JP3227373B2 - Air purification paint using photocatalyst - Google Patents
Air purification paint using photocatalystInfo
- Publication number
- JP3227373B2 JP3227373B2 JP06080096A JP6080096A JP3227373B2 JP 3227373 B2 JP3227373 B2 JP 3227373B2 JP 06080096 A JP06080096 A JP 06080096A JP 6080096 A JP6080096 A JP 6080096A JP 3227373 B2 JP3227373 B2 JP 3227373B2
- Authority
- JP
- Japan
- Prior art keywords
- photocatalyst
- synthetic zeolite
- paint
- air purification
- type
- 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.)
- Expired - Fee Related
Links
- 239000011941 photocatalyst Substances 0.000 title claims description 21
- 239000003973 paint Substances 0.000 title claims description 13
- 238000004887 air purification Methods 0.000 title claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 50
- 239000000377 silicon dioxide Substances 0.000 claims description 24
- 229910021536 Zeolite Inorganic materials 0.000 claims description 20
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 20
- 239000010457 zeolite Substances 0.000 claims description 20
- 239000003463 adsorbent Substances 0.000 claims description 11
- 239000011230 binding agent Substances 0.000 claims description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 9
- 238000005342 ion exchange Methods 0.000 claims description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 8
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 6
- -1 palladium ions Chemical class 0.000 claims description 6
- 239000008119 colloidal silica Substances 0.000 claims description 5
- 150000002500 ions Chemical class 0.000 claims description 5
- 239000010445 mica Substances 0.000 claims description 5
- 229910052618 mica group Inorganic materials 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims description 4
- 238000000576 coating method Methods 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 229910052763 palladium Inorganic materials 0.000 claims description 4
- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 229910052709 silver Inorganic materials 0.000 claims description 4
- 239000004332 silver Substances 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 34
- 238000001179 sorption measurement Methods 0.000 description 23
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 235000019645 odor Nutrition 0.000 description 9
- 238000000746 purification Methods 0.000 description 9
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 230000001877 deodorizing effect Effects 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 4
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical group [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- 229910001431 copper ion Inorganic materials 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000004332 deodorization Methods 0.000 description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000005745 Captan Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229940117949 captan Drugs 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- MUJIDPITZJWBSW-UHFFFAOYSA-N palladium(2+) Chemical group [Pd+2] MUJIDPITZJWBSW-UHFFFAOYSA-N 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
- Paints Or Removers (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Catalysts (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は光触媒を用いた空気
浄化塗料に関するものである。The present invention relates to an air purification paint using a photocatalyst.
【0002】[0002]
【従来の技術】空気の浄化物としては、一般的には活性
炭が知られている。活性炭は多数の細孔を有しており、
その細孔内に臭気等の汚れ成分を吸着させて空気を浄化
するものである。2. Description of the Related Art Activated carbon is generally known as an air purifier. Activated carbon has many pores,
It purifies air by adsorbing odor and other dirt components into the pores.
【0003】また、特開平5−293165号公報に
は、活性炭と光触媒を複合化したものが提案されてい
る。これは、活性炭の表面に光触媒を担持させることに
より、紫外線ランプ等を用いて光触媒を励起させ、活性
炭を再生させるとともに、臭気成分を分解するようにし
たものである。Further, Japanese Patent Application Laid-Open No. 5-293165 proposes a composite of activated carbon and a photocatalyst. In this method, a photocatalyst is supported on the surface of activated carbon to excite the photocatalyst using an ultraviolet lamp or the like, thereby regenerating the activated carbon and decomposing odor components.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上述し
た従来の空気浄化物のうち、前者の活性炭単独のものの
場合には、臭気を吸着するうちに吸着量が飽和状態に達
し、浄化性能が無くなってきて、いずれ交換しなければ
ならなくなるという問題がある。However, in the case of the former activated carbon alone among the above-mentioned conventional air purification products, the adsorption amount reaches a saturated state while adsorbing the odor, and the purification performance is lost. Therefore, there is a problem that it will eventually be necessary to replace it.
【0005】一方、後者の活性炭と光触媒を複合したも
のの場合においては、脱臭性能は活性炭の吸着性能によ
って決まり、活性炭で吸着困難なアンモニア、硫化水
素、アセトアルデヒド等の浄化性能が良くないという問
題がある。また、高湿度雰囲気下では吸湿して脱臭性能
が低下してしまうという問題がある。さらに、光触媒と
活性炭は塗料化できないため、光触媒はハニカム状等に
成形した活性炭に焼き付けられるが、焼き付け条件によ
っては活性炭が発火するという問題や、光触媒による活
性炭の分解が起こり得るという問題もある。On the other hand, in the latter case where activated carbon and photocatalyst are combined, there is a problem that the deodorizing performance is determined by the adsorption performance of activated carbon, and the purification performance of ammonia, hydrogen sulfide, acetaldehyde, etc., which is difficult to adsorb with activated carbon, is poor. . In addition, there is a problem that in a high-humidity atmosphere, moisture is absorbed and deodorization performance is reduced. Further, since the photocatalyst and the activated carbon cannot be formed into a paint, the photocatalyst is baked on activated carbon formed into a honeycomb shape or the like.
【0006】本発明は、上記のような問題点を解決する
ためになされたもので、その目的は、紫外線の照射によ
って浄化性能を再生することができ、高湿度雰囲気下で
も十分な浄化性能を有し、紫外線に対して安定してお
り、かつ発火の危険性がない空気浄化塗料を提供するこ
とにある。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to regenerate the purification performance by irradiating ultraviolet rays, and to achieve a sufficient purification performance even in a high humidity atmosphere. It is an object of the present invention to provide an air purifying paint which has a stable property against ultraviolet rays and has no danger of ignition.
【0007】また、本発明の他の目的は、どのような種
類の臭気成分も吸着可能な空気浄化塗料を提供すること
にある。It is another object of the present invention to provide an air purifying paint capable of adsorbing any kind of odorous component.
【0008】[0008]
【課題を解決するための手段】上記目的を達成するため
に、本発明は、光触媒と吸着剤をバインダーを用いて塗
料化した空気浄化塗料であって、前記吸着剤としてシリ
カ/アルミナ比が56以上92以下のハイシリカ合成ゼ
オライトH型ZSM5を用い、皮膜形成時における光触
媒の配合比率を15重量%以上とし、前記バインダーと
してコロイダルシリカを主成分とするものを用いたこと
を特徴とするものである。In order to achieve the above object, the present invention provides an air purifying paint comprising a photocatalyst and an adsorbent formed by using a binder, wherein the adsorbent has a silica / alumina ratio of 56. with high silica synthetic zeolite H-type ZSM5 of 92 inclusive, touch light during film formation
The mixing ratio of the medium is 15% by weight or more, and the binder and
And a material containing colloidal silica as a main component .
【0009】本発明の空気浄化塗料を各種材料のシート
またはハニカム等の通気性担体または容器壁等に塗布
し、乾燥・焼き付けを行って空気浄化皮膜を形成させる
と、この皮膜付近を通過する空気の臭気成分が皮膜に吸
着されて空気が浄化される。吸着された臭気成分は紫外
線照射によって分解され、これによって塗料の浄化性能
が再生される。本発明の空気浄化塗料は、吸着剤が疎水
性であるため、高湿度雰囲気下でも吸湿による浄化性能
の低下が少ない。また、吸着剤が活性炭よりも化学的に
安定しており、光触媒で分解されることがなく、発火す
る危険性もない。The air-purifying paint of the present invention is applied to a sheet of various materials, a gas-permeable carrier such as a honeycomb, or a container wall, and dried and baked to form an air-purifying film. The odor component is adsorbed on the film to purify the air. The adsorbed odor component is decomposed by ultraviolet irradiation, thereby regenerating the purification performance of the paint. In the air purification paint of the present invention, since the adsorbent is hydrophobic, there is little deterioration in purification performance due to moisture absorption even in a high humidity atmosphere. In addition, the adsorbent is more chemically stable than activated carbon, does not decompose with a photocatalyst, and has no danger of ignition.
【0010】なお、どのような臭気成分も吸着可能にす
るために、前記ハイシリカ合成ゼオライトH型ZSM5
は、中心イオンである水素イオンが銅または銀または白
金またはパラジウムのイオンでイオン交換されたハイシ
リカ合成ゼオライトH型ZSM5を一種類以上含むこと
が好ましい。In order to make any odorous component adsorbable, the high silica synthetic zeolite H type ZSM5 is used.
Preferably contains one or more types of high-silica synthetic zeolite H-type ZSM5 in which hydrogen ions as central ions are ion-exchanged with copper, silver, platinum or palladium ions.
【0011】また、前記ハイシリカ合成ゼオライトH型
ZSM5のイオン交換率を前記ハイシリカ合成ゼオライ
トH型ZSM5全体の1重量%以上にすると、活性炭以
上の浄化性能が得られるようになる。Further, when the ion exchange rate of the high silica synthetic zeolite H-type ZSM5 is 1% by weight or more of the whole high silica synthetic zeolite H-ZSM5, a purification performance higher than that of activated carbon can be obtained.
【0012】また、前記バインダーを、マイカを8重量
%以上含むものにすると、皮膜がひび割れしにくくな
り、厚く塗布することができるため、単位面積当りの吸
着量を多くすることができる。When the binder contains mica in an amount of 8% by weight or more, the film is less likely to crack and can be applied thickly, so that the amount of adsorption per unit area can be increased.
【0013】[0013]
【発明の実施の形態】以下、本発明の具体的な実施形態
を図面を参照しながら説明する。疎水性合成ゼオライト
であるH型ZSM5を用いてシリカ/アルミナ比が5
6、92、430となるように粉を作成し、この粉4g
について27リットルの密閉ボックス内で清浄空気をパ
ージした後、蒸留水を蒸発させて95%RH以上の高湿
度雰囲気とし、中にアンモニアを蒸発させて100pp
mの初期濃度とし、通風して粉を循環させ、濃度の変化
をガスセンサーにて測定することによりこれらの吸着性
能を測定した。図1がその結果を示すグラフである。シ
リカ/アルミナ比が高いほど疎水性が向上するとされて
いるが、430では逆に吸着性能が低下しており、シリ
カ/アルミナ比は92以下で良い。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, specific embodiments of the present invention will be described with reference to the drawings. Using a hydrophobic synthetic zeolite, H-type ZSM5, silica / alumina ratio of 5
6, 92, 430 powder was prepared, 4g of this powder
After purging clean air in a 27-liter closed box, distilled water is evaporated to a high humidity atmosphere of 95% RH or more, and ammonia is evaporated therein to 100 pp.
The adsorbing performance was measured by setting the initial concentration of m, circulating the powder through ventilation, and measuring the change in concentration with a gas sensor. FIG. 1 is a graph showing the results. It is said that the higher the silica / alumina ratio, the higher the hydrophobicity. However, in the case of 430, the adsorption performance is reduced, and the silica / alumina ratio may be 92 or less.
【0014】さらに、シリカ/アルミナ比が90の合成
ゼオライトH型ZSM5を用い、この中心イオンの水素
イオンを粉の重量比で1%を白金、パラジウム、銅、銀
等のイオンでイオン交換させた。これらの各種臭気成分
に対する吸着性能を見るために同上の方法により乾燥雰
囲気のなかで各種ガスを発生させて、吸着性能を測定し
た。図2はアンモニア(初期濃度170ppm)、図3
はトリメチルアミン(初期濃度90ppm)、図4は硫
化水素、図5はエチルメルカプタン(初期濃度80pp
m)、図6は硫化メチル(初期濃度100ppm)、図
7は酢酸(初期濃度140ppm)、図8はアセトアル
デヒド(初期濃度65ppm)、図9はエチレン(初期
濃度1400ppm)に対するものである。なお、各図
において、ブランクとは、密閉ボックス内に吸着剤を入
れないときのガスセンサー値である。Further, using a synthetic zeolite H-type ZSM5 having a silica / alumina ratio of 90, hydrogen ions of the central ion were ion-exchanged with 1% by weight of powder with ions of platinum, palladium, copper, silver and the like. . In order to check the adsorption performance for these various odor components, various gases were generated in a dry atmosphere by the same method as above, and the adsorption performance was measured. FIG. 2 shows ammonia (initial concentration 170 ppm), FIG.
Is trimethylamine (90 ppm initial concentration), FIG. 4 is hydrogen sulfide, and FIG. 5 is ethyl mercaptan (80 ppm initial concentration).
m), FIG. 6 for methyl sulfide (initial concentration 100 ppm), FIG. 7 for acetic acid (initial concentration 140 ppm), FIG. 8 for acetaldehyde (initial concentration 65 ppm), and FIG. 9 for ethylene (initial concentration 1400 ppm). In addition, in each figure, a blank is a gas sensor value when an adsorbent is not put in a closed box.
【0015】これらのグラフより、銅イオン交換ZSM
5、パラジウムイオン交換ZSM5は大抵の臭気に対し
て吸着性能が優れていることがわかる。なお、イオン交
換率を重量比で1%以上にすれば、吸着性能がいずれの
臭気に対しても活性炭と同等またはこれを凌賀するよう
になる。図5において、銅イオン交換ZSM5の重量比
を0.5%から1%にすると、吸着性能が向上して活性
炭とほぼ同等になることが判る。From these graphs, it can be seen that copper ion exchange ZSM
5. It can be seen that palladium ion exchange ZSM5 has excellent adsorption performance against most odors. If the ion exchange rate is 1% or more by weight, the adsorption performance is equal to or exceeds that of activated carbon for any odor. In FIG. 5, it can be seen that when the weight ratio of the copper ion exchange ZSM5 is changed from 0.5% to 1%, the adsorption performance is improved and becomes almost equivalent to activated carbon.
【0016】光触媒として石原作業株式会社製の酸化チ
タンST−01(商品名)を用い、吸着剤として、シリ
カ/アルミナ比が90で、1重量%を銅イオン交換した
ハイシリカ合成ゼオライトH型ZSM5を用い、バイン
ダーとしてテルニック工業株式会社製のコロイダルシリ
カ系バインダーベタック970GD(商品名)を用い
て、これらの配合比を種々変更して、60×80(m
m)のガラス基材板の片面に、いずれも12(mg/c
m2)となるように塗布し、380℃で1時間焼き付け
を行ってサンプルを作成した。Titanium oxide ST-01 (trade name, manufactured by Ishihara Works Co., Ltd.) was used as a photocatalyst, and high silica synthetic zeolite H type ZSM5 having a silica / alumina ratio of 90 and 1% by weight of copper ion exchanged was used as an adsorbent. Using a colloidal silica-based binder Bettac 970GD (trade name) manufactured by Telnic Industry Co., Ltd. as a binder, these compounding ratios were variously changed, and 60 × 80 (m
m) on one side of the glass substrate plate, 12 (mg / c
m 2 ) and baked at 380 ° C. for 1 hour to prepare a sample.
【0017】このサンプル4枚ずつを27リットルのボ
ックス内に設置し、乾燥した清浄空気をパージした後、
アセトアルデヒドを注入して初期濃度100ppmと
し、送風して循環させながら6Wブラックライト1本の
照射がある場合とない場合についてガスセンサーにより
脱臭性能を測定した。その結果が図10である。吸着量
が飽和するまでは、光触媒だけよりも光触媒とゼオライ
トを混合した方が脱臭速度は速い。また、吸着飽和後の
脱臭性能において、皮膜形成時における光触媒の配合重
量比が15%より少ないと、分解速度が極端に遅くな
り、十分な脱臭性能が得られない。15%以上であれ
ば、吸着飽和後においても分解しており、十分な脱臭性
能は得られる。Each of the four samples was placed in a 27-liter box and purged with dry clean air.
Acetaldehyde was injected to give an initial concentration of 100 ppm, and the air sensor was used to measure the deodorization performance with and without irradiation of a single 6 W black light while circulating by blowing air. FIG. 10 shows the result. Until the adsorption amount is saturated, the deodorizing speed is higher when the photocatalyst and the zeolite are mixed than when the photocatalyst alone is used. Further, in the deodorizing performance after the adsorption saturation, if the blending weight ratio of the photocatalyst at the time of film formation is less than 15%, the decomposition rate becomes extremely slow, and sufficient deodorizing performance cannot be obtained. If it is 15% or more, it is decomposed even after adsorption saturation, and sufficient deodorizing performance can be obtained.
【0018】なお、用いたバインダーの中にはマイカ粉
を添加しているが、このマイカの添加量がバインダー重
量に対して8%以下であれば焼き付け後にひび割れが生
じるが、8%以上であれば12(mg/cm2)以上に
厚く塗布してもひび割れしにくい結果となった。Although mica powder is added to the binder used, cracking occurs after baking if the amount of mica added is 8% or less based on the weight of the binder. For example, even when applied as thick as 12 (mg / cm 2 ) or more, the result was that cracking was difficult.
【0019】バインダー成分としてコロイダルシリカを
主成分とするものの代わりにシリコン樹脂、フッ素樹
脂、リン酸アルミニウムを主成分とするものを用いて同
様に塗料化したが、本発明のものと比べて十分な脱臭性
能が得られず、塗布量も12(mg/cm2)以上厚く
塗ることができなかった。[0019] Instead of the binder component containing colloidal silica as a main component, a coating material was similarly formed using a resin component containing a silicon resin, a fluororesin, or aluminum phosphate as a main component. No deodorizing performance was obtained, and the coating amount could not be as thick as 12 (mg / cm 2 ) or more.
【0020】[0020]
【発明の効果】以上説明したように、本発明によれば、
吸着剤としてシリカ/アルミナ比が56以上92以下の
ハイシリカ合成ゼオライトH型ZSM5を用いたことに
より、吸着剤が疎水性であるため高湿度雰囲気でも浄化
性能の低下が少ない。また、ハイシリカ合成ゼオライト
H型ZSM5は活性炭よりも化学的に安定しており、光
触媒で分解されることがなく、発火する危険性もない。
また、塗料化したことにより、使用時の自由度が高く、
非常に扱い易い。さらに、皮膜形成時における前記光触
媒の配合比率を15重量%以上にしたことにより、市販
のブラックライトでも十分な再生能力が得られるように
なり、再生効率が十分なものとなる。加えて、前記バイ
ンダーをコロイダルシリカを主成分とするものにしたこ
とにより、紫外線がバインダーを透過しやすくなり、光
触媒に紫外線が吸収されやすくなるとともに、多孔質で
あるため、皮膜を厚くしても紫外線が内部まで浸透する
ようになる。 As described above, according to the present invention,
By using high silica synthetic zeolite H-type ZSM5 having a silica / alumina ratio of 56 or more and 92 or less as the adsorbent, the adsorbent is hydrophobic, so that the purification performance is less reduced even in a high humidity atmosphere. In addition, the high silica synthetic zeolite H-type ZSM5 is more chemically stable than activated carbon, does not decompose with a photocatalyst, and has no danger of ignition.
In addition, by using paint, the degree of freedom during use is high,
Very easy to handle. Further, when the film is formed,
By increasing the mixing ratio of the medium to 15% by weight or more,
To be able to obtain sufficient playback ability even with black light
And the regeneration efficiency becomes sufficient. In addition,
The main component is colloidal silica.
This makes it easier for ultraviolet light to pass through the binder,
Ultraviolet light is easily absorbed by the catalyst, and it is porous.
UV light penetrates into the interior even if the coating is thick
Become like
【0021】請求項2によるときは、ハイシリカ合成ゼ
オライトH型ZSM5を、中心イオンである水素イオン
が銅または銀または白金またはパラジウムのイオンでイ
オン交換されたハイシリカ合成ゼオライトH型ZSM5
を一種類以上含むものにしたことにより、どのような種
類の臭気成分も吸着可能であり、かつ吸着量も多い。According to the second aspect, the high-silica synthetic zeolite H-type ZSM5 is used as the high-silica synthetic zeolite H-type ZSM5 in which the hydrogen ion as the central ion is ion-exchanged with copper, silver, platinum or palladium.
By including at least one of these, any type of odor component can be adsorbed and the amount of adsorption is large.
【0022】請求項3によるときは、合成ゼオライトの
イオン交換率を合成ゼオライト全体の1重量%以上にし
たことにより、活性炭以上の浄化性能が得られる。According to the third aspect, by setting the ion exchange rate of the synthetic zeolite to 1% by weight or more of the whole synthetic zeolite, a purification performance higher than that of activated carbon can be obtained.
【図1】 シリカ/アルミナ比の違いによる高湿状態で
のアンモニアの吸着性能の違いを比較したグラフ。FIG. 1 is a graph comparing differences in ammonia adsorption performance in a high humidity state due to differences in silica / alumina ratio.
【図2】 乾燥状態でのアンモニアの吸着性能を比較し
たグラフ。FIG. 2 is a graph comparing the adsorption performance of ammonia in a dry state.
【図3】 乾燥状態でのトリメチルアミンの吸着性能を
比較したグラフ。FIG. 3 is a graph comparing the adsorption performance of trimethylamine in a dry state.
【図4】 乾燥状態での硫化水素の吸着性能を比較した
グラフ。FIG. 4 is a graph comparing the adsorption performance of hydrogen sulfide in a dry state.
【図5】 乾燥状態でのエチルメチレンカプタンの吸着
性能を比較したグラフ。FIG. 5 is a graph comparing the adsorption performance of ethyl methylene captan in a dry state.
【図6】 乾燥状態での硫化メチルの吸着性能を比較し
たグラフ。FIG. 6 is a graph comparing the adsorption performance of methyl sulfide in a dry state.
【図7】 乾燥状態での酢酸の吸着性能を比較したグラ
フ。FIG. 7 is a graph comparing the adsorption performance of acetic acid in a dry state.
【図8】 乾燥状態でのアセトアルデヒドの吸着性能を
比較したグラフ。FIG. 8 is a graph comparing the adsorption performance of acetaldehyde in a dry state.
【図9】 乾燥状態でのエチレンの吸着性能を比較した
グラフ。FIG. 9 is a graph comparing ethylene adsorption performance in a dry state.
【図10】 光触媒と吸着剤の配合比の違いと紫外線照
射の有無によるアセトアルデヒドの吸着性能の違いを比
較したグラフ。FIG. 10 is a graph comparing the difference in the mixing ratio between the photocatalyst and the adsorbent and the difference in the acetaldehyde adsorption performance depending on the presence or absence of ultraviolet irradiation.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI B01J 35/02 C09C 3/00 C01B 39/38 B01D 53/36 J C09C 3/00 ZABH ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification code FI B01J 35/02 C09C 3/00 C01B 39/38 B01D 53/36 J C09C 3/00 ZABH
Claims (3)
料化した空気浄化塗料であって、 前記吸着剤としてシリカ/アルミナ比が56以上92以
下のハイシリカ合成ゼオライトH型ZSM5を用い、皮
膜形成時における光触媒の配合比率を少なくとも15重
量%とし、前記バインダーとしてコロイダルシリカ及び
マイカよりなり、皮膜形成時におけるマイカの配合比率
を少なくとも8%としたことを特徴とする光触媒を用い
た空気浄化塗料。1. An air purification coating material formed by using a photocatalyst, an adsorbent, and a binder, wherein a high silica synthetic zeolite H-type ZSM5 having a silica / alumina ratio of 56 to 92 is used as the adsorbent. The blending ratio of the photocatalyst is at least 15 % by weight, and as the binder, colloidal silica and
Made of mica, mix ratio of mica during film formation
Air purification paint using a photocatalyst, characterized in that the content is at least 8% .
M5は、中心イオンである水素イオンを銅または銀また
は白金またはパラジウムのイオンでイオン交換したハイ
シリカ合成ゼオライトH型ZSM5を一種類以上含むこ
とを特徴とする請求項1に記載の光触媒を用いた空気浄
化塗料。2. The high silica synthetic zeolite H-type ZS.
The air using a photocatalyst according to claim 1, wherein M5 contains at least one kind of high silica synthetic zeolite H-type ZSM5 obtained by ion-exchanging a hydrogen ion as a central ion with copper, silver, platinum, or palladium ions. Purifying paint.
M5のイオン交換率は、前記ハイシリカ合成ゼオライト
H型ZSM5全体の1重量%以上であることを特徴とす
る請求項2に記載の光触媒を用いた空気浄化塗料。3. The high silica synthetic zeolite H type ZS.
The air purification paint using a photocatalyst according to claim 2, wherein the ion exchange rate of M5 is 1% by weight or more of the whole high silica synthetic zeolite H-type ZSM5.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06080096A JP3227373B2 (en) | 1996-03-18 | 1996-03-18 | Air purification paint using photocatalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06080096A JP3227373B2 (en) | 1996-03-18 | 1996-03-18 | Air purification paint using photocatalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09249824A JPH09249824A (en) | 1997-09-22 |
JP3227373B2 true JP3227373B2 (en) | 2001-11-12 |
Family
ID=13152770
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP06080096A Expired - Fee Related JP3227373B2 (en) | 1996-03-18 | 1996-03-18 | Air purification paint using photocatalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3227373B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101499028B1 (en) * | 2013-09-27 | 2015-03-09 | 한국생산기술연구원 | Adsorbent coating solution containing two binder and a method of manufacturing the same |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010030773A (en) * | 1998-07-29 | 2001-04-16 | 이시하라 겐조 | Road provided with air cleaning function and method of cleaning polluted air on road |
JP4513141B2 (en) * | 1999-06-21 | 2010-07-28 | パナソニック株式会社 | air purifier |
JP2001321425A (en) * | 2000-05-17 | 2001-11-20 | Osaka Prefecture | Adsorbent and adsorbing material for volatile organic compound or the like |
JP2006297351A (en) * | 2005-04-25 | 2006-11-02 | Showa Denko Kk | Photocatalyst film and manufacturing method |
JP2006297350A (en) * | 2005-04-25 | 2006-11-02 | Showa Denko Kk | Photocatalyst film and manufacturing method |
GB0522229D0 (en) | 2005-11-01 | 2005-12-07 | Johnson Matthey Plc | Adsorption of volatile organic compounds derived from organic matter |
JP4924184B2 (en) * | 2007-04-27 | 2012-04-25 | パナソニック株式会社 | Photocatalytic member and air purification device using the photocatalytic member |
GB0911478D0 (en) | 2009-07-02 | 2009-08-12 | Johnson Matthey Plc | Adsorption of volatile organic compounds derived from organic matter |
JP6799401B2 (en) * | 2016-07-05 | 2020-12-16 | 日本ペイント株式会社 | Paint composition |
CN106345289A (en) * | 2016-08-28 | 2017-01-25 | 桂林市晶准测控技术有限公司 | Harmful gas purifier and preparation method thereof |
-
1996
- 1996-03-18 JP JP06080096A patent/JP3227373B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101499028B1 (en) * | 2013-09-27 | 2015-03-09 | 한국생산기술연구원 | Adsorbent coating solution containing two binder and a method of manufacturing the same |
Also Published As
Publication number | Publication date |
---|---|
JPH09249824A (en) | 1997-09-22 |
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