One kind is for VOCs argentum-based catalyzer preparation method of degrading
Technical field
The invention belongs to catalyst technical fields, and in particular to one kind is for degrade VOCs argentum-based catalyzer and its preparation side
Method.
Background technique
As air environmental pollution is got worse, there is a growing awareness that air environment prestige caused by human health
The side of body, and VOCs, that is, volatile organic contaminant is a kind of very harmful pollutant in atmosphere, it not only can be with the coup injury mankind
Respiratory mucosa causes surface skin allergy, and further secondary response forms photochemical fog and ozone pair in an atmosphere
Human health causes bigger harm.The discharge of VOCs is included in Con trolling index by national departments concerned, therefore efficient
The exploitation of VOCs degradation technique just seems more important.By using Ag/MnO2- ACF catalyst degradation VOCs is highest
One of method of effect is translated into CO while efficient degradation realizes that VOCs content reduces again2And H2O realizes innoxious
Discharge.
Most of effective catalyst is based on nano crystals catalyst now, and reaction temperature it is generally higher (110 DEG C with
On), and noble metal catalyst is using more in loaded catalyst, since noble metal is expensive, industrial application is difficult,
Noble metal utilisation is improved, while carrying out catalysis reaction under normal temperature conditions, realizes the economy and safety of catalytic degradation VOCs
Property become important research direction.In Ag/MnO2Atom level is realized by reducing the size of Ag active site in-ACF catalyst
Load, makes Ag active site high degree of dispersion, the utilization rate of precious metals ag, while MnO is improved while improving catalytic activity2
The carrier of the stronger adsorption function constituted with ACF carrier not only increases the monoatomic load stability of Ag, and plays and inhale
The attached synergistic effect with catalysis greatly improves catalytic activity.
Ag/MnO2The stable dispersion of monatomic Ag and the vacancy of catalyst surface are closely related in-ACF catalyst, foundation
Carrier surface vacancy is conducive to the realization of monatomic steady load.Tang Xingfu seminar etc. carries out to silver nano-grain catalyst
Discovery catalysis reaction occurs mainly in the neighboring atom of carrier and metal contact during research, reduces the partial size pair of noble metal
It is very desirable in improving metallic atom utilization rate.Long Liping etc. uses NiO/AL respectively2O3、CoO/AL2O3、MnO2/
AL2O3、Fe2O3/AL2O3And CuO/AL2O3Its O3 catalytic oxidation toluene performance is probed into, catalytic performance is best under normal temperature conditions
The degradation of toluene rate of catalyst be only 40%.Si Macong etc. uses Cu-Mn-Ce-O/ γ-AL2O3Catalyst is in 110-130
DEG C decline solution toluene in certain ozone concentration, toluene conversion is up to 83.9%.Nm-class catalyst still remains under normal low temperature
The lower disadvantage of catalytic performance.The size for reducing active site, can not only improve the utilization rate of noble metal, while also to a certain degree
On improve catalytic activity.MinLi etc. loads TiO2In in activated carbon fibre, under ultraviolet light conditions, the height of toluene is realized
Effect degradation.But article of the monatomic steady load on activated carbon fibre (ACF) be yet there are no into relevant report.
Summary of the invention
The purpose of the present invention is to overcome the disadvantages of the prior art, provides a kind of preparation of catalyst for VOCs degradation
Method, this method be not only able to achieve efficient degradation VOCs at normal temperature, but also can give full play to noble metal utilisation and realize monatomic bear
A possibility that carrying, enhancing catalyst industrial application.
The technical proposal for solving the technical problem of the invention are as follows:
A kind of preparation method of catalyst for VOCs degradation of the invention, comprising the following steps:
(1) activated carbon fibre piece is immersed in concentration is 0.1-0.2mol/L methanol solution 3-5min, uses deionization later
Water cleans 3-5min and removes the possible residue in surface, and taking-up is put into beaker and is placed in 55-65 DEG C of baking oven 20-30min, further takes out and put
Enter 2-3min in the NaOH solution that concentration is 0.5-1mol/L, then the activated carbon fibre piece for speckling with NaOH solution is placed into beaker
In, it is placed in 100-120 DEG C of baking oven and heats the hydrolysis that 30-40min promotes activated carbon fibre surface;
(2) taking mass ratio is (1-1.5): 4 (NH4)2C2O4·H2O and KMnO4It is molten to be dissolved in formation mixing in deionized water
Liquid, the KMnO4Solid-to-liquid ratio with deionized water is (0.015g-0.020g): 1ml;
Activated carbon fibre piece obtained by step (1), which will be put into mixed solution, and adds 0.2-0.5mol/L hydrochloric acid to mix
The pH of system is adjusted to 7-7.3, then mixed system is placed in the stirring in 90-110 DEG C of thermostatical oil bath with 140-160rpm
Speed is stirred to react 9-11h, and the taking-up of activated carbon fibre piece is washed with deionized 3-5 times after completion of the reaction, is put into 60-80 DEG C
Baking oven in dry 40-60min;The activated carbon fibre piece and KMnO4Mass ratio be 1:(0.3-0.6);
(3) ammonia spirit that mass fraction is 25%-30% is slowly added into AgNO3In solution, and stir until molten
Liquid bleach;The AgNO3AgNO in solution3It is (0.005-0.010) with taken activated carbon fibre tablet quality ratio in step (1):
1;
(4) H for being 30-35% by mass fraction2O2Solution is added in step (3) in clear solution and soaking step (2)
Gained activated carbon fiber piece stirs 30-40min at 0-10 DEG C, finally filters mixture in beaker, by filtrate deionization
Water cleans 3-5 times, the H2O2H in solution2O2With AgNO3Mass ratio (1.5-2): 1;
(5) filtrate dry 10-12h at 60-80 DEG C is obtained later by it in 300-400 DEG C of calcining 3-5h after washing
Obtain Ag/MnO2-ACF。
The invention has the benefit that in Ag/MnO2It is realized in-ACF catalyst by reducing the size of Ag active site
Atom level load, makes Ag active site high degree of dispersion, the utilization rate of precious metals ag is improved while improving catalytic activity, together
When MnO2The carrier of the stronger adsorption function constituted with ACF carrier not only increases the monoatomic load stability of Ag, and
The synergistic effect for playing absorption and catalysis greatly improves catalytic activity.
Detailed description of the invention
Fig. 1 is present invention preparation Ag/MnO2- ACF catalyst process schematic diagram.
Specific embodiment
The present invention is described in detail combined with specific embodiments below.
The present invention prepares reaction equation about the monatomic catalyst of Ag/Mn2-ACF:
KMnO4+(NH4)2C2O4·H2O+-OH→MnO2-
NH3·H2O+AgNO3→Ag(NH3)2OH+H2O
Ag(NH3)2OH+H2O2+MnO2-→AgMnO2-
There are also hydroxyl groups abundant in activated carbon fibre (ACF), can be formed by potassium permanganate oxidation and ACF is with chemical bond
Connected MnO2, and then with MnO2As young brilliant, promote in the liquid phase potassium permanganate the MnO to be formed is reacted with ammonium oxalate2Stablize
The surface ACF is formed with the MnO compared with multi-hole2- ACF carrier, so using anti-Ostwald method by Ag it is monatomic you load to
MnO2On-ACF carrier, to obtain monatomic Ag/MnO2- ACF catalyst.
Based on principles above, a kind of preparation method of catalyst for VOCs absorption degradation of the invention, including it is following
Step:
(1) activated carbon fibre piece is immersed in concentration is 0.1-0.2mol/L methanol solution 3-5min, uses deionization later
Water cleans 3-5min and removes the possible residue in surface, and taking-up is put into beaker and is placed in 55-65 DEG C of baking oven 20-30min, further takes out and put
Enter 2-3min in the NaOH solution that concentration is 0.5-1mol/L, then the activated carbon fibre piece for speckling with NaOH solution is placed into beaker
In, it is placed in 100-120 DEG C of baking oven and heats the hydrolysis that 30-40min promotes activated carbon fibre surface.
(2) taking mass ratio is (1-1.5): 4 (NH4)2C2O4·H2O and KMnO4It is molten to be dissolved in formation mixing in deionized water
Liquid, the KMnO4Solid-to-liquid ratio with deionized water is (0.015g-0.020g): 1ml.By activated carbon fibre piece obtained by step (1)
It is put into mixed solution and adds 0.2-0.5mol/L hydrochloric acid and adjust the pH of mixed system to 7-7.3, then by mixture
It is that the mixing speed being placed in 90-110 DEG C of thermostatical oil bath with 140-160rpm is stirred to react 9-11h, will lives after completion of the reaction
Property Carbon fibe piece taking-up be washed with deionized 3-5 time, be put into 60-80 DEG C of baking oven dry 40-60min.The active carbon
Fibre plate and KMnO4Mass ratio be 1:(0.3-0.6).
(3) ammonia spirit that mass fraction is 25%-30% is slowly added into AgNO3In solution, and stir until molten
Liquid bleach.The AgNO3AgNO in solution3It is (0.005-0.010) with taken activated carbon fibre tablet quality ratio in step (1):
1。
(4) H for being 30-35% by mass fraction2O2Solution is added in step (3) in clear solution and soaking step (2)
Gained activated carbon fiber piece stirs 30-40min at 0-10 DEG C, finally filters mixture in beaker, by filtrate deionization
Water cleans 3-5 times, the H2O2H in solution2O2With AgNO3Mass ratio (1.5-2): 1.
(5) filtrate dry 10-12h at 60-80 DEG C is obtained later by it in 300-400 DEG C of calcining 3-5h after washing
Obtain Ag/MnO2-ACF。
Embodiment 1
(1) 0.1g activated carbon fibre piece is immersed in concentration is 0.1mol/L methanol solution 3min, uses deionized water later
It cleans 3min and removes the possible residue in surface, taking-up is put into beaker and is placed in 55 DEG C of baking oven 20min, further takes out and is put into concentration and is
2min in the NaOH solution of 0.5mol/L, then the activated carbon fibre piece for speckling with NaOH solution is placed in beaker, it is placed in 100 DEG C
The hydrolysis that 30min promotes activated carbon fibre surface is heated in baking oven.
(2) taking mass ratio is the (NH of 1:44)2C2O4·H2O and KMnO4It is dissolved in deionized water and forms mixed solution, it is described
KMnO4Solid-to-liquid ratio with deionized water is 0.015g:1ml.Activated carbon fibre piece obtained by step (1) is put into mixed solution
And add 0.2mol/L hydrochloric acid and adjust the pH of mixed system to 7, then by mixed system be placed in 90 DEG C of thermostatical oil baths with
The mixing speed of 140rpm is stirred to react 9h, and the taking-up of activated carbon fibre piece is washed with deionized 3 times after completion of the reaction, is put into
Dry 40min in 60 DEG C of baking oven.The activated carbon fibre piece and KMnO4Mass ratio be 1:0.3.
(3) ammonia spirit that mass fraction is 25% is slowly added into AgNO3In solution, and stir until solution becomes saturating
It is bright.The AgNO3AgNO in solution3It is 0.005:1 with taken activated carbon fibre tablet quality ratio in step (1).
(4) H for being 30% by mass fraction2O2Solution is added in step (3) in clear solution and soaking step (2) institute
Activated carbon fiber piece is obtained, 30min is stirred at 0 DEG C, finally mixture in beaker is filtered, filtrate is cleaned 3 with deionized water
It is secondary, the H2O2H in solution2O2With AgNO3Mass ratio 1.5:1.
(5) filtrate dry 10h at 60 DEG C, obtains Ag/MnO in 300 DEG C of calcining 3h for it later after washing2-
ACF is denoted as A.
Embodiment 2
(1) 0.1g activated carbon fibre piece is immersed in concentration is 0.15mol/L methanol solution 4min, uses deionized water later
It cleans 4min and removes the possible residue in surface, taking-up is put into beaker and is placed in 60 DEG C of baking oven 25min, further takes out and is put into concentration and is
2.5min in the NaOH solution of 0.8mol/L, then the activated carbon fibre piece for speckling with NaOH solution is placed in beaker, it is placed in 110 DEG C
Baking oven in heating 35min promote activated carbon fibre surface hydrolysis.
(2) taking mass ratio is the (NH of 1.2:44)2C2O4·H2O and KMnO4It is dissolved in deionized water and forms mixed solution, institute
State KMnO4Solid-to-liquid ratio with deionized water is 0.018:1ml.Activated carbon fibre piece obtained by step (1) is put into mixed solution
In and add 0.3mol/L hydrochloric acid and adjust the pH of mixed system to 7.2, mixed system is then placed in 100 DEG C of thermostatical oil baths
In 10h is stirred to react with the mixing speed of 150rpm, the taking-up of activated carbon fibre piece is washed with deionized 4 after completion of the reaction
It is secondary, dry 50min is put into 70 DEG C of baking oven.The activated carbon fibre piece and KMnO4Mass ratio be 1:0.4.
(3) ammonia spirit that mass fraction is 28% is slowly added into AgNO3In solution, and stir until solution becomes saturating
It is bright.The AgNO3AgNO in solution3It is 0.008:1 with taken activated carbon fibre tablet quality ratio in step (1).
(4) H for being 33% by mass fraction2O2Solution is added in step (3) in clear solution and soaking step (2) institute
Activated carbon fiber piece is obtained, 35min is stirred at 5 DEG C, finally mixture in beaker is filtered, filtrate is cleaned 4 with deionized water
It is secondary, the H2O2H in solution2O2With AgNO3Mass ratio 1.8:1.
(5) filtrate dry 11h at 70 DEG C, obtains Ag/MnO in 350 DEG C of calcining 4h for it later after washing2-
ACF is denoted as B.
Embodiment 3
(1) 0.1g activated carbon fibre piece is immersed in concentration is 0.2mol/L methanol solution 5min, uses deionized water later
It cleans 5min and removes the possible residue in surface, taking-up is put into beaker and is placed in 65 DEG C of baking oven 30min, further takes out and is put into concentration and is
3min in the NaOH solution of 1mol/L, then the activated carbon fibre piece for speckling with NaOH solution is placed in beaker, it is placed in 120 DEG C of baking
The hydrolysis that 40min promotes activated carbon fibre surface is heated in case.
(2) taking mass ratio is the (NH of 1.5:44)2C2O4·H2O and KMnO4It is dissolved in deionized water and forms mixed solution, institute
State KMnO4Solid-to-liquid ratio with deionized water is 0.020g:1ml.Activated carbon fibre piece obtained by step (1) is put into mixed solution
In and add 0.5mol/L hydrochloric acid and adjust the pH of mixed system to 7.3, mixed system is then placed in 110 DEG C of thermostatical oil baths
In 11h is stirred to react with the mixing speed of 160rpm, the taking-up of activated carbon fibre piece is washed with deionized 5 after completion of the reaction
It is secondary, dry 60min is put into 80 DEG C of baking oven.The activated carbon fibre piece and KMnO4Mass ratio be 1:0.6.
(3) ammonia spirit that mass fraction is 30% is slowly added into AgNO3In solution, and stir until solution becomes saturating
It is bright.The AgNO3AgNO in solution3It is 0.010:1 with taken activated carbon fibre tablet quality ratio in step (1).
(4) H for being 35% by mass fraction2O2Solution is added in step (3) in clear solution and soaking step (2) institute
Activated carbon fiber piece is obtained, 40min is stirred at 10 DEG C, finally mixture in beaker is filtered, filtrate is cleaned 5 with deionized water
It is secondary, the H2O2H in solution2O2With AgNO3Mass ratio 2:1.
(5) filtrate dry 12h at 80 DEG C, obtains Ag/MnO in 400 DEG C of calcining 5h for it later after washing2-
ACF is denoted as C.
The catalyst of embodiment 1,2,3 is fitted into catalytic evaluation device, for the adsoption catalysis degradation reaction of toluene,
Reaction condition is that toluene is 500ppm, and reaction temperature is 65 DEG C, reaction velocity 8000h-1.Catalytic activity is shown in Table 1.
Table 1
, it can be seen that Ag/MnO prepared by the present invention from table 12- ACF catalyst, degradation of toluene rate with higher
With mineralization rate.
Although the embodiments of the present invention has been shown and described above, but the invention is not limited to above-mentioned specific
Embodiment, the above mentioned embodiment is only schematical, rather than restrictive, and technology belonging to the present invention is led
For the those of ordinary skill in domain, without departing from the inventive concept of the premise, several simple deductions can also be made or replaced
It changes, all shall be regarded as belonging to the present invention by the claims submitted and determine scope of patent protection.