OHClose high redox potential (2.5-3.1V), or even Also there is very strong activity, therefore energy efficient oxidation degradable organic pollutant, with good application under neutral and alkalescence condition Prospect.
The activation of permonosulphuric acid hydrogen salt (PMS) is to produce SO4 ●-Major way, research shows, transition metal or transition gold Belong to oxide nano particles heterogeneous catalysis decomposed P MS and produce SO4 ●-With very high efficiency, but individually nano particle due to Its higher surface energy, inactivation of easily reuniting in aqueous, and metal ion easily leach and cause secondary pollution, therefore usually Suitable carrier material is needed to load nano particle to improve its stability.In numerous materials, common carrier material is such as Silica, activated carbon, graphene, titanium dioxide etc. are because it is to based on the chemical lazy of potentiometric titrations high-level oxidation technology Property and be only capable of providing limited performance improvement, the requirement of actual use can not be met well, therefore, should be designed activity Component is with being provided simultaneously with the advanced composite material (ACM) that the carrier of PMS mobilizing functions is combined, further to adjust and improve reactivity Energy.
(3) content of the invention
Mesh of the present invention solves the bad mechanical strength of existing heterogeneous class fenton catalyst, pH and requires strict, metal ion Leaching content is big, catalytic efficiency is not high and catalyst is difficult to the technical problem of recycling, so as to provide a kind of CoFe2O4/N/ C hollow Nano ball-type catalyst, and can be coupled with peroxy-monosulfate to be formed heterogeneous Fenton-like catalysis oxidation remove it is organic Pollutant.
The technical solution adopted by the present invention is:
The present invention provides a kind of CoFe2O4/ N/C hollow nano-spheres, the nanosphere is with SiO2Nanosphere (particle diameter 100- It is 200nm) template, dopamine is generated polymer shell in template with cobalt, iron metal ion complexing under conditions of pH8-9 Layer, forms after carbonization annealing and is loaded with CoFe2O4The nitrogen-doped carbon material of metal nanoparticle, finally removes SiO with highly basic2Mould Plate is prepared into CoFe2O4/ N/C hollow nano-spheres.
Further, the polymeric shell layer is prepared as follows:By SiO2Nanosphere is added in deionized water a, is surpassed Sound adds dopamine, Co (NO after mixing3)2·6H2O and FeCl2·4H2O, adjusts pH to 8.0~9.0, and fierceness is stirred at room temperature Mix, centrifuge, precipitation is dried in vacuo after being washed with deionized water b, obtain the nanosphere that polymeric shell layer is generated in template;It is described SiO2Nanosphere and dopamine, Co (NO3)2·6H2O and FeCl2·4H2O mass ratio is 1:0.87~1.1:0.06~0.18: 0.12~0.2;The deionized water a volumetric usages are with SiO2Nanometer ball weight is calculated as 1~1.3ml/g;The deionized water a and Deionized water b is deionized water, is named for the ease of statement different step consumption difference, letter itself is without implication.
Further, the carbonization annealing conditions is are warming up to 700~800 DEG C with 3 DEG C/min heating rate, and keep 1.5~2.5h, obtains nitrogen-doped carbon material.
Further, the template minimizing technology is:By the nitrogen-doped carbon material and 1.5~2mol/L sodium hydroxides after carbonization The aqueous solution or the mixing of mass concentration 25-28% ammoniacal liquor, SiO is removed in 70~90 DEG C of reactions2Nanometer ball template, centrifuges, washs, very Sky is dried, and the CoFe is made2O4/ N/C hollow nano-spheres.
The present invention also provides a kind of CoFe2O4The preparation method of/N/C hollow nano-spheres, methods described is:(1) will SiO2Nanosphere is added in deionized water a, and ultrasound adds dopamine, Co (NO after mixing3)2·6H2O and FeCl2·4H2O, is adjusted PH to 8.0~9.0 is saved, at room temperature high degree of agitation (rotating speed 1300rpm, 16-20h), centrifugation, precipitation is washed with deionized water b After be dried in vacuo, obtain Surface Creation polymeric shell layer nanosphere;The SiO2Nanosphere and dopamine, Co (NO3)2· 6H2O and FeCl2·4H2O mass ratio is 1:0.87~1.1:0.06~0.18:0.12~0.2;The deionized water a volumes Consumption is with SiO2Nanometer ball weight is calculated as 1~1.3ml/g;
(2) by the nanosphere of step (1) Surface Creation polymeric shell layer in argon gas protects atmosphere, with 3 DEG C/min liter Warm speed is warming up to 700~800 DEG C, and keeps 1.5~2.5h carbonization annealing, the material after being carbonized;
(3) material and 1.5~2mol/L sodium hydrate aqueous solutions or mass concentration 25-28% after step (2) is carbonized Ammoniacal liquor is mixed, and SiO is removed in 70~90 DEG C of reactions2Nanometer ball template, centrifugation, washing, vacuum drying, is made the CoFe2O4/ N/C hollow nano-spheres.
Further, step (3) washing is to use volume ratio 1:1 ethanol and the mixed solution of deionized water are washed 3~5 times.
The present invention provides a kind of CoFe2O4Application of/N/C the hollow nano-spheres in degradable organic pollutant.
Further, the organic pollution be containing 1~100mg/L methylene blues, 1~100mg/L Norfloxacins or 1~ The waste water of 100mg/L phenol.
Further, the application is:By CoFe2O4/ N/C hollow nano-spheres are added containing organic pollution as catalyst In waste water, permonosulphuric acid hydrogen salt is added, 25 DEG C, oscillating reactions under 250rpm realize the degraded of organic pollution, reaction terminates Afterwards, by reaction solution Magnetic Isolation, collection catalyst is recycled;The content of the Organic Pollutants in Wastewater is 1-100mg/L, The CoFe2O4/ N/C hollow nano-spheres consumption is calculated as 0.08~0.15g/L, the CoFe with wastewater volume2O4/ N/C is hollow to be received Rice ball is 1 with permonosulphuric acid hydrogen salt weight ratio:6~8.
Further, pH value is adjusted to 2.0~10.0 after the addition permonosulphuric acid hydrogen salt.
SiO of the present invention2Nanosphere is prepared as follows:Tetraethyl orthosilicate, ethanol, deionized water and quality is dense The mixing of 25-28% ammoniacal liquor is spent, at room temperature high degree of agitation, centrifugation takes precipitation to be washed and be dried in vacuo with ethanol, obtains SiO2Receive Rice ball;The tetraethyl orthosilicate is 1 with ethanol, deionized water and ammoniacal liquor volume ratio:38.5~42.3:1.2~2.7:1.2~ 2.7。
The CoFe of the present invention2O4The heterogeneous class fenton catalyst of/N/C hollow Nano ball-types is a kind of magnetic nanometer of tool Level catalyst, the catalyst as sewage disposal.Such as processing contains phenol, antibiotic, dye class waste water.
The present invention is with SiO2Nanoparticle is sacrifices the N/C matrix hollow-core constructions made by template, with larger ratio table Area and porosity, improve the CoFe that shell is loaded2O4The distribution of nano metal particles, is enhanced to organic dirt in waste water Absorption and the catalytic activity of thing are contaminated, has been widened using pH scopes, and is recycled because its magnetic is recyclable, is economized on resources.
Compared with existing class Fenton type catalyst, main advantages of the present invention are as follows:
(1) CoFe of synthesis2O4/ N/C hollow nano-spheres are hollow mesoporous type spheric granules, and particle diameter reaches nanoscale, is 200~250nm, specific surface area is big, and suction-operated is strong, is conducive to active component fully to be contacted with oxidant, greatly improves catalysis Efficiency.
(2) the iron cobalt dual-metal form in the present invention is the ferrite compounds CoFe of spinel-type2O4, structural property is steady Fixed, metal ion is difficult dissolution, it is to avoid causes have certain synergy between secondary pollution, and iron cobalt dual-metal, is conducive to Reaction is promoted to carry out.
(3) the heterogeneous class fenton catalyst of synthesis still remains higher catalytic activity in the range of pH 2~10, has There are wider pH applications.
(4) catalyst of the invention has stronger magnetic, collects and reclaims easily in the presence of external magnet, is conducive to two It is secondary to utilize, economize on resources.
(4) illustrate
Fig. 1 is CoFe made from embodiment 12O4The XRD of/N/C catalyst.
Fig. 2 is CoFe made from embodiment 12O4The SEM figures of/N/C catalyst, a is CoFe2O4The overall shape of/N/C materials Looks figure, b is proof CoFe2O4/ N/C has the scanning electron microscope (SEM) photograph of hollow-core construction.
Fig. 3 is CoFe made from embodiment 12O4The photo that/N/C catalyst is separated under external magnet effect with reaction solution, A is the solution cloudy state after catalytic reaction terminates, and b is the phenomenon that catalyst is separated with reaction solution under external magnet effect.
Fig. 4 is CoFe made from embodiment 12O4The dynamic curve diagram of/N/C catalyst degradation methylene blues.
(5) embodiment
With reference to specific embodiment, the present invention is described further, but protection scope of the present invention is not limited in This:
Embodiment 1:CoFe2O4/ N/C hollow nano-spheres
(1)SiO2The preparation of nanoparticle:By 2.6mL tetraethyl orthosilicates, 108mL ethanol, 5mL deionized waters, 5mL ammoniacal liquor (mass concentration 25%) is added in conical flask, at room temperature high degree of agitation 12h, is centrifuged, is washed with ethanol 3~5 times, 80 DEG C true Sky is dried, and obtains SiO2Nanoparticle 400mg, particle diameter 150nm.
(2) by 150mg SiO2Nanoparticle is added in 150mL deionized waters, and 150mg dopamines are added after ultrasound, 17.5mg Co(NO3)2·6H2O and 23.88mg FeCl2·4H2O, is 8.5 with Tris-HCl buffer solutions regulation pH, starts anti- Should, mechanical agitation 18h, rotating speed 1300rpm, are collected by centrifugation black precipitate at room temperature, are washed with deionized after 2~3 times 80 DEG C of vacuum drying, obtain black particle thing 234mg.
(3) the black particle thing of gained in step (2) is put into be carbonized in the tube furnace of argon gas protection atmosphere and annealed, heating Program keeps 2h to be warming up to 750 DEG C with 3 DEG C/min heating rate, the material 153mg after being carbonized.
(4) the material 153mg after step (3) is carbonized is put into hydrothermal reaction kettle, adds 45ml, 2mol/L sodium hydroxide The aqueous solution (or mass concentration 25-28% ammoniacal liquor), reacts 5h to remove SiO at 80 DEG C2Ethanol is used in nanometer ball template, centrifugation With the mixed solution (1 of deionized water:1, v/v) wash 3~5 times, 80 DEG C of vacuum drying produce final product CoFe2O4/ N/C is empty Heart nanosphere 41mg.XRD spectrum as shown in Figure 1, SEM photograph as shown in Figure 2, external magnet effect under, CoFe2O4/ N/C is empty The photo that heart nanometer ball shape catalyst is separated with pollutant solution is as shown in Figure 3.
From figure 1 it appears that the CoFe of synthesis2O4/ N/C X-ray diffraction characteristic peak and CoFe2O4Standard card (JCPDS 22-1086) coincide substantially, the CoFe of this explanation synthesis2O4For cubic system spinel structure, and its main diffraction peak All occur and relatively more sharp, show the CoFe of synthesis2O4Crystallinity is fine.
A can be seen that sample particle is spherical in shape from Fig. 2, and size is homogeneous, and its size is about 200nm, and b can from Fig. 2 Will become apparent from the hollow-core construction of the catalyst.
From figure 3, it can be seen that muddy reaction solution did not had a few minutes just to become in the presence of external magnet originally Clarification, catalyst, in side, shows the CoFe by magnetic2O4/ N/C hollow Nano ball-type catalyst has good magnetic, favorably Recycled in secondary recovery.
Embodiment 2:
The CoFe prepared with embodiment 12O4/ N/C hollow nano-spheres contain 20mg/L as the degraded of heterogeneous class fenton catalyst The waste water of cationic dyes methylene blue.The degradation experiment is carried out in 250ml conical flasks, in 100ml waste water, catalyst Dosage final concentration is calculated as 0.1g/L with wastewater volume, and permonosulphuric acid hydrogen salt (PMS) throwing amount is calculated as 0.8g/L with wastewater volume, 25 DEG C, oscillating reactions under 250rpm, make catalyst be well mixed with solution, reaction are taken out from reaction system every certain time Liquid, determines methylene blue concentration with the change in reaction time, CoFe2O4The heterogeneous class fenton catalyst of/N/C hollow Nano ball-types The result of degradation of methylene blue is as shown in Figure 4.Under similarity condition, using simulated wastewater+catalyst and simulated wastewater+PMS as control.
Figure 4, it is seen that only in the presence of PMS (no catalyst), there was only 10% methylene blue quilt in 20min Remove, illustrate that the effect of PMS independent roles is extremely limited.When only under catalyst action, only 20% is sub- in reaction 20min Methyl blue is removed, and this is mainly due to the suction-operated of the catalyst.And under the conditions of catalyst and PMS are simultaneous, Methylene blue can be completely removed in 20min, and degradation effect has obtained significant raising, be shown in other conditions identical In the case of, CoFe2O4The addition notable catalytic activation of/N/C hollow Nano ball-type catalyst PMS, a large amount of sulfate radicals of generation from Accelerated to promote the degraded of methylene blue by base.
Embodiment 3
Catalytic activity test, its reaction condition ginseng are carried out using the material synthesized by step (3) in embodiment 1 as catalyst Number and step are same as Example 2.As a result show, the methylene blue for there was only 52% in 20min is removed, and shows CoFe2O4/ The hollow configuration of N/C hollow Nano ball-type catalyst is played an important role, and substantially increases the catalytic degradation efficiency of catalyst.
Embodiment 4
Organic Pollutants in Wastewater in embodiment 2 is changed to 20mg/L antibiotic Norfloxacins by dyestuff methylene blue, its His step and parameter are same as Example 2.As a result show, nearly 80% Norfloxacin is removed in 60min, is indicated CoFe2O4The general applicability of/N/C hollow Nano ball-type catalyst.
Embodiment 5
Organic Pollutants in Wastewater in embodiment 2 is changed to 20mg/L phenol by dyestuff methylene blue, other steps and ginseng Number is identical with specific embodiment 2.As a result show, phenol is completely removed in 20min, indicate CoFe2O4/ N/C hollow Nanos The general applicability of ball shape catalyst.
Embodiment 6
The reacted reaction solution of embodiment 2 is separated with magnet, reacted catalyst is collected, 200W in ionized water is added Ultrasonic 30min, continues to be washed with deionized after centrifuging 5min under 12000rpm, is dried in vacuo and collects at 80 DEG C, again Utilize, carry out catalyst repeated experiment, other steps and parameter are same as Example 2.As a result find, carrying out 5 repetitions Property experiment after, CoFe2O4/ N/C hollow Nano ball-type catalyst remains to reach 95% in 20min to the clearance of methylene blue Left and right, indicates the catalyst remarkable stability and repeatability.
Embodiment 7
It is 2.1 by the reaction solution regulation pH in embodiment 2, other steps and parameter are identical with specific embodiment 2.As a result show Show, nearly 96.2% methylene blue is removed in 20min, shows CoFe2O4/ N/C hollow Nano ball-type catalyst is in strong acid Property under still have stronger activity.
Embodiment 8
It is 4.8 by the reaction solution regulation pH in embodiment 2, other steps and parameter are identical with specific embodiment 2.As a result show Show, nearly 97.4% methylene blue is removed in 20min, shows CoFe2O4/ N/C hollow Nano ball-type catalyst is in acidity Under the conditions of still keep stronger activity.
Embodiment 9
It is 6.3 by the reaction solution regulation pH in embodiment 2, other steps and parameter are identical with specific embodiment 2.As a result show Show, nearly 96.1% methylene blue is removed in 20min, shows CoFe2O4/ N/C hollow Nano ball-type catalyst is in partially Property under the conditions of still have stronger activity.
Embodiment 10
It is 9.1 by the reaction solution regulation pH in embodiment 2, other steps and parameter are identical with specific embodiment 2.As a result show Show, nearly 99.04% methylene blue is removed in 20min, shows CoFe2O4/ N/C hollow Nano ball-type catalyst is in alkali Property under have stronger activity.
The CoFe of table 12O4The Contrast on effect of the different pollutants of/N/C catalytic decomposition PMS degradeds

Claims (10)

1. a kind of CoFe2O4/ N/C hollow nano-spheres, it is characterised in that the nanosphere is with SiO2Nanosphere is template, in pH8-9 Under conditions of dopamine and cobalt, iron metal ion complexing is generated polymeric shell layer in template, form load after carbonization annealing There is CoFe2O4The nitrogen-doped carbon material of metal nanoparticle, finally removes SiO with highly basic2Template is prepared into CoFe2O4/ N/C is hollow Nanosphere.
2. CoFe as claimed in claim 12O4/ N/C hollow nano-spheres, it is characterised in that the polymeric shell layer is as follows Prepare:By SiO2Nanosphere is added in deionized water a, and ultrasound adds dopamine, Co (NO after mixing3)2·6H2O and FeCl2· 4H2O, adjusts pH to 8.0~9.0, at room temperature high degree of agitation, centrifugation, and precipitation is dried in vacuo after being washed with deionized water b, is obtained Obtain the nanosphere that polymeric shell layer is generated in template;The SiO2Nanosphere and dopamine, Co (NO3)2·6H2O and FeCl2· 4H2O mass ratio is 1:0.87~1.1:0.06~0.18:0.12~0.2;The deionized water a volumetric usages are with SiO2Nanometer Ball weight is calculated as 1~1.3ml/g.
3. CoFe as claimed in claim 12O4/ N/C hollow nano-spheres, it is characterised in that the carbonization annealing conditions are:With 3 DEG C/ Min heating rate is warming up to 700~800 DEG C, and keeps 1.5~2.5h, obtains nitrogen-doped carbon material.
4. CoFe as claimed in claim 12O4/ N/C hollow nano-spheres, it is characterised in that the template minimizing technology is:Will carbonization Nitrogen-doped carbon material afterwards is mixed with 1.5~2mol/L sodium hydrate aqueous solutions or mass concentration 25-28% ammoniacal liquor, 70~90 DEG C reaction remove SiO2Nanometer ball template, centrifugation, washing, vacuum drying, is made the CoFe2O4/ N/C hollow nano-spheres.
5. CoFe described in a kind of claim 12O4The preparation method of/N/C hollow nano-spheres, it is characterised in that methods described is: (1) by SiO2Nanosphere is added in deionized water a, and ultrasound adds dopamine, Co (NO after mixing3)2·6H2O and FeCl2· 4H2O, adjusts pH to 8.0~9.0, at room temperature high degree of agitation, centrifugation, and precipitation is dried in vacuo after being washed with deionized water b, is obtained Obtain the nanosphere of Surface Creation polymeric shell layer;The SiO2Nanosphere and dopamine, Co (NO3)2·6H2O and FeCl2·4H2O Mass ratio be 1:0.87~1.1:0.06~0.18:0.12~0.2;The deionized water a volumetric usages are with SiO2Nanosphere Weight is calculated as 1~1.3ml/g;
(2) by the nanosphere of step (1) Surface Creation polymeric shell layer in argon gas protects atmosphere, with 3 DEG C/min heating speed Rate is warming up to 700~800 DEG C, and keeps 1.5~2.5h carbonization annealing, the material after being carbonized;
(3) material and 1.5~2mol/L sodium hydrate aqueous solutions or mass concentration 25-28% ammoniacal liquor after step (2) is carbonized Mixing, SiO is removed in 70~90 DEG C of reactions2Nanometer ball template, centrifugation, washing, vacuum drying, is made the CoFe2O4/ N/C is empty Heart nanosphere.
6. CoFe as claimed in claim 52O4The preparation method of/N/C hollow nano-spheres, it is characterised in that step (3) washing is to use Volume ratio 1:1 ethanol and the mixed solution of deionized water are washed 3~5 times.
7. CoFe described in a kind of claim 12O4Application of/N/C the hollow nano-spheres in degradable organic pollutant.
8. application as claimed in claim 7, it is characterised in that the organic pollution is containing 1~100mg/L methylene blues, 1 The waste water of~100mg/L Norfloxacins or 1~100mg/L phenol.
9. application as claimed in claim 8, it is characterised in that the application is:By CoFe2O4/ N/C hollow nano-spheres are as urging Agent is added in the waste water containing organic pollution, adds permonosulphuric acid hydrogen salt, and 25 DEG C, oscillating reactions under 250rpm, realization have The degraded of organic pollutants, after reaction terminates, by reaction solution Magnetic Isolation, collection catalyst is recycled;The CoFe2O4/N/C Hollow nano-sphere consumption is calculated as 0.08~0.15g/L, the CoFe with wastewater volume2O4/ N/C hollow nano-spheres and permonosulphuric acid Hydrogen salt weight ratio is 1:6~8.
10. application as claimed in claim 9, it is characterised in that after the addition permonosulphuric acid hydrogen salt regulation pH value to 2.0~ 10.0。
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