Summary of the invention
In view of the deficiencies of the prior art, the present invention intends to provide a kind of hollow more shells of metal composite oxide
Layer material, preparation method and use are adsorbed by two steps, there is significantly different metal ions in the carbon ball template after making absorption
Concentration gradient, to obtain the hollow more Shell Materials of metal composite oxide that energy order absorbs solar spectrum after baking.
To achieve this purpose, the present invention adopts the following technical scheme:
In a first aspect, the present invention provides a kind of preparation method of the hollow more Shell Materials of metal composite oxide, it is described
Method includes:
(1) it using the carbon ball of hydro-thermal method preparation as template, disperses carbon ball in the first metal salt solution, hydro-thermal enhancing
Solid precursor is obtained after absorption, drying;
(2) it disperses the solid precursor that step (1) obtains in the second metal salt solution, absorption, roasting obtain described
The hollow more Shell Materials of metal composite oxide;
Wherein, the hydrated ionic radius in first metal salt solution is less than the hydration in second metal salt solution
Ionic radius.
In the method, the presoma selection of metal oxide is extremely important, and the present invention is by selecting different hydrated ions
The metal salt solution of radius is as precursor solution, and different metal ions generate apparent concentration in the carbon ball template after making absorption
Gradient.Firstly, in step (1) by dispersion and hydro-thermal enhance adsorption operations so that have smaller hydrated ionic radius and institute it is right
The lesser metal ion of metal oxide band gap answered can deeper into be adsorbed onto inside carbon ball;By dividing in step (2)
Scattered and adsorption operations, make to have larger hydrated ionic radius and the corresponding biggish metal ion of metal oxide band gap are main
It is gathered in carbon ball surface, the narrow band gap metal oxidation that the hypostracum of the metallic oxide hollow sphere obtained after baking in this way contains
Object relative amount is high, and the broad-band gap metal oxide relative amount of outer shell is high.When being applied to photocatalysis field, outside
The weak ultraviolet portion of penetration capacity in the absorbable solar spectrum of the broad-band gap metal oxide of shell layer surface aggregation, and hypostracum
The narrow metal oxide of adsorption can absorb the visible light part that penetration capacity is strong in solar spectrum, to realize to sunlight
The light order of each wave band absorbs in spectrum.
As currently preferred technical solution, it is molten that first metal salt solution is selected from copper nitrate solution, copper chloride
Liquid, copper-bath, tetrachloro close copper acid solution, cupric tetramminosulfate, iron nitrate solution, ferric chloride solution, cobalt nitrate solution, chlorine
Change the combination of one of cobalt liquor and cobalt acetate solution or at least two, preferably copper nitrate solution, copper chloride solution, sulfuric acid
One of copper solution, ferric nitrate, cobalt nitrate or at least two combination;The first metal salt solution that the present invention selects for
The metal salt of smaller hydrated ionic radius, corresponding metal oxide have lesser forbidden bandwidth, the lesser metal of band gap
Oxide is in hypostracum, for absorbing the strong visible light part of penetration capacity in solar spectrum.
" hydro-thermal method " of the present invention, which refers to for carbon containing precursor water solution to be fitted into reaction kettle, carries out hydro-thermal reaction, warp
Cool down, be filtered, washed, dry after obtain the method for carbon ball template, compared with traditional mechanical attrition method, prepared by hydro-thermal method
Carbon ball uniform particle sizes, size is controllable, while a large amount of active function groups are contained on surface, and there is excellent hydrophily and surface to react
Activity, the more conducively absorption of metal ion are the common templates for preparing Core-shell structure material.
" hydro-thermal enhancing absorption " of the present invention, which refers to, is fitted into carbon ball template and metal salt solution in reaction kettle, hydro-thermal
Absorption of the enhancing carbon ball template to metal ion under state obtains after cooling, centrifugation, washing, drying rich in the first metal
The method of the solid precursor of salt ion.
Preferably, the solvent of first metal salt solution is selected from or mixtures thereof water, ethyl alcohol, and preferred solvent is water.
Preferably, it is molten to be selected from titanium tetrachloride solution, titanium tetrabromide solution, titanium tetra iodide for second metal salt solution
Liquid, fluorination titanium solution, solution of tetrabutyl titanate, isopropyl titanate solution, titanyl sulfate solution, zinc nitrate solution, zinc chloride are molten
One of liquid, cerous nitrate solution and solution of cerium chloride by oxidation or at least two combination, preferably titanium tetrachloride solution, four fourth of metatitanic acid
One of ester solution, isopropyl titanate solution, zinc nitrate, cerous nitrate or at least two combination;The present invention select second
Metal salt solution is the metal salt with larger hydrated ionic radius, and corresponding metal oxide has biggish forbidden band wide
Degree, the biggish metal oxide of band gap is in outer shell, for absorbing the weak ultraviolet portion of penetration capacity in solar spectrum.
Preferably, the solvent of second metal salt solution is selected from or mixtures thereof water, ethyl alcohol, and preferred solvent is water.
As currently preferred technical solution, the preparation method packet of the hollow more Shell Materials of metal composite oxide
It includes:
(a) carbon source aqueous solution is fitted into reaction kettle and carries out hydro-thermal reaction, obtain carbon ball mould after being filtered, washed and dried drying
Plate;
(b) it disperses the carbon ball template that step (a) obtains in the first metal salt solution, through hydro-thermal enhancing absorption, drying
After obtain the first solid precursor;
(c) the first solid precursor for obtaining step (b) is scattered in the second metal salt solution, after being adsorbed, being dried
Obtain the second solid precursor;
(d) the second solid precursor for obtaining step (c) roasts, and it is hollow to obtain the metal composite oxide
More Shell Materials.
As currently preferred technical solution, carbon source described in step (a) is glucose, fructose, sucrose, malt
One of sugar, starch or citric acid or at least two combination, preferably sucrose.
Preferably, in the carbon source aqueous solution carbon source concentration be 0.1-6M, such as can be 0.1M, 0.5M, 1M,
1.5M, 2M, 2.5M, 3M, 3.5M, 4M, 4.5M, 5M, 5.5M or 6M, preferably 1-5M, further preferred 2-3M.
Preferably, the hydro-thermal reaction carries out in a kettle.
Preferably, the temperature of the hydro-thermal reaction is 175-220 DEG C, such as can be 175 DEG C, 180 DEG C, 185 DEG C, 190
DEG C, 195 DEG C or 200 DEG C, preferably 190-205 DEG C, further preferably 195-200 DEG C.
Preferably, the time of the hydro-thermal reaction be 100-180min, such as can be 100min, 110min, 120min,
130min, 140min, 150min, 160min, 170min or 180min, preferably 120-140min, further preferably 125-
135min。
Preferably, it is washed using one of deionized water, methanol or ethyl alcohol or any two kinds of combination, such as can
To be the combination of deionized water, methanol, ethyl alcohol, deionized water and methanol, the combination of deionized water and ethyl alcohol or methanol and ethyl alcohol
Combination.
Preferably, the washing times are 2-5 times, such as be can be 2 times, 3 times, 4 times or 5 times, preferably 3-4 times.
Preferably, the temperature of the drying is 60-100 DEG C, such as can be 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85
DEG C, 90 DEG C, 95 DEG C or 100 DEG C, preferably 70-90 DEG C, further preferably 75-85 DEG C.
Preferably, the time of the drying be 6-24h, such as can be 6h, 8h, 10h, 12h, 14h, 16h, 18h, 20h,
22h or for 24 hours, preferably 15-24h, further preferably 18-20h.
As currently preferred technical solution, the concentration of the first metal salt solution described in step (b) is 0.01-
0.5M, such as can be 0.01M, 0.1M, 0.15M, 0.2M, 0.25M, 0.3M, 0.35M, 0.4M, 0.45M or 0.5M, preferably
0.05-0.2M, further preferably 0.1-0.15M.
Preferably, described to be adsorbed as hydro-thermal enhancing absorption.
Preferably, hydro-thermal enhancing adsorption temp is 100-160 DEG C, for example, can be 100 DEG C, 110 DEG C, 120 DEG C,
130 DEG C, 140 DEG C, 150 DEG C or 160 DEG C, preferably 120-160 DEG C, further preferably 130-150 DEG C.
Preferably, the adsorption time is 1-6h, such as can be 1h, 2h, 3h, 4h, 5h or 6h, preferably 2-5h, into one
Walk preferred 3-4h.
Preferably, the mixed liquor obtained after absorption to absorption is centrifuged, and is taken out lower layer's solid, is washed.
Preferably, it is washed using one of deionized water, methanol or ethyl alcohol or any two kinds of combination, such as can
To be the combination of deionized water, methanol, ethyl alcohol, deionized water and methanol, the combination of deionized water and ethyl alcohol or methanol and ethyl alcohol
Combination.
Preferably, the washing times are 2-5 times, such as be can be 2 times, 3 times, 4 times or 5 times, preferably 3-4 times.
Preferably, the temperature of the drying is 60-100 DEG C, such as can be 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85
DEG C, 90 DEG C, 95 DEG C or 100 DEG C, preferably 70-90 DEG C, further preferred 75-85 DEG C.
Preferably, the time of the drying be 6-24h, such as can be 6h, 8h, 10h, 12h, 14h, 16h, 18h, 20h,
22h or for 24 hours, preferably 15-24h, further preferred 18-20h.
As currently preferred technical solution, the concentration of the second metal salt solution described in step (c) is 1-5M, example
It such as can be 1M, 1.5M, 2M, 2.5M, 3M, 3.5M, 4M, 4.5M or 5M, preferably 1-3M, further preferably 1.5-2.5M.
Preferably, described to be adsorbed as stirring and adsorbing.
Preferably, the adsorption temp be 20-60 DEG C, such as can be 20 DEG C, 25 DEG C, 30 DEG C, 35 DEG C, 40 DEG C, 45 DEG C,
50 DEG C, 55 DEG C or 60 DEG C, preferably 30-50 DEG C, further preferred 35-45 DEG C.
Preferably, the adsorption time be 4-24h, such as can be 4h, 6h, 8h, 10h, 12h, 14h, 16h, 18h,
20h, 22h or for 24 hours, preferably 8-20h, further preferred 10-18h.
Preferably, the mixed liquor obtained after absorption to absorption is filtered and is cleaned.
Preferably, it is washed using one of deionized water, methanol or ethyl alcohol or any two kinds of combination, such as can
To be the combination of deionized water, methanol, ethyl alcohol, deionized water and methanol, the combination of deionized water and ethyl alcohol or methanol and ethyl alcohol
Combination.
Preferably, the wash number is 2-5 times, such as be can be 2 times, 3 times, 4 times or 5 times, preferably 3-4 times.
Preferably, the scavenging period be 0.5-24h, such as can be 2h, 4h, 6h, 8h, 10h, 11h, 14h, 16h,
18h, 20h, 22h or for 24 hours, preferably 5-20h, further preferred 10-15h.
Preferably, the drying temperature is 60-100 DEG C, such as can be 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85
DEG C, 90 DEG C, 95 DEG C or 100 DEG C, preferably 70-90 DEG C, further preferred 75-85 DEG C.
Preferably, the drying time be 6-24h, such as can be 6h, 8h, 10h, 12h, 14h, 16h, 18h, 20h,
22h or for 24 hours, preferably 15-24h, further preferably 18-20h.
As currently preferred technical solution, roasting described in step (d) in Muffle furnace, tube furnace or kiln into
Row.
Preferably, the maturing temperature be 400-800 DEG C, such as can be 400 DEG C, 450 DEG C, 500 DEG C, 550 DEG C,
600 DEG C, 650 DEG C, 700 DEG C, 750 DEG C or 800 DEG C, preferably 450-600 DEG C, further preferred 500-550 DEG C.
Preferably, the time of the roasting be 0.5-10h, such as can be 0.5h, 1h, 1.5h, 2h, 2.5h, 3h,
3.5h, 4h, 4.5h, 5h, 5.5h, 6h, 6.5h, 7h, 7.5h, 8h, 8.5h, 9h, 9.5h or 10h, preferably 1-2h, it is further excellent
Select 1.2-1.8h.
Preferably, the heating rate of the roasting be 0.5-10 DEG C/min, such as can be 0.5 DEG C/min, 1 DEG C/min,
1.5℃/min、2℃/min、2.5℃/min、3℃/min、3.5℃/min、4℃/min、4.5℃/min、5℃/min、5.5
℃/min、6℃/min、6.5℃/min、7℃/min、7.5℃/min、8℃/min、8.5℃/min、9℃/min、9.5℃/
Min or 10 DEG C/min, preferably 0.5-1 DEG C/min, further preferred 0.6-0.8 DEG C/min.
Preferably, the atmosphere of the roasting is air and/or oxygen, preferably air or oxygen, the present invention by using
Oxygen atmosphere calcining, accelerates the crystallization of metal oxide and the combustion decomposition of carbon ball, generates bulk gas and impacts shell wall, is prepared into
The internal metal oxide hollow structure with a plurality of cavities is arrived.
In the preparation process in accordance with the present invention, step (a) and step (b) 1-5 times can be repeated before roasting, to obtain shell
The hollow more Shell Materials of metal composite oxide between layer 2-4.
The present invention by adjusting the concentration of two kinds of metal salts with different hydrated ionic radius, inhale by adsorption temp, repetition
The synthesis conditions such as attached number, calcination atmosphere can make the content of different metal oxides in shell change, to realize not
Specific absorption is generated with light of the shell to different wave length, further realizes and the effect that order absorbs is generated to white light in solar spectrum
It answers, enhances the absorbing ability of prepared more shell hollow sphere photochemical catalysts, and then improve its photocatalysis efficiency.
As currently preferred technical solution, which comprises
(a) the carbon source aqueous solution that concentration is 0.1-6M is fitted into hydro-thermal reaction 100- in 175-220 DEG C of reaction kettle
180min is filtered after natural cooling, and after 2-5 washing, by product at 60-100 DEG C dry 6-24h, obtain carbon ball mould
Plate;
(b) it disperses the carbon ball template that step (a) obtains in the first metal salt solution that concentration is 0.01-0.5M,
In the first metal salt solution be copper nitrate solution, copper chloride solution, copper-bath, tetrachloro close copper solution, cupric tetramminosulfate
Solution, iron nitrate solution, one of ferric chloride solution, cobalt nitrate solution, cobalt chloride solution and cobalt acetate solution or at least two
The combination of kind, hydro-thermal adsorbs 1-6h at 100-160 DEG C, and the mixed liquor after absorption is centrifuged, and takes out lower layer's solid, uses deionization
Water, methanol or ethanol washing 2-5 times, dry 6-24h, obtains the first solid precursor at 60-100 DEG C;
(c) the first solid precursor for obtaining step (b) is scattered in the second metal salt solution that concentration is 1-5M,
In, the second metal salt solution is titanium tetrachloride solution, titanium tetrabromide solution, titanium tetra iodide solution, fluorination titanium solution, four fourth of metatitanic acid
Ester solution, isopropyl titanate solution, titanyl sulfate solution, zinc nitrate solution, liquor zinci chloridi, cerous nitrate solution and cerium chloride are molten
One of liquid or at least two combination, filtered after stirring and adsorbing 4-24h at 20-60 DEG C, with deionized water, methanol or second
Alcohol washs 2-5 times, washs 0.5-24h, and dry 6-24h, obtains the second solid precursor at 60-100 DEG C;
(d) the second solid precursor for obtaining step (c) is placed in the atmosphere in Muffle furnace or kiln in air or oxygen
Middle roasting 0.5-10h, maturing temperature are 400-800 DEG C, and heating rate is 0.5-10 DEG C/min, obtain the compound gold after cooling
Belong to the hollow more Shell Materials of oxide.
Second aspect, the present invention provides a kind of metal composite oxides that preparation method as described in relation to the first aspect obtains
Hollow more Shell Materials, the hollow more Shell Materials of metal composite oxide include at least one cavity and at least one layer of shell
Wall, wherein wall surface accumulation there are two types of or two or more metal oxide nanoparticles or nanometer rods.
Preferably, the shell wall is 2~4 layers, such as can be 2 layers, 3 layers or 4 layers.
Preferably, the band gap of the metal oxide of the housing wall surface accumulation is greater than the metal oxygen of inner casing wall surface accumulation
The band gap of compound.
Preferably, the shell wall energy order absorbs solar spectrum.
Preferably, the order is absorbed as the ultraviolet portion in shell wall absorption solar spectrum, and inner wall absorbs too
Visible light part in solar spectrum.
The third aspect, the present invention provides a kind of photochemical catalyst, the photochemical catalyst includes answering as described in second aspect
Close the more Shell Materials of metal oxide hollow.
Preferably, the photochemical catalyst can be contained under the irradiation of 300W xenon lamp with the production hydrogen resolution of velocity of 70mmol/h/g
There is the water-methanol mixed solution of 25% volume fraction.
The hollow more stronger light absorpting abilities of Shell Materials of the metal composite oxide that the present invention is prepared, more shells are multiple
Miscellaneous multilevel structure also can significantly extend the optical circuit path for injecting catalyst.In addition, the characteristics of more shells itself, makes to be catalyzed
Agent has bigger specific surface area, keeps contact of the catalyst with reaction solution more abundant, and above-mentioned hollow sphere is applied to photocatalysis
The photochemical catalyst for decomposing aquatic products hydrogen can be realized to the absorption of the order of solar spectrum, can be under the irradiation of 300W xenon lamp
The production hydrogen resolution of velocity of 70mmol/h/g contains the water-methanol mixed solution of 25% volume fraction, and can obtain more than 90h's
Reaction stability, performance are significantly larger than the nano particle of same composition.
Numberical range of the present invention not only includes enumerated point value, further includes the above-mentioned numerical value not included
Arbitrary point value between range, as space is limited and for concise consideration, range described in the present invention no longer exclusive list includes
Specific point value.
Compared with prior art, the invention has the benefit that
1, the invention proposes being adsorbed by two steps, hydro-thermal enhancing absorption hydrated ionic radius is smaller first and corresponding gold
Belong to the lesser metal ion of oxide band gap, then adsorbs that hydration radius is larger and the corresponding biggish metal of metal oxide band gap
Ion makes different metal ions in the carbon ball template after adsorbing have apparent concentration gradient, to obtain compound gold after baking
Belong to the hollow more Shell Materials of oxide.By the obtained more shell oxide hollow spheres of absorption calcining can be realized outer shell for
The relatively strong of the weak short wavelength UV area light of penetration power absorbs, and the relatively strong of the hypostracum wavelength visible area strong for penetration power is inhaled
It receives.
2, the hollow more Shell Materials of metal composite oxide that the present invention is prepared have stronger light absorpting ability, more
The multilevel structure of shell complexity also can significantly extend the optical circuit path for injecting catalyst.In addition, the characteristics of more shells itself
Make catalyst that there is bigger specific surface area, keeps contact of the catalyst with reaction solution more abundant, multi-stage porous can also be conducive to
The transmission of liquids and gases.Above-mentioned hollow sphere is applied to the photochemical catalyst of photocatalysis Decomposition aquatic products hydrogen, can be realized to the sun
The order of spectrum absorbs, and can contain 25% volume fraction under the irradiation of 300W xenon lamp with the production hydrogen resolution of velocity of 70mmol/h/g
Water-methanol mixed solution, and the reaction stability more than 90h can be obtained, performance is significantly larger than the nanometer of same composition
Particle.