CN104549370B - Photocatalysis cellular activated carbon net - Google Patents

Photocatalysis cellular activated carbon net Download PDF

Info

Publication number
CN104549370B
CN104549370B CN201410830775.1A CN201410830775A CN104549370B CN 104549370 B CN104549370 B CN 104549370B CN 201410830775 A CN201410830775 A CN 201410830775A CN 104549370 B CN104549370 B CN 104549370B
Authority
CN
China
Prior art keywords
activated carbon
carbon net
photocatalyst
cellular
alveolate activated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201410830775.1A
Other languages
Chinese (zh)
Other versions
CN104549370A (en
Inventor
许升
孔德双
谷昌军
刘志斌
孔令仁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU GAOCHUN CERAMICS CO Ltd
Original Assignee
JIANGSU GAOCHUN CERAMICS CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JIANGSU GAOCHUN CERAMICS CO Ltd filed Critical JIANGSU GAOCHUN CERAMICS CO Ltd
Priority to CN201410830775.1A priority Critical patent/CN104549370B/en
Publication of CN104549370A publication Critical patent/CN104549370A/en
Application granted granted Critical
Publication of CN104549370B publication Critical patent/CN104549370B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Catalysts (AREA)

Abstract

Photocatalysis cellular activated carbon net disclosed by the invention, using Alveolate activated carbon net as carrier, has loaded the TiO of Co, Pr and S on the net at Alveolate activated carbon2, described TiO2In photocatalyst Co: Pr: S: TiO2Mol ratio be 0.01~0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2.Both kept the function of activated carbon adsorption organic pollution, there is again the ability of catalyst responding to visible light degradable organic pollutant.It is good that photocatalysis Alveolate activated carbon net has straight hole network structure, aeration and light transmission, and its specific surface area is 750~1050m2/ g, iodine sorption value is 900~1100mg/g, and carbon tetrachloride adsorption rate is 40~60%.At 30m3Confined space and with visible ray as light source, the formaldehyde clearance after 50min is 95.6~98.7%, and toluene is 90.3~93.6%, and ammonia is 92.8~96.0%.

Description

Photocatalysis cellular activated carbon net
Technical field
The present invention relates to photocatalysis cellular activated carbon net and preparation method, especially Alveolate activated carbon net carrier and doping TiO2 The preparation of photocatalyst and the method that catalyst is carried on carrier.
Background technology
Activated carbon is widely used to administer air and water pollution as excellent adsorbent, conventional for granular active carbon and powder End activated carbon.The ature of coal cellular activated carbon developed in recent years has the advantage that specific surface area is big, absorption property is strong, the most very Paid attention to.Although it has many advantages, but the most saturated, use cost is high, even if being also difficult to be returned to previous level by regeneration.
With TiO2All of pollutant generation photolysis almost can be made under action of ultraviolet light to be changed into nothing as photocatalyst Pest, and reaction condition is gentle (room temperature, normal pressure), although there is very much prospect, but there is TiO2Can not by excited by visible light, Powdered form uses the drawbacks such as difficult recovery.This is carried out and has included to TiO2It is entrained in interior method to extend the sound to visible ray Should, and and the method for exploitation fixed catalyst.
For overcoming the deficiency of activated carbon and photocatalysis technology, play the strong point of the two, the most by photocatalysis technology and absorption The report that technology combines.The most conventional activated carbon supported TiO2Method have two kinds, one be by precursor load On carrier, then reheat and make precursor be changed into TiO2;Another kind is by TiO2Nano-powder is loaded by various modes On carrier.
CN1288077C discloses a kind of method directly being prepared Alveolate activated carbon by coal.The method is by coal dust, emulsifying coal Tar, water-soluble binder, lubricant and water through raw material pulverizing, dispensing, kneading, extrusion molding, be dried, carbonization, work Change and obtain.This invention has low cost, production equipment simplifies, the Alveolate activated carbon of preparation has unit volume specific surface area Greatly, voidage acid-fast alkali-proof high, water-fast, comprcssive strength high, heat-resist, the advantage such as easy hot recycling or regenerated from washing.But The physical property of material must be improved.
CN101857224 discloses the preparation method of a kind of resin-bonded Alveolate activated carbon, by dry powder blend, wet method kneading The honeycomb that the step of preparation plasticity pug, vacuum pugging, extrusion molding, dry, cured and secondary heat treatment obtains Activated carbon, owing to its phenolic resin is in addition to the mechanical strength that performance cementation improves this activated carbon, moreover it is possible to significantly improve honeybee The thermostability of nest shaped activated carbon;Add porous mineral and more can be effectively improved mechanical strength and the specific surface area of Alveolate activated carbon; This processing method heat treatment temperature ratio is relatively low, and energy consumption is little, it is possible to effectively reduce production cost;And preparation technology and equipment letter Single, investment of production is smaller, reduce further cost.
CN101596457A discloses a kind of boron and other element coblended nano TiO 2 light catalyst and preparation method thereof, Be use titanate esters and boric acid as titanium source and boron source, other doped chemical comprise transition metal, rare earth metal or nonmetal in One or more, use acetic acid, nitric acid or citric acid as hydrolysis catalyst, alcohol and water mixture as reaction system, Boron and other element coblended nano TiO 2 light catalyst is prepared by sol gel reaction and calcining.This method is used to prepare Boron and other element coblended nano TiO 2, it is possible to absorb visible ray and also there is visible light catalysis activity.
CN1015492994 discloses a kind of non-metallic element multiple doping nano titanium dioxide photocatalyst, mixes in this catalyst By weight percentage, carbon is 30~50% to miscellaneous nonmetalloid content, and nitrogen is 8~30%, and sulfur is 1~2%, and at content is In 100MG/L MBD liquid, add this catalyst of 2g/l, and degrade 2 hours under ultraviolet light, visible ray or daylight, its Degradation rate is all more than 95%.This invention also discloses the preparation method of this photocatalyst.The photocatalyst provided due to the present invention Doped with non-metals constituent content contained by is high, thus it not only has preferably response to ultraviolet light, visible ray or daylight, can make dye Dyestuff in liquid is degraded rapidly, and low cost.Additionally the system of preparation method is simple, and process is easily-controllable, operates safety, and also has Good repeatability.
CN101653720A disclose a kind of by the Alveolate activated carbon prepared in nanometer light catalyst solvent impregnation process Technology, this technology, can be with nuisances such as decomposing formaldehydes under illumination condition owing to adding photocatalyst agent on cellular activated carbon Matter, thus there is self-cleaning function.
Above-mentioned report relate to the preparation method of Alveolate activated carbon net, the preparation method of the photocatalyst that adulterates, and by catalyst The technique being carried on Alveolate activated carbon, but there is not yet the patent identical with present invention or document report.
Summary of the invention
It is an object of the invention to: aim to provide the product with the function such as visible light photocatalytic degradation and activated carbon adsorption, physical arrangement Performance is good, i.e. provides energy efficient degradation organic exhaust gas, the photocatalysis ature of coal Alveolate activated carbon of waste water and preparation method.
The technical scheme is that photocatalysis cellular activated carbon net, using Alveolate activated carbon net as carrier, in cellular work Property charcoal has loaded the TiO of Co, Pr and S on the net2, described TiO2In photocatalyst Co: Pr: S: TiO2Mol ratio be 0.01~0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2.
The size of Alveolate activated carbon net is 100~250mm × 100~250mm × 10~20mm, and the hole density of net is 30~50 Hole/cm2, the length of side that is shaped as in hole is square or equilateral triangle or the regular hexagon of 1~2mm.
The preparation method of photocatalysis cellular activated carbon net, prepares and has high density holes, high-specific surface area, straight hole structure, ventilative The ature of coal cellular activated carbon net carrier good with light transmission, comprises the following steps: first, including: 1. raw material consists of: coal dust: Inorganic filler: low temperature bonding agent: high-temperature agglomerant: lubricant: the mass ratio of water is 45~65: 2~15: 1~4: 10~20: 2~3: 10~15, wherein coal dust be bituminous coal with anchracite duff with 1: 0.2~0.8 mixture, inorganic filler is One or more in Kaolin or attapulgite or clay or Maifanitum or meerschaum arbitrarily mix;Low temperature glues Knot agent is that one or more in methylcellulose or hydroxypropyl methyl cellulose or carboxymethyl cellulose arbitrarily mix; High-temperature agglomerant is that one or more in coal tar or sodium dihydrogen phosphate or aluminium dihydrogen phosphate arbitrarily mix;Coal tar Bitumen content more than 35%, lubricant is edible oil or Polyethylene Glycol;The fineness of all non-aqueous solid materials is all crushed to More than 200 mesh.2. pretreatment of raw material, including: raw material is sufficiently mixed and mediates, then through vacuum white silk system with old, system Uniformly plasticity pug.3. pug is extruded into honeycomb ceramics, microwave drying, then carbonization in batch-type furnace under nitrogen protection, Finally it is passed through steam or carbon dioxide activation, i.e. obtains ature of coal Alveolate activated carbon net.
Secondly, preparation is doped with the nano-TiO of the elements such as Co, Pr and S2Photocatalyst, makes it to utilize excited by visible light Produce activated state oxygen, cause a series of redox reaction, make organic pollutant degradation.Including with CH4N2S is the raw material of sulfur, After dissolving in dehydrated alcohol, then mix the addition of C o (NO3)2·6H2O and Pr (NO3)3·6H2O, drips Ti (OC again after dissolving4H9)4Again Calcine at 500 DEG C, be ground to more than 200 mesh, prepare powdered form photocatalyst.
Its three, by prepared powdery photocatalyst on ature of coal cellular activated carbon net carrier, including: first clean carrier, point Do not use ultrasonic cleaning again after ammonia, nitric acid and soak with ethanol, dry;Then photocatalyst powder is carried on carrier, i.e. Photocatalyst powder is mixed with certain proportion with epoxy resin, adds ethanol and make serosity, then by the coal through pretreatment Honeycomb ceramic net is impregnated in serosity, takes out and dries, finally in 500 ± 100 DEG C, N in batch-type furnace2The lower roasting of protection, I.e. prepare photocatalysis ature of coal ceramic honey comb net.Control the dipping of ature of coal ceramic honey comb net and dry number of times, photocatalyst can be increased Load capacity.
The present invention has also carried out the organic gas clearances such as catalyst intensity of load, load factor, XRD, SEM, formaldehyde to sample Mensuration, characterize the characteristic of photocatalysis cellular activated carbon net.
The invention has the beneficial effects as follows: the present invention provide photocatalysis Alveolate activated carbon net owing to specific surface area is big, aeration is good, Thus improve the function of activated carbon adsorption organic pollutant, and there is good intensity, it is the most convenient to assemble and install and use; Due to activated carbon adsorption effect, the photocatalyst for loading provides the machine thing pollutant of higher concentration, thus improves photocatalysis Efficiency;Again due at nano-TiO2It is doped with the elements such as Co, Pr and S, enables it to utilize visible ray to produce catalytic action, fall Low photocatalysis cost is the highest in the absorption efficiency of visible ray.Therefore, photocatalysis Alveolate activated carbon net is to combine visible ray It is catalyzed, is adsorbed in the product of one process organic pollution.And preparation method is unique, basic non-environmental-pollution.Photocatalysis honeycomb It is good that shaped activated carbon net has straight hole network structure, aeration and light transmission, and its specific surface area is 750~1050m2/ g, iodine adsorbs Value is 900~1100mg/g, and carbon tetrachloride adsorption rate is 40~60%.At 30m3Confined space and with visible ray as light source, Formaldehyde clearance after 50min is 95.6~98.7%, and toluene is 90.3~93.6%, and ammonia is 92.8~96.0%.
Detailed description of the invention
The preparation of ature of coal Alveolate activated carbon net
(1) raw material consists of: coal dust: inorganic filler: low temperature bonding agent: high-temperature agglomerant: lubricant: the mass ratio of water Be 45~65: 2~15: 1~4: 10~20: 2~3: 10~15, inorganic filler be Kaolin, attapulgite, clay, One or more in Maifanitum or meerschaum arbitrarily mix;Low temperature bonding agent is methylcellulose, hydroxypropyl methyl fiber One or more in element or carboxymethyl cellulose arbitrarily mix;High-temperature agglomerant is coal tar, sodium dihydrogen phosphate or phosphoric acid One or more in aluminum dihydrogen arbitrarily mix;The bitumen content of coal tar is more than 35%, and lubricant is edible oil or poly-second Glycol;All non-aqueous solid materials are all crushed to more than 200 mesh;
(2) raw material mixing with mediate: coal dust, inorganic filler and low temperature bonding agent are added in blender be sufficiently stirred for 10~ 30min, the uniform siccative obtained is placed in kneader, sequentially adds high-temperature agglomerant, lubricant and water, stirring mediate 15~ 45min, makes uniform plasticity pug;
(3) pug practices system with old: is added by above-mentioned plasticity pug in vacuum deairing machine, keeps vacuum-0.06MPa Above, pump the air in pug, repeat to practice system and make pug mix homogeneously for more than 2 times, then by close for pug plastic film wrapped After sealing old 12~48h stand-by;
(4) extrusion molding: old good pug is equipped with on the extrusion shaping machine of cellular steel mould, with more than 8MPa's Pressure is extruded, and obtains cellular wet idiosome;
(5) being dried: put in microwave dryer by cellular wet idiosome, controlling microwave frequency is 0.8~1.5GHz, is dried 10~30min, obtain the cellular idiosome being dried;
(6) carbonization and activation: put in atmosphere protection batch-type furnace by dry cellular activated carbon base substrate, with nitrogen for protection gas Body, by for 3~8 DEG C/min ramp to 500~700 DEG C, carbonization 1~3h;Then by 5~10 DEG C/min ramp To 700~900 DEG C, it is passed through steam or carbon dioxide simultaneously, activates 1~5h, obtain Alveolate activated carbon, cellular activity Charcoal cuts into charcoal net, and loaded optic catalyst obtains photocatalysis cellular activated carbon net.
Wherein coal dust be bituminous coal with anchracite duff with 1: 0.2~0.8 mixture.
Photocatalyst is as follows for doping photocatalyst preparation method: take a certain amount of CH4N2S (thiourea) pulverizes with mortar, adds The absolute ethyl alcohol and stirring of 1~2 times of weight is dissolved, and adds and the addition of C o (NO3)2·6H2O、Pr(NO3)3·6H2O, stirring, so After slowly drip butyl titanate Ti (OC4H9)4, stir 0.5-2h, at 60 DEG C, vacuum drying obtains white crystal, is aged 2d Calcining 1~2h at latter 500 DEG C, sample is being ground to more than 200 mesh, i.e. obtains Co, Pr, S codope TiO2Photocatalyst Finished product;Wherein Co: Pr: S: TiO2Mol ratio is 0.01~0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2.
It is to be first to clean cellular activated carbon net carrier: by ature of coal honeycomb in the method for cellular activated carbon net by photocatalyst Active carbon net carrier is immersed in the ammonia spirit that mass fraction is 26%, and liquid and impurity are removed in ultrasonic cleaning 20min hypsokinesis, uses Deionized water wash 3 times;Remove liquid and impurity with the nitric acid ultrasonic cleaning 20min hypsokinesis that mass fraction is 45% again, spend from Sub-water washs 3 times.Then remove liquid and impurity with the hypsokinesis of alcohol dipping 10min, be washed with deionized 3 times, finally exist Dry 3h for 105 DEG C;
Followed by by photocatalyst on cellular activated carbon net carrier: weigh a certain amount of epoxy resin and 5~20g respectively Photocatalyst powder be placed in beaker, add 100~400ml ethanol, stir under 7000r/min rotating speed with high-speed shearing machine Mix 1h, then the ature of coal ceramic honey comb net through pretreatment be impregnated in the ethanol serosity of epoxy resin, 15min take out after Vacuum drying 5h at 60 DEG C, finally in 500 DEG C, N in batch-type furnace2The lower roasting 2h of protection, i.e. prepares photocatalysis ature of coal honeycomb Ceramic network.Control ature of coal ceramic honey comb net dipping in the ethanol serosity of epoxy resin and dry number of times, increasing photocatalyst Load capacity.
Described cellular steel mould is 20~50 holes/cm2Square or cylinder cellular steel mould.
Embodiment 1
1, (1) raw material and consisting of: coal dust: inorganic filler: low temperature bonding agent: high-temperature agglomerant: lubricant: water Mass ratio is 45~65: 2~15: 1~4: 10~20: 2~3: 10~15, wherein coal dust be bituminous coal with anchracite duff with The mixture of 1: 0.2~0.8, inorganic filler is in Kaolin or attapulgite or clay or Maifanitum or meerschaum One or more arbitrarily mix;Low temperature bonding agent be methylcellulose or hydroxypropyl methyl cellulose or carboxymethyl fine One or more in dimension element arbitrarily mix;High-temperature agglomerant is in coal tar or sodium dihydrogen phosphate or aluminium dihydrogen phosphate One or more arbitrarily mix;The bitumen content of coal tar is more than 35%, and lubricant is edible oil or Polyethylene Glycol; The fineness of all non-aqueous solid materials is all crushed to more than 200 mesh.
(2) raw material mixing with mediate: coal dust, inorganic filler and low temperature bonding agent are added in blender be sufficiently stirred for 10~ 30min, obtains uniform siccative and is placed in kneader, sequentially adds high-temperature agglomerant, lubricant and water, stirring mediate 15~ 45min, makes uniform plasticity pug.
(3) pug practices system with old: added in vacuum deairing machine by above-mentioned plasticity pug, holding vacuum-0.06MPa with On, pump the air in pug, repeat to practice system and make pug mix homogeneously for more than 2 times, then pug plastic film wrapped is sealed After old 12~48h stand-by.
(4) extrusion molding: old good pug is equipped with on the extrusion shaping machine of cellular steel mould, with more than 8MPa's Pressure is extruded, and obtains cellular wet idiosome.
(5) being dried: put in microwave dryer by cellular wet idiosome, controlling microwave frequency is 0.8~1.5GHz, is dried 10~30min, obtain the cellular idiosome being dried.
(6) carbonization and activation: dry cellular idiosome is put in atmosphere protection batch-type furnace, with nitrogen as protective gas, By for 3~8 DEG C/min ramp to 500~700 DEG C, carbonization 1~3h.Then by 5~10 DEG C/min ramp to 700~ 900 DEG C, it is passed through steam or carbon dioxide simultaneously, activates 1~5h, obtain ature of coal Alveolate activated carbon.
2, doping Co, Pr, S element ti O2The preparation of photocatalyst
Take a certain amount of CH4N2S (thiourea) pulverizes with mortar, and the absolute ethyl alcohol and stirring adding 1~2 times of weight is dissolved, then adds Enter and the addition of C o (NO3)2·6H2O、Pr(NO3)3·6H2O, stirring, the most slowly drip Ti (OC4H9)4(butyl titanate), Stirring 1h, at 60 DEG C, vacuum drying obtains white crystal, calcines 1~2h after ageing 2d at 500 DEG C, and sample is being ground to 200 More than mesh, i.e. obtain Co, Pr, S codope TiO2Photocatalyst finished product.Wherein Co: Pr: S: TiO2Mol ratio be 0.01~ 0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2.
3, photocatalyst is in carrier
(1) Vehicle element: be immersed in the ammonia spirit that mass fraction is 26% by ature of coal cellular activated carbon net carrier is super Sound cleans 20min hypsokinesis and removes liquid and impurity, is washed with deionized 3 times.Ultrasonic clearly with the nitric acid that mass fraction is 45% again Wash 20min hypsokinesis and remove liquid and impurity, be washed with deionized 3 times.Then liquid and miscellaneous is removed with the hypsokinesis of alcohol dipping 10min Matter, is washed with deionized 3 times.Finally dry 3hr at 105 DEG C.
(2) photocatalyst is in carrier: weigh respectively a certain amount of epoxy resin and 5~20g photocatalyst powder put In beaker, add 100~400ml ethanol, under 7000r/min rotating speed, stir 1h with high-speed shearing machine, then will pass through The ature of coal ceramic honey comb net of pretreatment is impregnated in the ethanol serosity of epoxy resin, 15min take out after at 60 DEG C vacuum drying 5h, finally in 500 DEG C, N in batch-type furnace2The lower roasting 2h of protection, i.e. prepares photocatalysis ature of coal cellular activated carbon net.Control coal Honeycomb ceramic net dipping in the ethanol serosity of epoxy resin and dry number of times, can increase the load capacity of photocatalyst.
4, performance detection
(1) intensity of load: by activated carbon supported TiO2Catalysis material is fixed in small-sized wind tunnel, and wind speed is 5m/s, 1h Rear mensuration weight-loss ratio.
(2) load factor: by activated carbon supported TiO2Catalysis material is roasting 2h at 1000 DEG C, and activated carbon is completely burned off, Remaining containing TiO2Solid, containing TiO on unit of account mass activity charcoal2The load factor of solid.
(3) SEM: observe catalysis material configuration of surface.
(4) XRD: observe TiO2Crystalline state.
(5) mensuration of iodine sorption value is according to GB/T 7702.7-2008
(6) mensuration 7702.20-2008 of specific surface area
(7) the mensuration GB/T 7702.13-1997 of carbon tetrachloride adsorption rate
(8) formaldehyde determination uses GB/T 18204.26-2000 standard, and ammonia measures and uses indophenol blue colorimetry, and toluene measures Use GB/T 14677-1993 standard.Analyze sample be taken respectively from: at 30m3Room in place equipped with 2 50W xenons Lamp lamp (falling the ultraviolet light of 200-400nm with ultraviolet ray intercepting glass membrane filtration), 12 pieces of photocatalysis cellular activated carbon nets and 1 typhoon amount is 3m3The blower fan of/min, allows the volatilization of liquid phase formaldehyde make indoor reach finite concentration (C0), it is then turned on light source and wind Machine makes formaldehyde pass through the circulation degraded of photocatalytic active carbon net, measures the concentration C after photodissociation after 50min1, then the clearance R of formaldehyde:
R = C 0 - C 1 C 0 × 100 %
Same method measures toluene and the clearance of ammonia.
Embodiment 2
1, the preparation of ature of coal Alveolate activated carbon net
(1) pretreatment of raw material: 7200g coal dust (6000g bituminous coal+1200g anthracite, be more than 200 mesh), 200g Clay (more than 200 mesh), 300g hydroxypropyl methyl cellulose, 250g Polyethylene Glycol add in blender, are sufficiently stirred for 30min, Adding 2000g coal tar (bitumen content is more than 35%) and 1160ml water, 25min is mediated in stirring.It is placed in vacuum the most again In pug mill, vacuum remains-0.08MPa, pumps the air in pug, practices 25min processed and makes pug mix homogeneously.Then By stand-by after the pug plastic film wrapped old 12h of sealing, obtain uniform plasticity pug.
(2) extrusion molding is with dry: be equipped with on the extrusion shaping machine of cellular steel mould by old good pug, with 15MPa Pressure extrusion, obtain cellular wet idiosome, a size of 220mm × 110mm × 15mm, hole density is 46 holes/cm2.Put again Entering in microwave dryer, controlling microwave frequency is that 1GHz is dried 20min, obtains the cellular idiosome being dried.
(3) carbonization and activation: dry cellular idiosome is put in atmosphere protection batch-type furnace, with nitrogen as protective gas, By 5 DEG C/min ramp to 700 DEG C, carbonization 1h;Then by 8 DEG C/min ramp to 850 DEG C, it is passed through water simultaneously and steams Gas activation 1h, obtains ature of coal Alveolate activated carbon.
2, doping Co, Pr, S element ti O2The preparation of photocatalyst
Take the CH of 45g4N2S pulverizes, and adds 90ml absolute ethyl alcohol and stirring and dissolves, adds the Co (NO of 39g3)2·6H2O、24g Pr (NO3)3·6H2O, stirring, the most slowly drip 2040gTi (OC4H9)4(butyl titanate), stirs 1h, at 60 DEG C Vacuum drying obtains white crystal, calcines 1~2h after ageing 2d at 500 DEG C, and sample is being ground to more than 200 mesh, i.e. obtains Co, Pr, S codope TiO2Photocatalyst finished product.
3, photocatalyst is in carrier
It is 30~40 holes/cm by 20 pieces a size of 100~250mm × 100~250mm × 10~20mm, hole density2, the length of side be The ature of coal ceramic honey comb net carrier of 1.5mm square hole is immersed in the ammonia spirit of 26% in batches, spend after ultrasonic cleaning 20min from Sub-water washs;It is washed with deionized after the nitric acid ultrasonic cleaning 20min of 45%;Afterwards with spend after alcohol dipping 10min from Sub-water washs, and dries 3h at 105 DEG C.The photocatalyst powder weighing 54g epoxy resin and 450g again is placed in beaker, Add 9000ml ethanol, under 7000r/min rotating speed, stir 1h with high-speed shearing machine, then by the ature of coal honeybee through pretreatment Nest ceramic network immerse, 15min take out after at 60 DEG C vacuum drying 5h, finally in 500 DEG C, N in batch-type furnace2The lower roasting of protection Burn 2h, i.e. prepare photocatalysis ature of coal ceramic honey comb net.
4, performance detection
(1) intensity of load: the weight-loss ratio of sample is less than 1.5%, shows that photocatalyst load on carrier is stronger.
(2) load factor: the photocatalyst rate on unit mass carrier is 15.0%.
(3) SEM: do not formed uniform films by SEM figure visible light catalytic material surface, but with individual particle or the form of aggregate Exist.
(4) XRD: the TiO in catalyst as seen from the figure2Having 79% is Detitanium-ore-type, and 21% is rutile-type.
(5) measured value of iodine sorption value is 950mg/g.
(6) carbon tetrachloride adsorption rate measured value is 45%.
(7) specific area measuring value is 800m2/g
(8) recording formaldehyde clearance is 97%, and toluene is 93%, and ammonia is 91%.
Embodiment 3
Adulterate TiO according to embodiment 2 step 22The preparation method of photocatalyst is removed and mixes S element, only reservation doping Co, Pr element, remaining step is same as in Example 1, and the measurement result of properties of product is as follows:
(1) intensity of load: the weight-loss ratio of sample is less than 1.5%, shows that photocatalyst load on carrier is stronger.
(2) load factor: the photocatalyst rate on unit mass carrier is 15.0%.
(3) SEM: being schemed from SEM, catalysis material surface does not forms uniform films, but with individual particle or the shape of aggregate Formula exists.
(4) XRD: as seen from the figure, the TiO in catalyst2Having 79% is Detitanium-ore-type, and 21% is rutile-type.
(5) measured value of iodine sorption value is 940mg/g.
(6) carbon tetrachloride adsorption rate measured value is 46%.
(7) specific area measuring value is 804m2/g
(8) formaldehyde clearance is 85%, and toluene is 83%, and ammonia is 79%.
Compareing with embodiment 1 result and show, the clearance that formaldehyde, toluene, ammonia are has decline, and this is due to undoped p S Element influences photocatalyst is to visible absorption, and other performance indications have almost no change.
Embodiment 4
Adulterate TiO according to embodiment 2 step 22The preparation method of photocatalyst is removed and mixes S element, only reservation doping Co, Pr element, remaining step is same as in Example 1, and the measurement result of properties of product is as follows:
(1) intensity of load: the weight-loss ratio of sample is less than 1.5%, shows that photocatalyst load on carrier is stronger.
(2) load factor: the photocatalyst rate on unit mass carrier is 15.0%.
(3) SEM: as seen from the figure, catalysis material surface does not forms uniform films, but deposits with the form of individual particle or aggregate ?.
(4) XRD: as seen from the figure, the TiO in catalyst2Having 79% is Detitanium-ore-type, and 21% is rutile-type.
(5) measured value of iodine sorption value is 940mg/g.
(6) carbon tetrachloride adsorption rate measured value is 46%.
(7) specific area measuring value is 804m2/g
(8) formaldehyde clearance is 82%, and toluene is 79%, and ammonia is 73%.
Compareing with embodiment 1 result and show, the clearance that formaldehyde, toluene, ammonia are has decline, this be due to undoped p Co, On the one hand Pr element have impact on photocatalyst to visible absorption, also affects photocatalysis efficiency, and other performance indications are the most several It is not changed in.

Claims (4)

1. the preparation method of photocatalysis cellular activated carbon net, using Alveolate activated carbon net as carrier, at online load C o of Alveolate activated carbon, the TiO of Pr and S2Photocatalyst, described TiO2In photocatalyst Co: Pr: S: TiO2Mol ratio be 0.01~0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2;The size of Alveolate activated carbon net is 100~250mm × 100~250mm × 10~20mm, and the hole density of net is 30~50 holes/cm2, the length of side that is shaped as in hole is square, triangle or the regular hexagon of 1~2mm;Alveolate activated carbon net is ature of coal Alveolate activated carbon net;
It is characterized in that comprising the following steps: 1) raw material consists of: coal dust: inorganic filler: low temperature bonding agent: high-temperature agglomerant: lubricant: the mass ratio of water is 45~65: 2~15: 1~4: 10~20: 2~3: 10~15, wherein coal dust be bituminous coal with anchracite duff with 1: 0.2~0.8 mixture, inorganic filler is that one or more in Kaolin, attapulgite, Maifanitum or meerschaum arbitrarily mix;Low temperature bonding agent is that one or more in methylcellulose, hydroxypropyl methyl cellulose or carboxymethyl cellulose arbitrarily mix;High-temperature agglomerant is that one or more in coal tar, sodium dihydrogen phosphate or aluminium dihydrogen phosphate arbitrarily mix;The bitumen content of coal tar is more than 35%, and lubricant is edible oil or Polyethylene Glycol;The fineness of all non-aqueous solid materials is all crushed to more than 200 mesh;
2) pretreatment of raw material, including: raw material it is sufficiently mixed and mediates, then through vacuum white silk system with old, making uniform plasticity pug;
3) plasticity pug is extruded into honeycomb ceramics, microwave drying, then carbonization in batch-type furnace under nitrogen protection, is finally passed through steam or carbon dioxide activation, i.e. obtains Alveolate activated carbon net, i.e. ature of coal Alveolate activated carbon net;
Photocatalyst is doping photocatalyst, and its preparation method is as follows: take a certain amount of CH4N2S mortar pulverizes, and the absolute ethyl alcohol and stirring adding 1~2 times of weight is dissolved, and adds the addition of C o (NO3)2·6H2O、Pr(NO3)3·6H2O, stirring, the most slowly dropping butyl titanate Ti (OC4H9)4, stir 0.5-2h, at 60 DEG C, vacuum drying obtains white crystal, calcines 1~2h after ageing 2d at 500 DEG C, and sample is ground to more than 200 mesh again, i.e. obtains Co, Pr, S codope TiO2Photocatalyst finished product;Wherein Co: Pr: S: TiO2Mol ratio is 0.01~0.03: 0.005~0.015: 0.5~2.0: 0.9~1.2;
Photocatalyst in the method for Alveolate activated carbon net is, by prepared powdery photocatalyst on Alveolate activated carbon net carrier, including: first clean Alveolate activated carbon net carrier, be respectively adopted ultrasonic cleaning again after ammonia, nitric acid and soak with ethanol, dry;Then photocatalyst powder is carried on Alveolate activated carbon net carrier, will photocatalyst powder mix with certain proportion with epoxy resin, add ethanol and make serosity, then the Alveolate activated carbon net through pretreatment is impregnated in serosity, take out and dry, finally in 500 ± 100 DEG C, N in batch-type furnace2The lower roasting of protection, i.e. prepares photocatalysis cellular activated carbon net;Control the dipping of Alveolate activated carbon net and dry number of times, the load capacity of photocatalyst can be increased.
2. the preparation method of as claimed in claim 1 photocatalysis cellular activated carbon net, is characterized in that concrete grammar prepared by cellular activated carbon net: 1) wherein coal dust be bituminous coal powder with anchracite duff with 1: 0.2~0.8 mixture;
2) raw material mixing and kneading: 10~30min will be sufficiently stirred in coal dust, inorganic filler and low temperature bonding agent addition blender, the uniform siccative obtained is placed in kneader, sequentially adding high-temperature agglomerant, lubricant and water, stirring is mediated 15~45min, is made uniform plasticity pug;
3) pug practices system with old: added by above-mentioned plasticity pug in vacuum deairing machine, keep more than vacuum-0.06MPa, pump the air in pug, repeat to practice system and make pug mix homogeneously for more than 2 times, stand-by after then pug plastic film wrapped being sealed old 12~48h;
4) extrusion molding: be equipped with on the extrusion shaping machine of cellular steel mould by old good pug, extrudes with the pressure of more than 8MPa, obtains cellular wet idiosome, and cut into charcoal net;
5) being dried: put in microwave dryer by cellular wet idiosome, controlling microwave frequency is 0.8~1.5GHz, is dried 10~30min, obtains the cellular idiosome being dried;
6) carbonization and activation: dry green honeycomb body is put in atmosphere protection batch-type furnace, with nitrogen as protective gas, by for 3~8 DEG C/min ramp to 500~700 DEG C, carbonization 1~3h;Then by 5~10 DEG C/min ramp to 700~900 DEG C, it is passed through steam or carbon dioxide simultaneously, activates 1~5h, obtain Alveolate activated carbon net, and loaded optic catalyst obtains photocatalysis cellular activated carbon net.
The preparation method of photocatalysis cellular activated carbon net the most according to claim 2, it is characterized in that it being first to clean Alveolate activated carbon net carrier: be immersed in the ammonia spirit that mass fraction is 26% by Alveolate activated carbon net carrier, liquid and impurity are removed in ultrasonic cleaning 20min hypsokinesis, are washed with deionized 3 times;Remove liquid and impurity with the nitric acid ultrasonic cleaning 20min hypsokinesis that mass fraction is 45% again, be washed with deionized 3 times, then remove liquid and impurity with the hypsokinesis of alcohol dipping 10min, be washed with deionized 3 times, finally dry 3h at 105 DEG C;
Followed by by photocatalyst on Alveolate activated carbon net carrier: weigh respectively a certain amount of epoxy resin and 5~20g photocatalyst powder be placed in beaker, add 100~400ml ethanol, under 7000r/min rotating speed, 1h is stirred with high-speed shearing machine, then the Alveolate activated carbon net through pretreatment is impregnated in the ethanol serosity of epoxy resin, 15min take out after at 60 DEG C vacuum drying 5h, finally in 500 DEG C, N in batch-type furnace2The lower roasting 2h of protection, i.e. prepares photocatalysis cellular activated carbon net;Control Alveolate activated carbon net dipping in the ethanol serosity of epoxy resin and dry number of times, increasing the load capacity of photocatalyst.
The preparation method of photocatalysis cellular activated carbon net the most according to claim 2, it is characterised in that described cellular steel mould is 20~50 holes/cm2Square or cylinder cellular steel mould.
CN201410830775.1A 2014-12-26 2014-12-26 Photocatalysis cellular activated carbon net Active CN104549370B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410830775.1A CN104549370B (en) 2014-12-26 2014-12-26 Photocatalysis cellular activated carbon net

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410830775.1A CN104549370B (en) 2014-12-26 2014-12-26 Photocatalysis cellular activated carbon net

Publications (2)

Publication Number Publication Date
CN104549370A CN104549370A (en) 2015-04-29
CN104549370B true CN104549370B (en) 2016-09-14

Family

ID=53067075

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410830775.1A Active CN104549370B (en) 2014-12-26 2014-12-26 Photocatalysis cellular activated carbon net

Country Status (1)

Country Link
CN (1) CN104549370B (en)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105481048A (en) * 2015-12-16 2016-04-13 无锡吉进环保科技有限公司 Improved visible light photocatalytic oxidation water treatment reactor
CN106395996A (en) * 2016-08-26 2017-02-15 南京国能环保工程有限公司 Preparation method of micro-electrolysis filler
CN106629719A (en) * 2016-09-21 2017-05-10 广东美的制冷设备有限公司 Preparation technology for activated carbon
CN106994330A (en) * 2017-04-13 2017-08-01 田得君 A kind of preparation method of column-shaped active carbon
CN107126923A (en) * 2017-04-19 2017-09-05 句容市百诚活性炭有限公司 A kind of water resistance cellular activated carbon and preparation method thereof
CN109589972A (en) * 2017-09-30 2019-04-09 江苏瑞丰科技实业有限公司 A kind of oil smoke cleaning material
CN107899421A (en) * 2017-12-13 2018-04-13 深圳市格绿丝纳米科技有限公司 A kind of photocatalysis air-cleaning filter core module processing technology
CN108043221A (en) * 2018-01-24 2018-05-18 合肥工业大学 A kind of photocatalytic active carbon absorption tail gas processing unit and its processing method
CN109046010A (en) * 2018-08-12 2018-12-21 昆山康玛琦环保科技有限公司 Blanket composite cover material preparation method for the control of face source stench
CN109268104B (en) * 2018-09-14 2020-10-13 铜陵市天峰汽车维修服务有限责任公司 Automobile exhaust purifies integrated device
CN109174160B (en) * 2018-10-12 2021-11-30 辽宁大学 g-C3N4Photocatalyst coating and preparation method and application thereof
CN110433770B (en) * 2019-07-17 2022-03-18 天津大学 Photocatalytic honeycomb carbon-based composite material and preparation method thereof
CN111036187B (en) * 2019-12-23 2021-03-30 中国科学院过程工程研究所 Honeycomb carrier and preparation method and application thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1648040A (en) * 2004-12-21 2005-08-03 中国科学院山西煤炭化学研究所 Method for directly preparing honeycomb active carbon from coal

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070265161A1 (en) * 2006-05-11 2007-11-15 Gadkaree Kishor P Activated carbon honeycomb catalyst beds and methods for the manufacture of same

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1648040A (en) * 2004-12-21 2005-08-03 中国科学院山西煤炭化学研究所 Method for directly preparing honeycomb active carbon from coal

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
不同方法制备Fe、S、Ce共掺杂TiO2光催化剂的对比研究;赵来等;《广州化工》;20130430;第41卷(第8期);第1.2.1节 *
活性炭与TiO2相结合去除室内污染物甲醛的实验研究(Ⅰ);鹿院卫等;《太阳能学报》;20080131;第29卷(第1期);第1.2节 *

Also Published As

Publication number Publication date
CN104549370A (en) 2015-04-29

Similar Documents

Publication Publication Date Title
CN104549370B (en) Photocatalysis cellular activated carbon net
CN107029668B (en) A kind of honeycomb type molecular sieve-active carbon compound adsorbent, preparation method and applications
CN106582596A (en) Method for forming fly-ash-based honeycomb type denitration catalyst ceramic carrier
CN102836745B (en) Preparation method for photo-catalysis material with aerogel substrate
WO2017035848A1 (en) Flue gas denitrification catalyst and preparation method thereof
CN102614866B (en) Honeycomb SCR smoke denitration catalyst embryoid body and preparation method thereof
CN102441373A (en) Preparation method of flue gas denitrification catalyst with honeycomb activated carbon as carrier
CN106902812A (en) A kind of preparation method of the loaded catalyst for heterogeneous catalysis ozonisation
CN106824088A (en) A kind of fluffy base optic catalytic cellular activated carbon of Chinese chestnut fruit and its off-gas cleaning equipment
CN103240110A (en) Iron and nitrogen co-doping titanium dioxide/active carbon photocatalyst
CN101791549A (en) Method for preparing formed selective catalytic reduction denitration catalyst by using ultrasonic mixing sedimentation method
CN107573770A (en) A kind of interior wall removes formaldehyde-latex paint and preparation method thereof
CN109569519A (en) The method for preparing active sludge carbon base formaldehyde adsorbent using municipal sludge
CN103240069B (en) Titanium dioxide/active carbon photocatalyst and preparation method and application thereof
CN107754810A (en) A kind of wide temperature smoke denitrating catalyst of non-vanadium base monolithic, preparation method and application
CN113908842B (en) Denitration catalyst for CO-SCR flue gas denitration and preparation method thereof
CN104707588A (en) Modified titanium dioxide/bamboo charcoal composite environment-friendly aerogel and preparation method thereof
CN102772953B (en) Preparation method of compound filtering material loaded with efficient denitrification catalyst
CN113198523A (en) Preparation method of efficient flue gas desulfurization and denitrification catalyst
CN108413419B (en) Microwave catalytic combustion waste gas treatment device and carrier preparation method
CN111514884A (en) Denitration catalyst with honeycomb structure and preparation method thereof
CN113398919B (en) Method for preparing coating type denitration catalyst from municipal sludge
CN109569726A (en) A kind of MOFs/CNT photochemical catalyst and preparation method
CN1511081A (en) Gas absorbing material
CN104707593B (en) The method that integral extruding type Faveolate denitration catalyst is prepared by raw material of metatitanic acid

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant