CN105731514B - Cubic nano CeO2 and application thereof in degrading o-aminophenol - Google Patents

Cubic nano CeO2 and application thereof in degrading o-aminophenol Download PDF

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CN105731514B
CN105731514B CN201610057876.9A CN201610057876A CN105731514B CN 105731514 B CN105731514 B CN 105731514B CN 201610057876 A CN201610057876 A CN 201610057876A CN 105731514 B CN105731514 B CN 105731514B
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aminophenol
ceo
degradation rate
degrading
ceo2
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CN105731514A (en
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李春光
彭伟功
陈淑敏
罗旭
梁丽珍
周浩
崔节虎
张珂
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Zhengzhou University of Aeronautics
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F17/00Compounds of rare earth metals
    • C01F17/20Compounds containing only rare earth metals as the metal element
    • C01F17/206Compounds containing only rare earth metals as the metal element oxide or hydroxide being the only anion
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C01P2004/60Particles characterised by their size
    • C01P2004/62Submicrometer sized, i.e. from 0.1-1 micrometer
    • 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

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Abstract

The invention belongs to the technical field of water treatment, and particularly relates to a cubic nano cerium oxide (CeO2) and application thereof as a mimic oxidase in degrading o-aminophenol. In the CeO2 preparation process, Ce(NO3)3.6H2O is used as a cerium source, urea is used as a precipitant, and CTAB (cetyltrimethylammonium bromide) is used as a surfactant. A precursor is firstly prepared, and the precursor is calcined to obtain the CeO2. Compared with the natural oxidase, the cerium oxide provided by the invention has the advantages of high stability, low denaturation tendency, wide application range and high reutilization ratio, is easy for storage and transportation, also has high-efficiency oxidase catalytic activity, and thus, can well substitute the existing natural oxidase. When the cerium oxide provided by the invention is used in degrading o-aminophenol, the maximum degradation rate can reach 70% or above.

Description

Cubic nanometer CeO2And its application in o-aminophenol degraded
Technical field
The invention belongs to water-treatment technology field, and in particular to a kind of cubic nanometer ceria(CeO2)And its as mould Intend application of the oxidizing ferment in o-aminophenol degraded.
Background technology
Enzyme is efficient biocatalyst, almost participates in biological all of reaction in vivo.Enzyme have high efficiency, selectivity, The characteristics of diversity and mildness.Native enzyme has great reality in medicine, chemical industry, food processing, environmental protection and agricultural Apply on border.But native enzyme has the shortcomings that mutability inactivation, expensive, purification difficult, storage and use cost are high, and this is all limited Their extensive application is made.Therefore, simulate native enzyme to the molecular recognition of substrate and the research of the analogue enztme of efficient catalytic into For the task of top priority.
Find that ferroferric oxide nano granules have the catalysis of peroxidase first from 2007 Nian Yanxiyun research groups Since activity, the exploration of nano material mimetic enzyme catalysis activity causes at once highest attention.Later, people had found successively various Nano material such as golden nanometer particle, Co3O4, carbon quantum dot, FeS, V2O5Deng the work for being also found to have similar peroxidase Property, but these analogue enztmes nearly all will could occur catalytic reaction by oxidant of hydrogen peroxide, which greatly limits these materials Expect potential application prospect.2009, Perez team found CeO2Nano particle does not need the presence of hydrogen peroxide, it is possible to Oxidation substrates, with the oxidasic activity of simulation, but with regard to CeO2Application still lack further research.
Phenol wastewater be it is a kind of quite serious to harm and and the industrial wastewater of generally existing, to phenol wastewater Administering common processing method has Physical, chemical method and bioanalysis etc., but is all difficult to meet the requirement that thoroughly degraded is removed. 2- amino phenols, is commonly called as o-aminophenol, is a kind of using more extensive fine-chemical intermediate, in medicine production, dyestuff system There is relatively broad purposes in the fields such as standby, rubber synthesis, feed, oil;Thus the pollutant effluents containing o-aminophenol It is a kind of more typical phenol wastewater.Due to the height of the production waste strength containing o-aminophenol, colourity depth, difficult degradation, can Biochemical is poor, and with very big toxicity, the method for dealing with cumbersome, general treatment classification waste water is all difficult effectively place Reason amino phenols waste water.And the oxidasic process for appearing as phenol wastewater of new nanometer simulation provides a kind of new solution party Case, but have not yet to see the report for preferably combining both.
The content of the invention
The invention provides a kind of specific cubic nanometer ceria material and preparation method thereof, and carry based on this A kind of new water process side of application of cubic nanometer ceria as simulation oxidizing ferment in o-aminophenol degraded is supplied Method.
The technical solution used in the present invention is described in detail as follows.
A kind of cubic nanometer CeO2, it is prepared from using following steps:
(1)With Ce (NO3)3·6H2O as cerium source, using urea as precipitating reagent, with CTAB(Cetyl trimethyl bromination Ammonium)As surfactant;By Ce (NO3)3·6H2O, CTAB, urea are dissolved in deionized water, ultrasonic wave dissolving, until solution Become colorless and transparent;
Each material is with molar ratio computing, Ce (NO3)3·6H2O ︰ CTAB ︰ urea=2.28 ~ 2.32:0.24~0.30:9.03~ 9.37;Optimum ratio is, 2.3:0.27:9.2;
(2)By step(1)Middle solution is transferred in the stainless steel autoclave that liner is polytetrafluoroethylene (PTFE), 160 DEG C ~ 200 DEG C of 18 ~ 36h of reaction, preferably 180 DEG C 24 h of reaction, naturally cool to room temperature;
(3)By step(2)Reactant liquor centrifugation after middle cooling, preferred 10000r/min is centrifuged 5 minutes, takes out precipitation Alternately washing 3 times of thing, sediment absolute ethyl alcohol and deionized water, oven drying, 60 DEG C ~ 80 DEG C 3 ~ 6h of drying, preferably 70 DEG C Be dried 5h, obtain cerium oxide precursor body;
(4)By step(3)Middle cerium oxide precursor body roasting in Muffle furnace, 400 DEG C ~ 600 DEG C 10 ~ 15h of roasting, preferably The h of roasting 12 at 500 DEG C, obtains light yellow powder cubic nanometer ceria.
Cubic nanometer CeO2Preparation method, specifically include following steps:
(1)With Ce (NO3)3·6H2O as cerium source, using urea as precipitating reagent, with CTAB(Cetyl trimethyl bromination Ammonium)As surfactant;By Ce (NO3)3·6H2O, CTAB, urea are dissolved in deionized water, ultrasonic wave dissolving, until solution Become colorless and transparent;
Each material is with molar ratio computing, Ce (NO3)3·6H2O ︰ CTAB ︰ urea=2.28 ~ 2.32:0.24~0.30:9.03~ 9.37;Optimum ratio is, 2.3:0.27:9.2;
(2)By step(1)Middle solution is transferred in the stainless steel autoclave that liner is polytetrafluoroethylene (PTFE), 160 DEG C ~ 200 DEG C of 18 ~ 36h of reaction, naturally cool to room temperature;
(3)By step(2)Reactant liquor centrifuge after middle cooling, takes out sediment, sediment absolute ethyl alcohol Alternately wash and be centrifuged 3 times with deionized water, 60 DEG C in an oven ~ 80 DEG C 3 ~ 6h of drying obtain cerium oxide precursor body;
(4)By step(3)Middle cerium oxide precursor body 400 DEG C ~ 600 DEG C 10 ~ 15h of roasting in Muffle furnace, obtain light yellow Powder cubic nanometer ceria.
Cubic nanometer CeO2Application in o-aminophenol degraded, cubic nanometer CeO2Play as analogue enztme and make With, using when, concrete proportioning is:
When o-aminophenol concentration is 10 ~ 70 mg/L, 20mL, CeO2Addition be 10 ~ 70mg, pH=2 ~ 10,0 ~ 300 R/min, 1 ~ 6h of constant temperature oscillation;
Proportion optimizing is:
When o-aminophenol concentration is 40 mg/L, 20mL, CeO2Addition not less than 30mg, pH=3,25 DEG C, 225 R/min constant temperature oscillation 3h.
The invention provides a kind of specific cubic nanometer ceria, this ceria can be as analogue enztme so as to urging Change and degrade and adsorb o-aminophenol., compared to Native Oxide enzyme, its stability is high, be difficult for ceria provided by the present invention Generation denaturation, it is applied widely, be easy to store and transport, and recycling degree is high, and equally there is efficient oxidizing ferment to urge Change activity, thus can preferably substitute the application of existing day thermal oxide enzyme.Ceria provided by the present invention compared to Other Mimetic Peroxidases, it is not necessary to which hydrogen peroxide is thus easy to use as oxidant, in o-aminophenol degraded, Highest degradation rate is up to more than 70%.In general, the cubic nanometer ceria in the present invention, its preparation process is simple can be grasped The property made is strong, and has preferably application prospect in o-aminophenol process, thus with preferable application value.
Description of the drawings
Fig. 1 is cube nano Ce O prepared by embodiment 12SEM figure;
Fig. 2 is cube nano Ce O prepared by embodiment 12XRD spectrum figure;
Fig. 3 is cube nano Ce O prepared by embodiment 12FT-IR figure;
Fig. 4 is cube nano Ce O prepared by embodiment 12TMB lab diagrams, wherein a is to be not added with CeO2(It is colourless), b is Plus CeO2(Become blue), c is that acid adding stops(Turn yellow);
Fig. 5 is o-aminophenol concentration-absorbance standard curve;
Fig. 6 is the abosrption spectrogram of o-aminophenol under condition of different pH;
Fig. 7 is illumination for o-aminophenol degradation rate affects;
Fig. 8 is addition H2O2Impact to degradation rate;
Fig. 9 is impact of the oscillation rate to degradation rate;
Figure 10 is impacts of the pH to degradation rate;
Figure 11 is CeO2Impact of the addition to degradation rate;
Figure 12 is impact of the concussion time to degradation rate;
Figure 13 is impact of the o-aminophenol initial concentration to degradation rate.
Specific embodiment
Technical scheme is further described with reference to embodiment as follows.Before introducing specific embodiment, to this The situation of partial material used and experimental provision is briefly discussed below in invention.
Material used is common experimental medicine in laboratory in the present invention, and purity is pure for analysis;
Involved major experimental instrument has:
SEM (SEM), Q250 F, FEI Co. of the U.S.;
X-ray diffractometer(XRD), XD-3, Beijing Puxi General Instrument Co., Ltd;
Fourier transformation infrared spectrometer, Nicolet iS 10, Thermo Fisher Scientific companies of the U.S.;
Multi parameter analysis instrument, DZS-708, Shanghai Precision Scientific Apparatus Co., Ltd;
Ultraviolet-uisible spectrophotometer, T6 new centuries, Beijing Puxi General Instrument Co., Ltd.
Embodiment 1
Before specific embodiment is introduced, first to preparing CeO in the present invention2Know-why be briefly discussed below.
The present invention is with Ce (NO3)3·6H2O as cerium source, using urea as precipitating reagent, using CTAB as surfactant, First CeO is prepared by hydro-thermal method2Presoma, then the calcining preparation of this presoma lived to obtain CeO again2.Concrete reaction mechanism is such as Under:
First, in reaction mixture, urea decomposes generation ammonium ion and cyanic acid ion:
H2N-CO-NH2→NH4 + + OCN-
When in acid condition, cyanic acid ion occurs rapidly following reaction:
OCN- + 2H+ + H2O → CO2 + NH4 +
When under neutral or basic conditions, it will following reaction occurs:
OCN- + OH- + H2O → NH3 + CO3 2-
Due to Ce3+It is charge with alkalescent and height, will there is strong aquation, specifically:
Ce3+Hydrolysis and with hydrone or OH-Complexing:
Ce3+ + yH2O→[Ce(OH)(H2O)n−1]2+ + H3O+
With the rising and the lengthening in reaction time of reaction temperature, the hydrolysis rate of urea is accelerated, CO3 2- With H3O+Start It is a large amount of to generate, finally obtain CeO2Presoma:
[Ce(OH)(H2O)n−1]2+ + CO3 2- = CeOHCO3(CeCO3OH)+(n-1)H2O;
And presoma CeOHCO3CeO can be thermally decomposed to generate under 500 DEG C of high temperature2
4CeCO3OH + O2→4CeO2 + 2H2O + 4CO2
The cubic nanometer ceria prepared by the present invention is specifically described as follows with reference to embodiment.
The cubic nanometer ceria that the present embodiment is provided, is prepared from using following steps:
(1)By Ce (NO3)3·6H2O、CTAB(Cetyl trimethylammonium bromide), urea be dissolved in the deionized water of 10 mL In, ultrasonic wave dissolving, until solution becomes colorless and transparent;
The concrete consumption of each material is:Ce(NO3)3·6H2O ︰ CTAB ︰ urea=2.3mmol:0.27 mmol:9.2mmol;
(2)By step(1)Middle solution is transferred in the stainless steel autoclave of 20 mL inner liner polytetrafluoroethylenes, sealing Afterwards, it is placed in baking oven, 180 DEG C of 24 h of reaction naturally cool to room temperature;
(3)By step(2)Reactant liquor after the middle cooling centrifuge 5 minutes of 10000r/min, takes out sediment, Alternately washing 3 times of sediment absolute ethyl alcohol and deionized water, 5h are dried in 70 DEG C of baking oven and obtain cerium oxide precursor body;
(4)By step(3)The h of roasting 12 in Muffle furnace of the middle cerium oxide precursor body at 500 DEG C, obtains buff powder Shape cubic nanometer ceria.
For prepared CeO2, inventor further carried out SEM morphology analysis, XRD scanning, fourier-transform infrared The Morphometric analysis such as analysis, correlated process is briefly discussed below.
SEM morphology analysis
When SEM is scanned, it is specifically configured to:During high vacuum pattern, 3.0nm when 1.0nm, 1kv during 30kv;Low-vacuum mode When, 3.0nm when 1.4nm, 3kv during 30kv;During environment vacuum pattern, 2.5nm during 30kv.Multiplication factor is under the pattern of high-altitude 14x-1000000x, multiplication factor error is less than 3%.
As a result it is as shown in Figure 1.
CeO2Crystal morphology change mechanism be:With the rising of reaction temperature, crystal satiety in one side reaction system Reduce with degree;On the other hand, crystal face is more smooth-out, because the growth tendency of nano particle is usually to be intended to three from one-dimensional Dimension development, that is to say, that the particle diameter of product slowly diminishes, when reacted between reach one timing, the size of sample particle diameter is with reaction The rising of temperature and reduce.From figure 1 it appears that the CeO prepared by the present embodiment2Particle diameter between 200 ~ 300nm, category In nanometer materials.
XRD analysis
X-ray diffraction analysis is to determine crystal structure, the analysis of thing phase of material, by the diffraction maximum position to sample Compare the crystalline phase that can obtain sample after being normalized with intensity with standard powder diffraction PDF cards, so as to realize determining for sample Property facies analysis.CeO prepared by the present embodiment2The concrete test condition of sample is:Using curved product graphite monochromator and Cu under room temperature K alpha rays (λ=0.154056nm), Ni optical filters, operating voltage be 36 kV, operating current be 20 mA, 2 ° of sweep speed/ Min, step-length is 0.02, and scanning angle of diffraction 2 θ is 10-90 °.
As a result it is as shown in Figure 2.In fig. 2, the height and width at peak represents the size of crystal grain and the height of degree of crystallinity, peak More narrow higher, it is bigger to represent crystal grain, crystallizes more perfect;Otherwise peak is more wide shorter, it may be possible to which crystal grain is smaller, poor causing is crystallized 's.From figure 2 it can be seen that 30 degree, 35 degree, 45 degree, the peak at 58 degree it is all higher, it is only shorter individually, illustrate system It is higher for the degree of crystallinity for going out.
FT-IR(Fourier-transform infrared light splitting)Analysis
Infrared spectrum collection is carried out to sample using pellet technique.Test condition is:Wave-number range is 4000-400 cm-1, scanning times are 32 times, and resolution ratio is 4.Sample preparation methods are:First cerium oxide powder and KBr are pressed into one Certainty ratio is ground, and then carries out compressing tablet, you can tested.
As a result it is as shown in Figure 3.In figure 3,3300-3500 cm-1Strong absworption peak be due to sample surfaces physical absorption What the stretching vibration of the O-H in water and the crystallization water caused;1600 cm-1- the H that neighbouring absworption peak can belong to the crystallization water is curved Qu Zhendong;1300 cm-1、1093 cm-1And 400 cm-1Three neighbouring absworption peaks correspond to CeO2
CeO2 analogue enztme activities are identified(TMB colour developing checkings)
CeO is verified using TMB2Whether there is analogue enztme activity.Detailed process is:
Substrate colour developing A liquid is prepared first:The g of sodium acetate 13.6, the g of citric acid 1.6, distilled water adds to 500 mL;
Prepare chromogenic substrate B liquid:The g of disodium ethylene diamine tetraacetate 0.2, the g of citric acid 0.95, the mL of glycerine 50, then take 0.15 GTMB is dissolved in 3mL ethanol solutions, and distilled water adds to 500mL;
A liquid, B liquid note keeping in dark place;
During checking, A liquid, each 0.5mL of B liquid are taken, add 5mg CeO2, after being well mixed, colour developing situation is observed after 10min.
As a result it is as shown in Figure 4.Figure 4, it is seen that CeO2Can act on TMB, there is blue reaction, illustrate CeO2Tool There is the oxidasic activity of simulation.
Embodiment 2
Due in the present invention in solution o-aminophenol concentration mensuration Main Basiss concentration and absorbance relation determine, Thus the present invention is as follows firstly the need of o-aminophenol concentration calibration curve corresponding with absorbance, detailed process is drawn:
0 mg/L, 10 mg/L, 20 mg/L, 30 mg/L, 40 mg/L, 50 mg/L, 60 mg/L, 70mg/L are prepared respectively O-aminophenol solution, using distilled water as blank, regulation Detection wavelength is 280nm, uses spectrophotometry Meter difference mensuration absorbance, and draw calibration curve.
As a result it is as shown in Figure 5.In Figure 5, ordinate Y represents absorbance(Abs), abscissa X represents in solution adjacent amino Mass concentration c of phenol(mg/L), in addition as seen from the figure, the equation of linear regression of o-aminophenol is Y=0.0346X- 0.0144, linearly dependent coefficient R2=0.9991。
Due under condition of different pH, the absorbing wavelength of o-aminophenol is different, thus for adjacent amino in Accurate Determining solution The absorbance of phenol, inventor has done o-aminophenol absorbing wavelength measure work under condition of different pH, specially:
Using the o-aminophenol solution of 40 mg/L, with the quartz colorimetric utensil of 1cm, blank reference is done with distilled water, in purple On outer spectrophotometer from the nm of wavelength 190 to 330 nm, every 10 nm determine an absorbance, with wavelength as abscissa, inhale Luminosity is ordinate, draws o-aminophenol absorption spectrum curve, the absorbing wavelength corresponding to absworption peak is found out, if multiple Absorbing wavelength, which then compares again is affected smaller by pH, so as to select optimal absorption wavelength.
As a result it is as shown in Figure 6.From fig. 6 it can be seen that the abosrption spectrogram change of PH=2, PH=3, PH=4.5 tri- becomes Gesture is similar.Wavelength corresponding to maximum absorption band is respectively:230 nm and 275 nm, absworption peak when wavelength is 230 nm be by What the amino on o-aminophenol was caused, wavelength is affected less when being 275 nm by pH, therefore can be used as maximum absorption wavelength.
The clearance of o-aminophenol()It is calculated as follows:
A in formula0For initial absorbance, A is absorbance after degraded.
Using CeO2During catalytic degradation o-aminophenol, due to pH value of solution, CeO may be subject to2Consumption, illumination, adjacent aminobenzene The Multiple factors such as phenol concentration affect, so that inquire into optimum response being equipped with, correlation test process is briefly discussed below.
Impact of the light to o-aminophenol of degrading
Detailed process is:Simulation neighbour's ammonia that 20 mL concentration are 40 mg/L is separately added in the conical flask of four 50 mL Base phenolic waste water, wherein No. 1 conical flask is not added with CeO2;No. 2 conical flasks add 30mg CeO2;No. 3 conical flasks are encased with masking foil, no Plus CeO2;No. 4 conical flasks are encased with masking foil, plus 30 mgCeO2, then pH=2 be put into 25 DEG C, 300 r/ in isothermal vibration device Min vibrates 3 h.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in Figure 7.From figure 7 it can be seen that having light and the unglazed impact to degradation rate less, CeO is illustrated2Degraded O-aminophenol is not photocatalysis.
The impact that H2O2 degrades to o-aminophenol
Detailed process is:The H of 0,1,2,3,4,10 mL mass fractions 15% is separately added in five conical flasks2O2, then The CeO of o-aminophenol simulated wastewater that 20 mL concentration are 40 mg/L and 30 mg is added in each conical flask2, pH=2 puts Enter 25 DEG C in isothermal vibration device, the h of 300 r/min oscillating reactions 3.After reaction terminates, sand core funnel is filtered, mensuration absorbance meter Calculate degradation rate.
As a result it is as shown in Figure 8.From figure 8, it is seen that with addition H2O2The increase of amount, degradation rate dramatic decrease, explanation CeO2In there is no a peroxide root, degradation is not peroxide catalysis.
Impact of the concussion speed to o-aminophenol of degrading
Detailed process is:The o-aminophenol simulation that 20 mL concentration are 40 mg/L is separately added in five conical flasks useless Water and 30 mg CeO2, pH=2, in being individually placed to the constant temperature oscillator that speed is 0,75,150,225,300 r/min, 25 DEG C are shaken Swing 3 h of reaction.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in Figure 9.It can be seen in figure 9 that as the increase of speed, degradation rate are gradually increased, finally tending to Balance.Its reason is that when rotating speed increases, dissolved oxygen increases, due to nano Ce O2There is the storage oxygen function of uniqueness, work as rotating speed Increase, nano Ce O2Storage oxygen is more and more, Ce3+Become Ce4+, increase degradation rate.When speed be 225 r/min when degradation rate Reach most preferably, now degradation rate is 58%.
Impacts of the pH to o-aminophenol of degrading
Detailed process is:The o-aminophenol simulation that 20 mL concentration are 40 mg/L is separately added in 9 conical flasks useless Water, it is 2,2.5,3,3.5,4,5,6,8,10 that pH is adjusted respectively, is subsequently adding 30 mgCeO2, be put into 25 DEG C in isothermal vibration device, 225 r/min vibrate 3 h.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in Figure 10.It can be seen from fig. 10 that pH is at 2-3, as the increase degradation rate of PH is raised, when When pH is more than 3, with the increase of pH, degradation rate is more and more lower.Therefore, as pH=3, preferably, now degradation rate is degradation effect 64.9%。
Impact of the dosage of CeO2 to o-aminophenol of degrading
Detailed process is:The o-aminophenol simulation that 20 mL concentration are 40 mg/L is separately added in 7 conical flasks useless Water, is then respectively adding 10mg, 20 mg, 30 mg, 40 mg, 50 mg, 60 mg, the CeO of 70 mg2, regulation pH=3,25 DEG C, The h of 225 r/min constant temperature oscillations 3.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in figure 11.It can be seen from fig. 11 that with dosage be continuously increased when, degraded take the lead in increase then Slowly tend towards stability, when dosage is more than 30 mg, degradation rate is almost unchanged, remains 58%.Therefore, optimum dosage is 30 mg。
Impact of the concussion time to o-aminophenol of degrading
Detailed process is:The o-aminophenol simulated wastewater that 20 mL concentration are 40 mg/L is added in 6 conical flasks, so The CeO of 30 mg is added afterwards2, adjust pH=3,25 DEG C, 225 r/min constant temperature oscillations, duration of oscillation be respectively set to 1h, 2h, 3h, 4h、5h、6 h.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in figure 12.In figure 12 it can be seen that after the concussion time 4 h is more than, with the increasing of concussion time Plus, degradation rate is slowly reduced on the contrary, it may be said that bright CeO2Not only there is oxidation catalytic degradation o-aminophenol, there is also absorption and make With when overlong time is shaken, the rate of adsorption is less than desorption rate, reduces degradation rate.Therefore, the optimal concussion time is 3 h, Now degradation rate is 62.7%.
Impact of the initial concentration to o-aminophenol of degrading
Detailed process is:20 mL concentration are separately added in 7 conical flasks for 10,20,30,40,50,60,70 mg/L O-aminophenol simulated wastewater and 30 mg CeO2, adjust pH=3,25 DEG C, 225 r/min constant temperature oscillation 3h.Reaction terminates Afterwards, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.
As a result it is as shown in figure 13.It can be observed from fig. 13 that when concentration be 40 mg/L when, degradation rate be it is best, now For 68.4%.
O-aminophenol degradation rate under the conditions of optimal proportion
On the basis of above-mentioned optimal conditions, inventor has further carried out experimental verification, concrete to arrange as follows:
O-aminophenol simulated wastewater and 30 mg CeO that 20 mL concentration are 40 mg/L are added in conical flask2, adjust PH=3,25 DEG C, 225 r/min constant temperature oscillation 3h.After reaction terminates, sand core funnel is filtered, and mensuration absorbance calculates degradation rate.Knot Fruit shows that now degradation rate is up to 71%.

Claims (2)

1. cubic nanometer CeO2Application in o-aminophenol degraded, it is characterised in that cubic nanometer CeO2Send out as analogue enztme The effect of waving, using when, concrete proportioning is:
When o-aminophenol concentration is 10 ~ 70 mg/L, 20mL, CeO2Addition be 10 ~ 70mg, pH=2 ~ 10,0 ~ 300 r/ Min, 1 ~ 6h of constant temperature oscillation.
2. cubic nanometer CeO as claimed in claim 12Application in o-aminophenol degraded, it is characterised in that when applying, tool Body proportioning is:
When o-aminophenol concentration is 40 mg/L, 20mL, CeO2Addition is not less than 30mg, pH=3,25 DEG C, 225 r/min Constant temperature oscillation 3h.
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