CN101927158A - Preparation method of nano ZnO/gamma-Al2O3 composite photocatalyst - Google Patents

Preparation method of nano ZnO/gamma-Al2O3 composite photocatalyst Download PDF

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CN101927158A
CN101927158A CN 201010227773 CN201010227773A CN101927158A CN 101927158 A CN101927158 A CN 101927158A CN 201010227773 CN201010227773 CN 201010227773 CN 201010227773 A CN201010227773 A CN 201010227773A CN 101927158 A CN101927158 A CN 101927158A
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CN101927158B (en
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赵永红
康如金
杜志平
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China Daily Chemical Industry Research Institute
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China Daily Chemical Industry Research Institute
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Abstract

A preparation method of a nano ZnO/gamma-Al2O3 composite photocatalyst comprises the following steps: selecting the granules with size of 0.2-0.3mm after grinding gamma-Al2O3 and drying the granules at 110-150 DEG C for 3-6h after washing the granules with deionized water to obtain a gamma-Al2O3 carrier; mixing ZnO, ammonium bicarbonate and ammonia water according to the molar ratio of 1:1-3:1-6, stirring the mixture for 2-8h and taking the supernatant after standing for 1-3h to obtain zinc ammonia liquid; after adding the gamma-Al2O3 carrier to the zinc ammonia liquid according to the mass ratio of ZnO to gamma-Al2O3 carrier being 3:1-9, distilling ammonia at 85-95 DEG C for 4-6h, filtering, washing with water and washing with absolute ethyl alcohol to obtain a precursor; and drying the precursor at 110-150 DEG C for 1-6h and then calcining the precursor at 300-600 DEG C for 2-4h, thus obtaining the nano ZnO/gamma-Al2O3 composite photocatalyst. The preparation method has the advantages of simple process, high ZnO utilization ratio, easy change of load ratio and secure load.

Description

Nano-ZnO/γ-Al 2O 3The preparation method of composite photo-catalyst
Technical field
The invention belongs to a kind of preparation method of catalyst, be specifically related to a kind of nano-ZnO/γ-Al 2O 3The preparation method of composite photo-catalyst.
Background technology
In various environmental pollutions, the most general, main and what have the greatest impact is chemical contamination.Thereby; controlling and administer various chemical pollutants effectively is emphasis in the comprehensive environmental improvement to the destruction that constitutes human survival the most basic water resource, soil and atmospheric environment, and exploitation can be the innoxious practical technique of various chemical pollutants the key of environmental protection.Traditional pollutant processing method exist to some extent or efficient low, can not be thoroughly that pollutant is innoxious, easily produce secondary pollution; Or the scope of application is narrow, only is fit to specific pollutant; Or the energy consumption height, be not suitable for the defective of aspects such as large-scale promotion.
Photocatalysis technology is meant that semiconductor catalyst produces electronics-hole under visible light or action of ultraviolet light, makes to be adsorbed on its surperficial O 2, H 2O and contaminant molecule are accepted light induced electron or hole, thereby a series of redox reaction takes place, make toxic pollutant be degraded to a kind of photochemical method nontoxic or material that toxicity is less, it has that energy consumption is low, oxidability is strong, reaction condition is gentle and characteristics such as non-secondary pollution.Purposes is widely being arranged aspect the toxic pollutant processing.
Early stage researchers mainly are photocatalyst material such as TiO 2, ZnO etc. directly puts in the solution that needs degraded light-catalyzed reaction take place, but the catalyst granules that suspends tiny, be difficult to reclaim and easily cause the catalyst waste, so photocatalyst is become the emphasis of people's research to some carriers.Seeking good carrier and being easy to industrialized preparation method is wherein the most key part.
Summary of the invention
The object of the invention is to provide a kind of technology simple, ZnO utilization rate height, and load factor is easy to change and load nano-ZnO/γ-Al firmly 2O 3The preparation method of composite photo-catalyst.
Nano-ZnO/γ of the present invention-Al 2O 3The preparation method of composite photo-catalyst may further comprise the steps:
(1) with γ-Al 2O 3Choose the particle that particle diameter is 0.2-0.3mm after the grinding, after the deionized water washing, 110 ℃~150 ℃ lower oven dry 3~6 hours, obtain γ-Al 2O 3Carrier;
(2) be 1 in molar ratio with ZnO, carbonic hydroammonium and ammoniacal liquor under the room temperature: (1~3): the ratio of (1~6) is mixed, and stirs 2~8 hours, leaves standstill after 1~3 hour and gets supernatant liquor, obtains the zinc ammoniacal liquor;
(3) press ZnO and γ-Al 2O 3The carrier mass ratio is 3: the ratio of (1~9), and with γ-Al 2O 3After carrier joined the zinc ammoniacal liquor, 85~95 ℃ of lower ammonia still processs 4~6 hours, filtration, washing, absolute ethanol washing obtained predecessor;
(4) predecessor was dried 1~6 hour under 110~150 ℃, namely obtained nano-ZnO/γ-Al in 2~4 hours in 300~600 ℃ of lower calcinings again 2O 3Composite photo-catalyst.
Nano-ZnO/γ of the present invention-Al 2O 3The preparation method of composite photo-catalyst has following features:
(1) solved the difficult recovery of floating type catalyst and easily caused the shortcoming of catalyst waste, and can be recycled, catalytic efficiency is still very high.
(2) γ-Al 2O 3Carrier is strong to the absorption of ZnO, the firm difficult drop-off of load.
(3) the ZnO particle diameter of load is still nanoscale, the catalytic efficiency height.
(4) this preparation method's cost of material is cheap, and ZnO utilization rate (amount of load accounts for the ratio of growing amount) is high, process is simple, and the cycle weak point is easy to industrialization.
Description of drawings
Fig. 1 is γ-Al 2O 3The ESEM of carrier (SEM) picture.
Fig. 2 is ESEM (SEM) picture of embodiment 1.
The ESEM of Fig. 3 embodiment 2 (SEM) picture
The ESEM of Fig. 4 embodiment 3 (SEM) picture
The specific embodiment
Specify the present invention below in conjunction with example
Embodiment 1
With γ-Al 2O 3Choose the particle that diameter is 0.2~0.3mm after the grinding, be placed in the baking oven through the deionized water washing and under 110 ℃, dried 6 hours, obtain γ-Al 2O 3Carrier, Fig. 1 are its sem photographs.Be that 1: 1: 6 ratio joins 10g ZnO, 9.7g carbonic hydroammonium and 56.4ml ammoniacal liquor in the there-necked flask in ZnO, carbonic hydroammonium and ammoniacal liquor mol ratio under the room temperature, stirred 2 hours, leave standstill after 1 hour and get supernatant liquor, obtain the zinc ammoniacal liquor; Press ZnO and γ-Al 2O 3The carrier mass ratio is that 3: 1 ratio is got 9.8ml zinc ammoniacal liquor and 0.5g γ-Al 2O 3Carrier, 95 ℃ of lower ammonia still processs 4 hours, filtration, washing, absolute ethanol washing obtained predecessor.The gained predecessor is put into baking oven in 110 ℃ of lower oven dry 6 hours, and the product after will dry is again put into Muffle furnace in 300 ℃ of lower calcinings 4 hours, namely gets mass ratio and be the nano-ZnO/γ of 3: 1 (load factor is 58%)-Al 2O 3Composite photo-catalyst, the particle diameter that calculates institute's loading ZnO according to the scherrer formula is 7.4nm.Fig. 2 is the sem photograph of gained catalyst.
Embodiment 2
With γ-Al 2O 3Choose the particle that diameter is 0.2~0.3mm after the grinding, be placed in the baking oven through the deionized water washing and under 130 ℃, dried 3 hours, obtain γ-Al 2O 3Carrier, Fig. 1 are its sem photographs.Be that 1: 3: 1 ratio joins 10g ZnO, 29.1g carbonic hydroammonium and 9.4ml ammoniacal liquor in the there-necked flask in ZnO, carbonic hydroammonium and ammoniacal liquor mol ratio under the room temperature, stirred 4 hours, leave standstill after 2 hours and get supernatant liquor, obtain the zinc ammoniacal liquor; Press ZnO and γ-Al 2O 3The carrier mass ratio is that 2: 1 ratio is got 6.3ml zinc ammoniacal liquor and 0.5g γ-Al 2O 3Carrier, 90 ℃ of lower ammonia still processs 5 hours, filtration, washing, absolute ethanol washing obtained predecessor.The gained predecessor is put into baking oven in 120 ℃ of lower oven dry 4 hours, and the product after will dry is again put into Muffle furnace in 400 ℃ of lower calcinings 3 hours, namely gets mass ratio and be the nano-ZnO/γ of 2: 1 (load factor is 57%)-Al 2O 3Composite photo-catalyst, the particle diameter that calculates institute's loading ZnO according to the scherrer formula is gained catalyst sem photograph for 6.8nm Fig. 3.
Embodiment 3
With γ-Al 2O 3Choose the particle that diameter is 0.2~0.3mm after the grinding, be placed in the baking oven through the deionized water washing and under 150 ℃, dried 3 hours, obtain γ-Al 2O 3Carrier, Fig. 1 are its sem photographs.Be that 1: 2: 3 ratio joins 10g ZnO, 19.4g carbonic hydroammonium and 28.2ml ammoniacal liquor in the there-necked flask in ZnO, carbonic hydroammonium and ammoniacal liquor mol ratio under the room temperature, stirred 8 hours, leave standstill after 3 hours and get supernatant liquor, obtain the zinc ammoniacal liquor; Press ZnO and γ-Al 2O 3The carrier mass ratio is that 1: 3 ratio is got 3ml zinc ammoniacal liquor and 0.5g γ-Al 2O 3Carrier, 85 ℃ of lower ammonia still processs 6 hours, filtration, washing, absolute ethanol washing obtained predecessor.The gained predecessor is put into baking oven in 150 ℃ of lower oven dry 1 hour, and the product after will dry is again put into Muffle furnace in 600 ℃ of lower calcinings 2 hours, namely gets mass ratio and be the nano-ZnO/γ of 1: 3 (load factor is 20%)-Al 2O 3Composite photo-catalyst, the particle diameter that calculates institute's loading ZnO according to the scherrer formula is 10.2nm.Fig. 4 is a gained catalyst sem photograph.

Claims (1)

1. nano-ZnO/γ-Al 2O 3The preparation method of composite photo-catalyst is characterized in that comprising the steps:
(1) with γ-Al 2O 3Choose the particle that particle diameter is 0.2-0.3mm after the grinding, after the deionized water washing, 110 ℃~150 ℃ lower oven dry 3~6 hours, obtain γ-Al 2O 3Carrier;
(2) under the room temperature be that 1: 1~3: 1~6 ratio is mixed in molar ratio, stirred 2~8 hours, leave standstill after 1~3 hour and get supernatant liquor, obtain the zinc ammoniacal liquor ZnO, carbonic hydroammonium and ammoniacal liquor;
(3) press ZnO and γ-Al 2O 3The carrier mass ratio is 3: 1~9 ratio, with γ-Al 2O 3After carrier joined the zinc ammoniacal liquor, 85~95 ℃ of lower ammonia still processs 4~6 hours, filtration, washing, absolute ethanol washing obtained predecessor;
(4) predecessor was dried 1~6 hour under 110~150 ℃, namely obtained nano-ZnO/γ-Al in 2~4 hours in 300~600 ℃ of lower calcinings again 2O 3Composite photo-catalyst.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102515252A (en) * 2011-12-28 2012-06-27 韶关凯鸿纳米材料有限公司 Film-coating production technology for nano zinc oxide
CN102513083A (en) * 2011-12-13 2012-06-27 吉林省兰舍硅藻新材料有限公司 Preparation method of diatomite loaded nano-zinc oxide composite powder material
CN108855037A (en) * 2018-07-19 2018-11-23 刘青 A kind of preparation method of alumina-silica zinc composite catalyzing material
CN109110793A (en) * 2018-03-22 2019-01-01 云南大学 A kind of preparation method of alumina load nano-cerium oxide compound gold and ru oxide
CN111729664A (en) * 2020-06-05 2020-10-02 吉林大学 Supported nano zinc oxide and preparation and application thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108031431B (en) * 2017-12-26 2021-04-27 大连全净科技有限公司 Surface modified composite active Al2O3Preparation method of (E) -ZnO carrier spherical particles

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JP2004136223A (en) * 2002-10-18 2004-05-13 Mitsubishi Gas Chem Co Inc Catalyst for dimethyl ether reformation and production method for hydrogen-containing gas using the catalyst
CN1660490A (en) * 2004-12-21 2005-08-31 中国科学院广州能源研究所 Preparation method of synthesizing catalyst of methyl alcohol
CN1876619A (en) * 2006-07-04 2006-12-13 浙江大学 Method for preparing benzaldehyde by catalytic reduction of composite oxide

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JPH09192490A (en) * 1996-01-25 1997-07-29 Nissan Motor Co Ltd Material for exhaust gas purifying catalyst and its production
CN1350883A (en) * 2000-10-27 2002-05-29 南化集团研究院 Copper-series catalyst for CD conversion and its preparing process
JP2004136223A (en) * 2002-10-18 2004-05-13 Mitsubishi Gas Chem Co Inc Catalyst for dimethyl ether reformation and production method for hydrogen-containing gas using the catalyst
CN1660490A (en) * 2004-12-21 2005-08-31 中国科学院广州能源研究所 Preparation method of synthesizing catalyst of methyl alcohol
CN1876619A (en) * 2006-07-04 2006-12-13 浙江大学 Method for preparing benzaldehyde by catalytic reduction of composite oxide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102513083A (en) * 2011-12-13 2012-06-27 吉林省兰舍硅藻新材料有限公司 Preparation method of diatomite loaded nano-zinc oxide composite powder material
CN102515252A (en) * 2011-12-28 2012-06-27 韶关凯鸿纳米材料有限公司 Film-coating production technology for nano zinc oxide
CN102515252B (en) * 2011-12-28 2013-06-05 韶关凯鸿纳米材料有限公司 Film-coating production technology for nano zinc oxide
CN109110793A (en) * 2018-03-22 2019-01-01 云南大学 A kind of preparation method of alumina load nano-cerium oxide compound gold and ru oxide
CN108855037A (en) * 2018-07-19 2018-11-23 刘青 A kind of preparation method of alumina-silica zinc composite catalyzing material
CN111729664A (en) * 2020-06-05 2020-10-02 吉林大学 Supported nano zinc oxide and preparation and application thereof
CN111729664B (en) * 2020-06-05 2022-11-11 吉林大学 Supported nano zinc oxide and preparation and application thereof

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