JP2001190964A - Photocatalyst, method for producing the same, and method for using photocatalyst - Google Patents
Photocatalyst, method for producing the same, and method for using photocatalystInfo
- Publication number
- JP2001190964A JP2001190964A JP2000005812A JP2000005812A JP2001190964A JP 2001190964 A JP2001190964 A JP 2001190964A JP 2000005812 A JP2000005812 A JP 2000005812A JP 2000005812 A JP2000005812 A JP 2000005812A JP 2001190964 A JP2001190964 A JP 2001190964A
- Authority
- JP
- Japan
- Prior art keywords
- photocatalyst
- sulfide
- zinc
- aqueous solution
- fine particle
- 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.)
- Granted
Links
- 239000011941 photocatalyst Substances 0.000 title claims abstract description 141
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims description 47
- 239000005083 Zinc sulfide Substances 0.000 claims abstract description 126
- 229910052984 zinc sulfide Inorganic materials 0.000 claims abstract description 126
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims abstract description 113
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 claims abstract description 113
- 239000010419 fine particle Substances 0.000 claims abstract description 106
- 239000011787 zinc oxide Substances 0.000 claims abstract description 56
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 52
- 239000011593 sulfur Substances 0.000 claims abstract description 51
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims abstract description 46
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims abstract description 45
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 38
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000002245 particle Substances 0.000 claims abstract description 35
- 239000000203 mixture Substances 0.000 claims abstract description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 51
- 239000007864 aqueous solution Substances 0.000 claims description 48
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 41
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 41
- 239000000243 solution Substances 0.000 claims description 33
- -1 sulfur ions Chemical class 0.000 claims description 32
- 150000001875 compounds Chemical class 0.000 claims description 17
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 17
- 239000004065 semiconductor Substances 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 13
- 238000003756 stirring Methods 0.000 claims description 11
- 239000003638 chemical reducing agent Substances 0.000 claims description 9
- 230000001678 irradiating effect Effects 0.000 claims description 9
- 230000005587 bubbling Effects 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 8
- 239000002775 capsule Substances 0.000 claims description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 238000000151 deposition Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 27
- 239000000126 substance Substances 0.000 abstract description 26
- 239000001257 hydrogen Substances 0.000 abstract description 23
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 23
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 239000003574 free electron Substances 0.000 abstract description 11
- 239000002994 raw material Substances 0.000 abstract description 10
- 230000006798 recombination Effects 0.000 abstract description 7
- 238000005215 recombination Methods 0.000 abstract description 7
- 239000007795 chemical reaction product Substances 0.000 abstract description 6
- 238000006722 reduction reaction Methods 0.000 abstract description 6
- 238000007254 oxidation reaction Methods 0.000 abstract description 5
- 231100000956 nontoxicity Toxicity 0.000 abstract description 4
- 230000005684 electric field Effects 0.000 abstract description 3
- JBQYATWDVHIOAR-UHFFFAOYSA-N tellanylidenegermanium Chemical compound [Te]=[Ge] JBQYATWDVHIOAR-UHFFFAOYSA-N 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 13
- 238000010586 diagram Methods 0.000 description 12
- 229910001868 water Inorganic materials 0.000 description 10
- 238000004090 dissolution Methods 0.000 description 7
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- VDQVEACBQKUUSU-UHFFFAOYSA-M disodium;sulfanide Chemical compound [Na+].[Na+].[SH-] VDQVEACBQKUUSU-UHFFFAOYSA-M 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 6
- 238000000635 electron micrograph Methods 0.000 description 6
- 238000006303 photolysis reaction Methods 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 5
- 239000010779 crude oil Substances 0.000 description 5
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 5
- 229910052753 mercury Inorganic materials 0.000 description 5
- 230000001699 photocatalysis Effects 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- 239000011701 zinc Substances 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical group [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 239000003929 acidic solution Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 238000006479 redox reaction Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000013032 photocatalytic reaction Methods 0.000 description 3
- 230000015843 photosynthesis, light reaction Effects 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- 238000000967 suction filtration Methods 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 238000003917 TEM image Methods 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 2
- 231100001243 air pollutant Toxicity 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010894 electron beam technology Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000005350 fused silica glass Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 102100032566 Carbonic anhydrase-related protein 10 Human genes 0.000 description 1
- 101000867836 Homo sapiens Carbonic anhydrase-related protein 10 Proteins 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000000020 Nitrocellulose Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 238000000441 X-ray spectroscopy Methods 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- UHYPYGJEEGLRJD-UHFFFAOYSA-N cadmium(2+);selenium(2-) Chemical compound [Se-2].[Cd+2] UHYPYGJEEGLRJD-UHFFFAOYSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 230000003278 mimic effect Effects 0.000 description 1
- 229920001220 nitrocellulos Polymers 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- UGZADUVQMDAIAO-UHFFFAOYSA-L zinc hydroxide Chemical compound [OH-].[OH-].[Zn+2] UGZADUVQMDAIAO-UHFFFAOYSA-L 0.000 description 1
- 229940007718 zinc hydroxide Drugs 0.000 description 1
- 229910021511 zinc hydroxide Inorganic materials 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Physical Water Treatments (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
(57)【要約】
【課題】 触媒活性が高く、毒性がなく、廉価で寿命が
長い、新たな光触媒と、その製造方法及びその光触媒を
用いて硫化水素を分解し、水素とイオウを製造する方法
を提供する。
【解決手段】 光触媒である硫化亜鉛微粒子層状物質
は、5nmから10nmの粒径の硫化亜鉛(ZnS)微
粒子層から成る外殻1と、空洞を2を有し、かつ、この
外殻1は穴3を有する。また、この硫化亜鉛微粒子層状
物質は、原料物質である酸化亜鉛粒子の外形を反映した
外殻を有する。さらに、この光触媒である硫化亜鉛微粒
子層は、亜鉛(Zn)とイオウ(S)の成分比が層厚方
向に変化した構造を有し、層厚方向に電界が存在し、光
照射によって生じた自由電子と自由ホールの再結合が減
少し、酸化反応生成物と還元反応生成物との再結合も減
少し、高い触媒活性を得ることができる。
PROBLEM TO BE SOLVED: To provide a new photocatalyst having high catalytic activity, no toxicity, low cost and long life, a method for producing the same, and hydrogen sulfide being decomposed by using the photocatalyst to produce hydrogen and sulfur. Provide a way. SOLUTION: A zinc sulfide fine particle layered material as a photocatalyst has an outer shell 1 composed of a zinc sulfide (ZnS) fine particle layer having a particle diameter of 5 nm to 10 nm, a cavity 2, and the outer shell 1 has a hole. 3 The layered substance of zinc sulfide fine particles has an outer shell reflecting the outer shape of zinc oxide particles as a raw material. Further, the zinc sulfide fine particle layer as the photocatalyst has a structure in which the composition ratio of zinc (Zn) and sulfur (S) changes in the layer thickness direction, and an electric field exists in the layer thickness direction, which is generated by light irradiation. The recombination between free electrons and free holes is reduced, the recombination between oxidation reaction products and reduction reaction products is also reduced, and high catalytic activity can be obtained.
Description
【0001】[0001]
【発明の属する技術分野】この発明は、光触媒を利用し
て有用な化学物質を生成する化学工業分野、及び光触媒
を利用して悪臭物質、大気汚染物質を除去する環境保全
分野などで利用され、硫化水素を利用し、水素とイオウ
を生成するための光触媒、その光触媒の製造方法、並び
にその光触媒を利用して硫化水素から水素とイオウを製
造する方法に関するものである。BACKGROUND OF THE INVENTION The present invention is used in the chemical industry field for producing useful chemical substances using a photocatalyst, and in the environmental protection field for removing malodorous substances and air pollutants using a photocatalyst. The present invention relates to a photocatalyst for producing hydrogen and sulfur using hydrogen sulfide, a method for producing the photocatalyst, and a method for producing hydrogen and sulfur from hydrogen sulfide using the photocatalyst.
【0002】[0002]
【従来の技術】光触媒技術の応用は、環境汚染物質や悪
臭成分・雑菌などの分解などの様々な化学反応を促進す
る特性を持つことから、抗菌効果のあるタイルや空気清
浄機の抗菌・脱臭フィルターなどへの実用化が始まって
いる。一方で、水などに光触媒を作用させて水素を得る
ことを目的とした研究があるが、光触媒技術の応用はこ
れらに止まらない。有害物質に光触媒を作用させて有用
な化学物質を得ることも可能である。例えば、原油の脱
硫工程に応用することが考えられる。2. Description of the Related Art The application of photocatalytic technology is to promote various chemical reactions such as decomposition of environmental pollutants, odorous components and various germs. Practical application to filters etc. has begun. On the other hand, there is research aimed at obtaining hydrogen by making a photocatalyst act on water or the like, but the application of photocatalyst technology does not stop there. It is also possible to obtain a useful chemical substance by causing a photocatalyst to act on a harmful substance. For example, it is conceivable to apply the present invention to a crude oil desulfurization step.
【0003】図11は、現在、一般的に行われている原
油の脱硫工程を示す。図11に示すように、原油を蒸留
する際に、重質ナフサを水素化生成して原油に含まれる
イオウ成分を全て硫化水素にして回収する。この硫化水
素はクラウス法と呼ばれるプロセスを経て、イオウを酸
化して回収する。クラウス法は、硫化水素の3分の1を
酸化して亜硫酸ガスとし、これと残りの硫化水素とを反
応させて元素イオウとするプロセスである。[0003] Fig. 11 shows a crude oil desulfurization step generally performed at present. As shown in FIG. 11, when distilling crude oil, heavy naphtha is hydrogenated to convert all sulfur components contained in the crude oil into hydrogen sulfide and collect it. This hydrogen sulfide is oxidized and recovered by sulfur through a process called the Claus method. The Claus method is a process in which one-third of hydrogen sulfide is oxidized into sulfur dioxide gas, and the remaining hydrogen sulfide is reacted with the sulfur dioxide gas to form elemental sulfur.
【0004】このプロセスでは、亜硫酸ガスと硫化水素
の触媒反応だけではなく、加熱や凝縮を繰り返すため
に、膨大なエネルギーを要している。また、亜硫酸ガス
の管理にコストがかかるなどの問題を有している。In this process, enormous energy is required not only for the catalytic reaction of sulfur dioxide and hydrogen sulfide but also for repeated heating and condensation. In addition, there is a problem that management of sulfurous acid gas is costly.
【0005】硫化水素が溶解したアルカリ水に光触媒を
加え、紫外線を照射し、その紫外線の光エネルギーを吸
収して光触媒が発生する自由電子及び自由ホールによ
り、硫化水素が溶解したアルカリ水を酸化還元し、水素
とイオウを得る方法、すなわち、光触媒により硫化水素
を分解し、水素及びイオウを生成する方法が実用化でき
れば、遥かに少ないエネルギーで有害物質である硫化水
素を分解し、有用物質である水素及びイオウを生産する
ことが可能になる。すなわち、環境問題の解決に寄与
し、かつ、有用物質を安く生産できることになる。A photocatalyst is added to alkaline water in which hydrogen sulfide is dissolved, and ultraviolet light is irradiated. The free electrons and free holes generated by the photocatalyst by absorbing the light energy of the ultraviolet light redox the alkaline water in which hydrogen sulfide is dissolved. If a method for obtaining hydrogen and sulfur, that is, a method for decomposing hydrogen sulfide by a photocatalyst and producing hydrogen and sulfur can be put to practical use, hydrogen sulfide, which is a harmful substance, is decomposed with much less energy and is a useful substance. It becomes possible to produce hydrogen and sulfur. That is, it contributes to solving environmental problems and can produce useful substances at low cost.
【0006】しかしながら、従来の光触媒は、硫化水素
を分解し、水素及びイオウを得る目的に使用するには、
以下に述べる解決すべき課題があった。第1に、触媒活
性が低い。第2に、光触媒に毒性がある。第3に、貴金
属のような助触媒を使用し、高価である。However, the conventional photocatalyst cannot be used for the purpose of decomposing hydrogen sulfide to obtain hydrogen and sulfur.
There were the following problems to be solved. First, the catalyst activity is low. Second, the photocatalyst is toxic. Third, they use co-catalysts such as precious metals and are expensive.
【0007】光触媒に光照射すると、自由電子と自由正
孔が生じるが、再結合してしまう確率が高く、また、酸
化還元反応により分解された化学物質が再び再結合して
元の化合物に戻ってしまう確率も高く、触媒活性が低く
なってしまう。このため、従来は、光触媒の表面の一部
に貴金属を担持させることによって、触媒活性の低下を
防いでいる。例えば、酸化チタンTiO2光触媒は表面
の一部に白金(Pt)を担持して触媒活性を高めている
が、このため触媒が高価になってしまう。When the photocatalyst is irradiated with light, free electrons and free holes are generated, but the probability of recombination is high, and the chemical substance decomposed by the redox reaction is recombined to return to the original compound. The probability is high, and the catalytic activity is low. For this reason, a reduction in catalytic activity has been conventionally prevented by supporting a noble metal on a part of the surface of the photocatalyst. For example, a titanium oxide TiO2 photocatalyst carries platinum (Pt) on a part of its surface to increase the catalytic activity, but the catalyst becomes expensive.
【0008】第4に、触媒の寿命が短い。光触媒に光照
射すると、自由電子と自由正孔が生じるが、その強い酸
化還元反応により、目的とする化学物質以外に触媒それ
自身が酸化還元され、溶解してしまい、触媒作用を失う
といった光溶解の問題がある。このため、一般に、犠牲
還元剤といわれる物質を使用し触媒の溶解を防いでいる
が、いまだ、実用上十分な寿命を持つ光触媒と犠牲還元
剤の組み合わせが得られていない。Fourth, the life of the catalyst is short. Irradiation of the photocatalyst with light generates free electrons and free holes. The strong redox reaction causes the catalyst itself to redox and dissolve in addition to the target chemical substance. There is a problem. For this reason, generally, a substance called a sacrificial reducing agent is used to prevent dissolution of the catalyst, but a combination of a photocatalyst and a sacrificial reducing agent having a practically sufficient life has not yet been obtained.
【0009】[0009]
【発明が解決しようとする課題】上記に述べたように、
従来の光触媒では、触媒活性が低い、毒性がある、高価
である、寿命が短いといった解決すべき課題があり、有
用化学物質の生産、大気汚染物質の除去等の環境保全目
的に使用するには、未だ不十分である。SUMMARY OF THE INVENTION As mentioned above,
Conventional photocatalysts have problems to be solved, such as low catalytic activity, toxic, expensive, and short lifespan.Therefore, they cannot be used for environmental protection purposes such as production of useful chemicals and removal of air pollutants. Is still inadequate.
【0010】そこでこの発明は、上記の課題にかんが
み、触媒活性が高く毒性がなく、安価で寿命が長い新た
な光触媒、その製造方法、及びその光触媒を用いて硫化
水素を分解し、水素と硫黄を製造する方法を提供するこ
とを目的とする。In view of the above problems, the present invention provides a new photocatalyst having high catalytic activity, non-toxicity, low cost and long life, a method for producing the same, and a method for decomposing hydrogen sulfide using the photocatalyst to produce hydrogen and sulfur. An object of the present invention is to provide a method for producing the same.
【0011】[0011]
【課題を解決するための手段】上記目的を達成するため
に、この発明のうち光触媒の発明は、化合物半導体微粒
子が層状に集合し、この層の厚み方向にこの化合物の成
分比が変化していることを特徴とする光触媒であり、好
適には、化合物半導体微粒子は、5から10nmの粒径
を有する。さらに、この発明の光触媒は、上記層状の集
合体から成る外殻を有し、かつ、この外殻は穴を有して
いる。好適には、外殻の形状がカプセル状又は球形状で
ある。Means for Solving the Problems In order to achieve the above object, the invention of a photocatalyst according to the present invention is characterized in that compound semiconductor fine particles are aggregated in a layer and the component ratio of the compound changes in the thickness direction of the layer. Preferably, the compound semiconductor fine particles have a particle size of 5 to 10 nm. Further, the photocatalyst of the present invention has an outer shell made of the above-mentioned layered aggregate, and the outer shell has a hole. Preferably, the shape of the outer shell is capsule or spherical.
【0012】さらに、化合物半導体はII族元素とVI
族元素からなり、最適には、硫化亜鉛である。Further, the compound semiconductor is composed of a group II element and VI
Consisting of group III elements, most preferably zinc sulfide.
【0013】さらに、この光触媒を製造するには、前記
化合物半導体を構成するII族元素の酸化物粒子を、イ
オウイオンを含む水溶液中で溶解し、このII族元素の
硫化物微粒子を析出させて製造する。好適には、前記I
I族元素の酸化物粒子は酸化亜鉛である。Further, in order to produce the photocatalyst, oxide particles of a group II element constituting the compound semiconductor are dissolved in an aqueous solution containing sulfur ions, and sulfide fine particles of the group II element are precipitated. To manufacture. Preferably, said I
The oxide particles of the Group I element are zinc oxide.
【0014】この光触媒の製造方法は、最適には、酸化
亜鉛微粒子と硫化ナトリウム水溶液とを混合する工程
と、この混合液を攪拌する工程とからなる光触媒の製造
方法である。さらに、酸化亜鉛微粒子と硫化ナトリウム
水溶液とを混合する工程と、この混合液に紫外線を照射
しながら攪拌する工程とからなる光触媒の製造方法であ
る。さらには、酸化亜鉛微粒子と硫化ナトリウム水溶液
とを混合する工程と、この混合液に硫化水素をバブリン
グしながら攪拌する工程と、硫化水素ガスを止め、さら
に一定時間攪拌する工程とからなる光触媒の製造方法で
ある。さらには、酸化亜鉛微粒子と硫化ナトリウム水溶
液とを混合する工程と、この混合液に紫外線を照射し、
且つ硫化水素をバブリングする工程とからなる光触媒の
製造方法である。This method for producing a photocatalyst is optimally a method for producing a photocatalyst comprising a step of mixing zinc oxide fine particles and an aqueous solution of sodium sulfide, and a step of stirring this mixture. Further, the present invention provides a method for producing a photocatalyst, comprising a step of mixing zinc oxide fine particles and an aqueous solution of sodium sulfide, and a step of stirring the mixture while irradiating the mixture with ultraviolet rays. Further, a photocatalyst production process comprising the steps of mixing zinc oxide fine particles and an aqueous solution of sodium sulfide, stirring hydrogen sulfide while bubbling the mixture, and stopping hydrogen sulfide gas and further stirring for a certain period of time. Is the way. Further, a step of mixing the zinc oxide fine particles and the aqueous solution of sodium sulfide, and irradiating the mixed solution with ultraviolet rays,
And a step of bubbling hydrogen sulfide.
【0015】この発明の硫化亜鉛光触媒を使用する方法
は、犠牲還元剤として硫化ナトリウム水溶液を用いる。In the method using the zinc sulfide photocatalyst of the present invention, an aqueous sodium sulfide solution is used as a sacrificial reducing agent.
【0016】この発明の光触媒の使用方法のうち、硫化
水素を分解し、水素、及びイオウを製造する方法は、本
発明光触媒を使用して、硫化ナトリウム水溶液を、この
光触媒の犠牲還元剤として用し、好適には、次の各工程
よりなる。 (イ)苛性ソーダ水溶液に硫化水素を溶解する工程。 (ロ)該溶液に光触媒を加え、紫外線を照射し、水素ガ
スを回収する工程。 (ハ)(ロ)の工程後の該溶液からイオウを回収する工
程。 (ニ)(ハ)の工程後の該溶液を(イ)の工程の苛性ソ
ーダ水溶液として再利用する工程。Among the methods for using the photocatalyst of the present invention, the method for decomposing hydrogen sulfide to produce hydrogen and sulfur uses the aqueous sodium sulfide solution as a sacrificial reducing agent for the photocatalyst using the photocatalyst of the present invention. Preferably, the method comprises the following steps. (A) A step of dissolving hydrogen sulfide in an aqueous solution of caustic soda. (B) a step of adding a photocatalyst to the solution, irradiating the solution with ultraviolet rays, and collecting hydrogen gas. (C) recovering sulfur from the solution after the step (b). (D) a step of reusing the solution after the step (c) as the aqueous caustic soda solution of the step (a).
【0017】次に、この発明による光触媒の特徴につい
て述べる。この発明に係る光触媒である硫化亜鉛微粒子
層は、この層の厚み方向に、硫化亜鉛の亜鉛原子数とイ
オウ原子数の比、すなわち、成分比が変化しているた
め、この層厚方向に電界が発生している。このため、光
照射によって生じた自由電子と自由ホールは互いに離れ
る方向に移動する。このため、自由電子と自由ホールの
再結合が減少し、また、酸化反応の反応場所と還元反応
の反応場所も分離することから、酸化反応生成物と還元
反応生成物との再結合も減少する。Next, the features of the photocatalyst according to the present invention will be described. The zinc sulfide fine particle layer, which is a photocatalyst according to the present invention, has a ratio of the number of zinc atoms to the number of sulfur atoms of zinc sulfide in the thickness direction of the layer, that is, the component ratio changes. Has occurred. Therefore, free electrons and free holes generated by light irradiation move in directions away from each other. For this reason, recombination of free electrons and free holes is reduced, and the reaction site of the oxidation reaction is separated from the reaction site of the reduction reaction, so that the recombination between the oxidation reaction product and the reduction reaction product is also reduced. .
【0018】これによって、光照射によって生成した自
由電子、自由ホールが、目的とする酸化還元反応に有効
に使われるので、本発明の硫化亜鉛微粒子層は高い光触
媒活性を有する。As a result, the free electrons and free holes generated by light irradiation are effectively used in the intended oxidation-reduction reaction, so that the zinc sulfide fine particle layer of the present invention has high photocatalytic activity.
【0019】次に、この発明の光触媒の製造方法の特徴
について述べる。原料である酸化亜鉛微粒子と硫化ナト
リウム水溶液とを混合し、この混合液を撹拌すると、酸
化亜鉛が水と反応して亜鉛酸イオンになり水溶液中に溶
出する。この亜鉛酸イオンは硫化ナトリウム水溶液のイ
オウ・イオンと反応し、硫化亜鉛になる。この硫化亜鉛
は原料である酸化亜鉛粒子の表面に析出し、硫化亜鉛微
粒子層を形成する。この硫化亜鉛微粒子層が形成される
と、水がこの硫化亜鉛微粒子層を浸透し、原料である酸
化亜鉛表面に至り、酸化亜鉛と反応し、亜鉛酸イオンが
生成する。この亜鉛酸イオンは上記硫化亜鉛微粒子層を
拡散して、表面に達し、イオウ・イオンと反応し、硫化
亜鉛になり硫化亜鉛微粒子層に析出する。硫化亜鉛微粒
子層が成長するにつれ、亜鉛酸イオンが硫化亜鉛微粒子
層を拡散し難くなり、化学量論比からずれた組成の硫化
亜鉛が析出する。Next, the features of the method for producing a photocatalyst of the present invention will be described. When zinc oxide fine particles as a raw material and an aqueous solution of sodium sulfide are mixed, and this mixed solution is stirred, zinc oxide reacts with water to form zincate ions and elutes into the aqueous solution. The zincate ion reacts with sulfur ions in the aqueous sodium sulfide solution to form zinc sulfide. The zinc sulfide precipitates on the surface of zinc oxide particles as a raw material, and forms a zinc sulfide fine particle layer. When the zinc sulfide fine particle layer is formed, water penetrates the zinc sulfide fine particle layer, reaches the surface of zinc oxide as a raw material, reacts with zinc oxide, and generates zincate ions. The zincate ions diffuse in the zinc sulfide fine particle layer, reach the surface, react with sulfur ions, become zinc sulfide, and precipitate on the zinc sulfide fine particle layer. As the zinc sulfide fine particle layer grows, zincate ions become difficult to diffuse through the zinc sulfide fine particle layer, and zinc sulfide having a composition deviating from the stoichiometric ratio is deposited.
【0020】この硫化亜鉛微粒子層の生成速度を大きく
するには紫外線照射が有効である。すなわち、酸化亜鉛
微粒子と硫化ナトリウム水溶液を混合し、紫外線照射す
れば、酸化亜鉛が光溶解をおこすため亜鉛酸イオンが溶
出し易くなり、硫化亜鉛微粒子層の成長が早くなる。Ultraviolet irradiation is effective for increasing the formation rate of the zinc sulfide fine particle layer. That is, when the zinc oxide fine particles and the aqueous solution of sodium sulfide are mixed and irradiated with ultraviolet light, zinc oxide causes photodissolution, so that zincate ions are easily eluted and the growth of the zinc sulfide fine particle layer is accelerated.
【0021】この硫化亜鉛微粒子層の生成速度を大きく
するには硫化水素の溶解が有効である。すなわち、酸化
亜鉛微粒子と水の混合液に硫化水素を溶解すると、イオ
ウ・イオンを含む弱酸性溶液となり、酸化亜鉛は弱酸性
溶液に良く溶けるため、同様に硫化亜鉛微粒子層の成長
が早くなる。Dissolution of hydrogen sulfide is effective for increasing the rate of formation of the zinc sulfide fine particle layer. That is, when hydrogen sulfide is dissolved in a mixed liquid of zinc oxide fine particles and water, a weakly acidic solution containing sulfur ions is formed. Since zinc oxide is well dissolved in the weakly acidic solution, the growth of the zinc sulfide fine particle layer is similarly accelerated.
【0022】この硫化亜鉛微粒子層の生成速度を大きく
するには紫外線照射と硫化水素の溶解を組み合わせても
良い。すなわち、酸化亜鉛微粒子と硫化ナトリウム水溶
液と硫化水素を混合し、紫外線を照射し、攪拌すれば、
さらに、硫化亜鉛微粒子層の成長が早くなる。To increase the formation rate of the zinc sulfide fine particle layer, ultraviolet irradiation and dissolution of hydrogen sulfide may be combined. That is, if zinc oxide fine particles, sodium sulfide aqueous solution and hydrogen sulfide are mixed, irradiated with ultraviolet rays, and stirred,
Further, the growth of the zinc sulfide fine particle layer is accelerated.
【0023】上記したこれらの方法によって、本発明の
光触媒である硫化亜鉛微粒子層を製造することができ
る。By the above-described methods, a zinc sulfide fine particle layer as the photocatalyst of the present invention can be produced.
【0024】次に、本発明の光触媒使用方法について説
明する。本発明の光触媒である硫化亜鉛微粒子層を使用
する場合に、犠牲還元剤として硫化ナトリウム水溶液を
用いれば、硫化ナトリウム水溶液中のナトリウムが、硫
化亜鉛微粒子層の亜鉛に代わって酸化されるため、硫化
亜鉛微粒子層の亜鉛が水溶液中にの溶出することを防止
でき、硫化亜鉛微粒子層の光触媒特性が劣化しない。Next, the method of using the photocatalyst of the present invention will be described. When using a zinc sulfide fine particle layer as the photocatalyst of the present invention, if an aqueous sodium sulfide solution is used as a sacrificial reducing agent, sodium in the aqueous sodium sulfide solution is oxidized instead of zinc in the zinc sulfide fine particle layer. Elution of zinc in the zinc fine particle layer into the aqueous solution can be prevented, and the photocatalytic property of the zinc sulfide fine particle layer does not deteriorate.
【0025】次に、本発明の光触媒使用方法のうち、硫
化水素を光分解し、水素、及びイオウを製造する方法の
特徴について説明する。苛性ソーダに硫化水素を溶解す
ると、犠牲還元剤として有効な硫化ナトリウムと水が生
成し、この溶液に本発明の硫化亜鉛微粒子層を加え、紫
外線照射すると水素ガスとイオウが生成する。水素ガス
と硫黄を回収すれば、溶液は苛性ソーダに戻る。この溶
液は硫化水素を溶解するための苛性ソーダに再利用する
ことができる。Next, among the methods for using the photocatalyst of the present invention, the features of the method for producing hydrogen and sulfur by photolysis of hydrogen sulfide will be described. When hydrogen sulfide is dissolved in caustic soda, sodium sulfide and water, which are effective as sacrificial reducing agents, are generated. The zinc sulfide fine particle layer of the present invention is added to this solution, and irradiation with ultraviolet rays generates hydrogen gas and sulfur. Once the hydrogen gas and sulfur are recovered, the solution returns to caustic soda. This solution can be reused in caustic soda to dissolve hydrogen sulfide.
【0026】この方法を用いれば、紫外線光源に必要な
エネルギー以外には、何も必要とせずに、硫化水素を分
解し、水素及びイオウを得ることができる。By using this method, hydrogen sulfide can be decomposed and hydrogen and sulfur can be obtained without requiring anything other than the energy required for the ultraviolet light source.
【0027】[0027]
【発明の実施の形態】以下、図1,図2,図3に基づ
き、同一又は対応する部分には同一符号を用いて、本発
明による光触媒及びその製造方法並びに光触媒使用方法
の好適な実施の形態を説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to FIGS. 1, 2 and 3, the same or corresponding parts are designated by the same reference numerals, and a preferred embodiment of a photocatalyst according to the present invention, a method for producing the same and a method for using the photocatalyst will be described. The form will be described.
【0028】本発明の光触媒のうち、化合物半導体が、
II−VI族化合物半導体であり、II−VI族化合物
半導体が硫化亜鉛である光触媒、すなわち、硫化亜鉛微
粒子層状物質の構造を図1に基づいて説明する。図1は
この発明にかかる光触媒である硫化亜鉛微粒子層状物質
の構造模式図である。図1(A)は硫化亜鉛微粒子層状
物質の外形構造模式図、図1(B)は、図1(A)で矢
印で示した方向の断面の構造模式図である。In the photocatalyst of the present invention, the compound semiconductor is
The structure of a photocatalyst that is a II-VI compound semiconductor and the II-VI compound semiconductor is zinc sulfide, that is, the structure of a zinc sulfide fine particle layered material will be described with reference to FIG. FIG. 1 is a schematic structural view of a zinc sulfide fine particle layered material which is a photocatalyst according to the present invention. FIG. 1A is a schematic diagram of the external structure of the zinc sulfide fine particle layered material, and FIG. 1B is a schematic structural diagram of a cross section in a direction indicated by an arrow in FIG. 1A.
【0029】この発明にかかる光触媒である硫化亜鉛微
粒子層状物質は、次の(1)及び(2)の特徴を有して
いる。 特徴(1): 図1(B)に示すように、本発明にかか
る光触媒である硫化亜鉛微粒子層状物質は、5nmから
10nmの粒径の硫化亜鉛(ZnS)微粒子層から成る
外殻1と、空洞2を有し、かつ、この外殻1は穴3を有
する。また、この硫化亜鉛微粒子層状物質は、原料物質
である酸化亜鉛粒子の外形を反映した外殻を有する。 特徴(2): 本発明にかかる光触媒である硫化亜鉛微
粒子層は、亜鉛(Zn)とイオウ(S)の成分比が、層
厚方向に変化した構造を有する。The zinc sulfide fine particle layered material which is a photocatalyst according to the present invention has the following features (1) and (2). Feature (1): As shown in FIG. 1 (B), the zinc sulfide fine particle layered material which is a photocatalyst according to the present invention has an outer shell 1 composed of a zinc sulfide (ZnS) fine particle layer having a particle diameter of 5 to 10 nm; It has a cavity 2 and the shell 1 has a hole 3. The layered substance of zinc sulfide fine particles has an outer shell reflecting the outer shape of zinc oxide particles as a raw material. Feature (2): The zinc sulfide fine particle layer as the photocatalyst according to the present invention has a structure in which the component ratio of zinc (Zn) and sulfur (S) changes in the layer thickness direction.
【0030】次に、本発明にかかる光触媒である硫化亜
鉛微粒子層状物質の上記(1)及び(2)の特徴を、図
2及び図3に基づいて説明する。Next, the features (1) and (2) of the zinc sulfide fine particle layered material which is a photocatalyst according to the present invention will be described with reference to FIGS.
【0031】特徴(1)を図2に基づいて説明する。図
2(A)は本発明の光触媒である硫化亜鉛微粒子層状物
質を、図1(B)の断面に垂直な方向から図1(A)の
Y方向に電子線を照射して撮影した透過電子顕微鏡写真
(この写真を図8として示す。)の模写図である。図2
(A)にみられる黒色部分1及び灰色部分1は、それぞ
れ、図1(A)の直方体の縁と面に対応する。The feature (1) will be described with reference to FIG. FIG. 2A shows transmitted electrons obtained by irradiating a layered substance of zinc sulfide fine particles, which is a photocatalyst of the present invention, with an electron beam from a direction perpendicular to the cross section of FIG. 1B in the Y direction of FIG. FIG. 9 is a simulated view of a micrograph (this photograph is shown as FIG. 8). FIG.
The black portion 1 and the gray portion 1 seen in FIG. 1A correspond to the edge and the surface of the rectangular parallelepiped in FIG.
【0032】図2(A)にみられる黒色部分1及び灰色
部分1は、微少領域EDX(Energy Dispe
rsive X−ray Spectroscopy)
を使用して測定した結果、どちらも5nmから10nm
の粒径から成る硫化亜鉛微粒子の層であることが確認さ
れている。同一物質で構成された直方体の縁と面で、透
過電子線の強度が異なるのは、この直方体の内部に空洞
があることを示している。The black portion 1 and the gray portion 1 shown in FIG. 2A are minute regions EDX (Energy Disp.).
rsive X-ray Spectroscopy)
As a result of measurement using
It has been confirmed that the layer is a layer of zinc sulfide fine particles having a particle size of The difference in the intensity of the transmitted electron beam between the edge and the surface of the rectangular parallelepiped made of the same substance indicates that there is a cavity inside the rectangular parallelepiped.
【0033】すなわち、本発明にかかる光触媒である硫
化亜鉛微粒子層状物質は図1(B)の模式図に示したよ
うに、5nmから10nmの粒径の硫化亜鉛(ZnS)
微粒子層から成る外殻1と空洞2とを有し、かつ、この
外殻1は穴3を有していることが判る。That is, as shown in the schematic diagram of FIG. 1B, the zinc sulfide fine particle layered material which is a photocatalyst according to the present invention has a particle diameter of 5 to 10 nm.
It can be seen that it has an outer shell 1 made of a fine particle layer and a cavity 2, and this outer shell 1 has a hole 3.
【0034】また、図2(B)はこの硫化亜鉛微粒子層
状物質の生成に用いた原料の酸化亜鉛粒子4の走査型電
子顕微鏡写真(この写真を図9に示す。)の模写図であ
る。この図から明らかなように、本発明にかかる光触媒
である硫化亜鉛微粒子層状物質は、原料として用いた酸
化亜鉛粒子の形状を反映した外形を持つ。この例では該
直方体の形状について示したが、カプセル状又は球状で
も良い。FIG. 2B is a schematic drawing of a scanning electron microscope photograph (this photograph is shown in FIG. 9) of the zinc oxide particles 4 used as a raw material for producing the zinc sulfide fine particle layered material. As is clear from this figure, the zinc sulfide fine particle layered material as the photocatalyst according to the present invention has an outer shape reflecting the shape of zinc oxide particles used as a raw material. In this example, the shape of the rectangular parallelepiped is shown, but the shape may be a capsule or a sphere.
【0035】なお、この透過電子顕微鏡写真に使用し
た、本発明にかかる光触媒である硫化亜鉛微粒子層状物
質は、本発明光触媒の製造方法の実施の形態に述べる製
造方法で作製した硫化亜鉛微粒子層状物質を、0.1モ
ル硫化ナトリウム(Na2 S)水溶液に加え、50時間
の紫外線照射による光分解反応を生じさせた後のもので
ある。The photocatalytic zinc sulfide fine particle layered material used in the transmission electron micrograph was the zinc sulfide fine particle layered material prepared by the production method described in the embodiment of the photocatalyst production method of the present invention. Was added to a 0.1 molar aqueous solution of sodium sulfide (Na 2 S) to cause a photolysis reaction by irradiation with ultraviolet rays for 50 hours.
【0036】特徴(2)を、図3に基づいて説明する。
図3(A)は、生成途中の本発明の光触媒である硫化亜
鉛微粒子層状物質を、図1と同様の条件で撮影した透過
電子顕微鏡写真(この写真を図10に示す。)の模写図
である。図3(B)はその断面方向の構造模式図であ
る。図3(A)の中心にみられる黒色部分4は、微少領
域EDXによる測定の結果、酸化亜鉛であることが確認
されており、図3(B)の酸化亜鉛粒子4に対応する。
図3(A)の中心にみられる黒色部分4の外側の灰色の
帯状部分2は図3(B)の空洞2に対応する。図3
(A)の帯状の灰色の部分2の外側の黒色部分1は硫化
亜鉛微粒子層であることが微少領域EDXによる測定で
確認されており、図3(B)の外殻1に対応する。図3
(A)の黒色部分1の外側と、空洞2の上と、酸化亜鉛
粒子4の上に分布している雲状の物質5は硫化亜鉛の凝
集体であることが微少領域EDX分析機による測定によ
り、確認されている。The feature (2) will be described with reference to FIG.
FIG. 3A is a simulated view of a transmission electron micrograph (the photograph is shown in FIG. 10) of the zinc sulfide fine particle layered material that is the photocatalyst of the present invention in the process of being produced under the same conditions as in FIG. is there. FIG. 3B is a schematic structural view in the cross-sectional direction. The black portion 4 seen at the center of FIG. 3A has been confirmed to be zinc oxide as a result of measurement using the microscopic region EDX, and corresponds to the zinc oxide particles 4 in FIG. 3B.
The gray strip 2 outside the black portion 4 at the center of FIG. 3A corresponds to the cavity 2 in FIG. 3B. FIG.
It has been confirmed by measurement in the minute region EDX that the black portion 1 outside the band-like gray portion 2 in (A) is a zinc sulfide fine particle layer, and corresponds to the outer shell 1 in FIG. 3 (B). FIG.
(A) The cloud-like substance 5 distributed on the outside of the black portion 1, on the cavity 2, and on the zinc oxide particles 4 is determined to be an aggregate of zinc sulfide by a micro-area EDX analyzer. Has been confirmed by
【0037】図3(A)に見られるように、酸化亜鉛粒
子4と硫化亜鉛微粒子層から成る外殻1との間に空洞2
がみられることは、以下に述べる生成過程で、硫化亜鉛
微粒子層が生成されることを示している。すなわち、硫
化ナトリウム(Na2 S)水溶液中で、酸化亜鉛(Zn
O)が、酸化亜鉛粒子4の表面から、亜鉛酸イオン(Z
nO2-)の形で溶出する。この亜鉛酸イオンは、硫化ナ
トリウム(Na2 S)水溶液のイオウイオン(S2-)と
反応し、硫化亜鉛(ZnS)になる。この硫化亜鉛は酸
化亜鉛粒子4の表面に析出し、硫化亜鉛微粒子層を形成
する。この硫化亜鉛微粒子層が形成されると、水がこの
硫化亜鉛微粒子層を浸透し、原料である酸化亜鉛4の表
面に到り、酸化亜鉛4と反応し、亜鉛酸イオンが生成す
る。この亜鉛酸イオンは硫化亜鉛微粒子層を拡散して、
この硫化亜鉛微粒子層が酸化亜鉛粒子4と対向する面と
反対側の面、すなわち、硫化亜鉛微粒子層の表面に到
る。この表面で、この亜鉛酸イオンは、イオウ・イオン
と反応し、硫化亜鉛になり硫化亜鉛微粒子層に析出し、
硫化亜鉛微粒子層が成長していく。As shown in FIG. 3A, a cavity 2 is provided between the zinc oxide particles 4 and the outer shell 1 composed of the zinc sulfide fine particle layer.
This indicates that a zinc sulfide fine particle layer is formed in the formation process described below. That is, in an aqueous solution of sodium sulfide (Na 2 S), zinc oxide (Zn)
O) from the surface of the zinc oxide particles 4
eluting in the form of nO 2-). The zincate ion reacts with the sulfur ion (S 2− ) of the aqueous solution of sodium sulfide (Na 2 S) to form zinc sulfide (ZnS). The zinc sulfide precipitates on the surface of the zinc oxide particles 4 to form a zinc sulfide fine particle layer. When the zinc sulfide fine particle layer is formed, water penetrates the zinc sulfide fine particle layer, reaches the surface of the zinc oxide 4 as a raw material, reacts with the zinc oxide 4, and generates zincate ions. This zincate ion diffuses through the zinc sulfide fine particle layer,
The zinc sulfide fine particle layer reaches the surface opposite to the surface facing the zinc oxide particles 4, that is, the surface of the zinc sulfide fine particle layer. On this surface, this zincate ion reacts with sulfur ions to form zinc sulfide, which is deposited on the zinc sulfide fine particle layer,
The zinc sulfide fine particle layer grows.
【0038】このような生成過程であるので、酸化亜鉛
粒子4の一部が亜鉛酸イオンとして溶出して無くなった
分の体積の欠損が生じるため、図3(A)に見られるよ
うな空洞2が生じる。In such a production process, a part of the zinc oxide particles 4 is eluted as zincate ions and disappears, resulting in a volume loss, so that the cavity 2 as shown in FIG. Occurs.
【0039】上記のように、化学反応の一方の成分が拡
散によって供給され、かつ、この反応生成物がこの拡散
層を形成する場合、拡散層の成長に伴い、一方の成分の
供給量がしだいに減少し、化学成分比が変化した層が形
成される。すなわち、本発明にかかる光触媒である硫化
亜鉛微粒子層は、亜鉛(Zn)とイオウ(S)の成分比
が、層厚方向に変化した構造を有する。As described above, when one component of the chemical reaction is supplied by diffusion, and the reaction product forms the diffusion layer, the supply amount of one component is gradually increased as the diffusion layer grows. And a layer having a changed chemical composition ratio is formed. That is, the zinc sulfide fine particle layer as the photocatalyst according to the present invention has a structure in which the component ratio of zinc (Zn) and sulfur (S) changes in the layer thickness direction.
【0040】なお、図3(A)にみられる雲状の物質
5、すなわち、硫化亜鉛の凝集体は、次のようにして生
ずる。硫化亜鉛微粒子層がかなり成長した段階では、亜
鉛酸イオンが硫化亜鉛微粒子層を拡散し難くなるため、
硫化亜鉛微粒子層の内側で、溶出した亜鉛酸イオンの圧
力が高まり、硫化亜鉛微粒子層を破って噴出する。噴出
した亜鉛酸イオンは周辺のイオウイオンと反応し、硫化
亜鉛の凝集体である雲状の物質5になる。図1(B)に
示した穴3は、このようにしてできたものである。The cloudy substance 5 shown in FIG. 3A, that is, the aggregate of zinc sulfide is generated as follows. When the zinc sulfide fine particle layer has grown considerably, zincate ions are less likely to diffuse through the zinc sulfide fine particle layer,
Inside the zinc sulfide fine particle layer, the pressure of the eluted zincate ions is increased, and the zinc sulfide ion breaks and ejects the zinc sulfide fine particle layer. The ejected zincate ions react with the surrounding sulfur ions to form cloud-like substances 5 which are aggregates of zinc sulfide. The hole 3 shown in FIG. 1 (B) is formed in this way.
【0041】次に、本発明光触媒の製造方法の実施の形
態について説明する。本発明の光触媒の組成は硫化亜鉛
(ZnS)であるが、酸化亜鉛粒子から生成するところ
に特徴がある。すなわち、ZnSを生成する場合は亜鉛
イオン溶液と硫化水素の化学反応プロセスを用いるのが
一般的である。これに対し本発明では、酸化亜鉛粒子か
ら硫化亜鉛を生成する。以下に具体的製造方法を説明す
る。Next, an embodiment of the method for producing a photocatalyst of the present invention will be described. The composition of the photocatalyst of the present invention is zinc sulfide (ZnS), which is characterized in that it is formed from zinc oxide particles. That is, when ZnS is generated, a chemical reaction process of a zinc ion solution and hydrogen sulfide is generally used. On the other hand, in the present invention, zinc sulfide is generated from zinc oxide particles. Hereinafter, a specific manufacturing method will be described.
【0042】光触媒製造方法の第一の実施の形態:原料
である酸化亜鉛(ZnO)と硫化ナトリウム(Na
2 S)水溶液を混合し、室温で撹拌する。上記処理後、
ニトロセルロース製メンブランフィルター(孔径0.1
μm)で吸引濾過・蒸留水洗浄後、60℃の恒温槽で乾
燥する。例えば、酸化亜鉛(純度99.999%、粒径
約1μm)5gの場合、0.1モル硫化ナトリウム(N
a2 S・9H2 O,純度98%)水溶液100mlを混
合し、撹拌15時間以上が最適である。First Embodiment of Photocatalyst Production Method: Zinc oxide (ZnO) and sodium sulfide (Na
2 S) Mix the aqueous solution and stir at room temperature. After the above processing,
Nitrocellulose membrane filter (pore size 0.1
After filtration with suction and washing with distilled water, the product is dried in a thermostat at 60 ° C. For example, in the case of 5 g of zinc oxide (purity 99.999%, particle size of about 1 μm), 0.1 mol sodium sulfide (N
(a 2 S.9H 2 O, purity 98%) aqueous solution (100 ml) is mixed and stirred for 15 hours or more.
【0043】つぎに、この方法で、本発明の光触媒であ
る硫化亜鉛微粒子層が生成する過程について説明する。
酸化亜鉛粒子(ZnO)と硫化ナトリウム(Na2 S)
水溶液を混合し、この混合液を撹拌すると、酸化亜鉛が
水と反応し、亜鉛酸イオン(ZnO2 2-)の形で溶出
し、硫化ナトリウム水溶液のイオウイオン(S2-)と反
応して硫化亜鉛(ZnS)になり、酸化亜鉛粒子の表面
に析出して硫化亜鉛微粒子層を形成する。引き続き、硫
化亜鉛微粒子層を浸透してきた水酸化亜鉛が反応して生
成する亜鉛酸イオンが、既に生成された硫化亜鉛微粒子
層を拡散して硫化亜鉛微粒子層の表面に達し、イオウイ
オンと反応して硫化亜鉛になり、硫化亜鉛微粒子層に析
出する。硫化亜鉛微粒子層が成長するにつれ、亜鉛酸イ
オンが硫化亜鉛微粒子層を拡散し難くなり、硫化亜鉛の
成分比のずれた組成の硫化亜鉛微粒子が析出し、本発明
にかかる光触媒である硫化亜鉛微粒子層状物質が生成す
る。Next, the process of forming a zinc sulfide fine particle layer as the photocatalyst of the present invention by this method will be described.
Zinc oxide particles (ZnO) and sodium sulfide (Na 2 S)
When the aqueous solution is mixed and this mixture is stirred, zinc oxide reacts with water, elutes in the form of zincate ions (ZnO 2 2- ), and reacts with sulfur ions (S 2- ) of the sodium sulfide aqueous solution. It becomes zinc sulfide (ZnS) and precipitates on the surface of the zinc oxide particles to form a zinc sulfide fine particle layer. Subsequently, zincate ions generated by the reaction of zinc hydroxide penetrating the zinc sulfide fine particle layer diffuse through the already generated zinc sulfide fine particle layer, reach the surface of the zinc sulfide fine particle layer, and react with sulfur ions. It becomes zinc sulfide and deposits on the zinc sulfide fine particle layer. As the zinc sulfide fine particle layer grows, it becomes difficult for zincate ions to diffuse through the zinc sulfide fine particle layer, and zinc sulfide fine particles having a composition in which the component ratio of zinc sulfide is shifted are precipitated. Layered material forms.
【0044】光触媒製造方法の第2の実施の形態:溶融
石英容器に酸化亜鉛と硫化ナトリウム水溶液を入れ、紫
外線照射する。例えば、酸化亜鉛(純度99.999
%、粒径約1μm)50mgの場合、0.1モル硫化ナ
トリウム水溶液5mlを混合し、500W超高圧水銀灯
照射1時間以上が最適である。上記処理後、メンブラン
フィルターで吸引濾過・蒸留水洗浄し、60℃の恒温槽
で乾燥する。Second Embodiment of Photocatalyst Production Method: Zinc oxide and an aqueous solution of sodium sulfide are placed in a fused quartz container and irradiated with ultraviolet rays. For example, zinc oxide (99.999 purity)
%, Particle size of about 1 μm), 50 mg is best mixed with 5 ml of a 0.1 molar sodium sulfide aqueous solution and irradiated with a 500 W ultra-high pressure mercury lamp for 1 hour or more. After the above treatment, the resultant is subjected to suction filtration and distilled water washing with a membrane filter, and dried in a thermostat at 60 ° C.
【0045】次に、この方法で、本発明の光触媒である
硫化亜鉛微粒子層が生成する過程について説明する。硫
化亜鉛微粒子層が生成する過程は、光触媒製造方法の第
1の実施の形態の場合と同じであるが、紫外線照射をす
れば、酸化亜鉛が光溶解をおこし、亜鉛酸イオンが溶出
し易くなり、硫化亜鉛微粒子層の成長が早くなる。Next, the process of forming a zinc sulfide fine particle layer as the photocatalyst of the present invention by this method will be described. The process of forming the zinc sulfide fine particle layer is the same as in the case of the first embodiment of the photocatalyst manufacturing method. However, when ultraviolet irradiation is performed, zinc oxide undergoes photodissolution and zincate ions are easily eluted. As a result, the growth of the zinc sulfide fine particle layer is accelerated.
【0046】光触媒製造方法の第3の実施の形態:酸化
亜鉛粒子と蒸留水を混合し、硫化水素(H2 S)ガスで
バブリングしながら撹拌し、一定時間後硫化水素ガスを
止め、さらに一定時間撹拌する。例えば、酸化亜鉛(純
度99.999%、粒径約1μm)2gの場合、蒸留水
50mlを混合し、硫化水素ガス流量50ml/min
で、約1時間バブリングし、ガスを止めた後、約12時
間以上の撹拌が最適である。上記処理後、メンブランフ
ィルターで吸引濾過・蒸留水洗浄し、60℃の恒温槽で
乾燥する。Third Embodiment of Photocatalyst Production Method: A mixture of zinc oxide particles and distilled water is stirred while bubbling with hydrogen sulfide (H 2 S) gas. Stir for hours. For example, in the case of 2 g of zinc oxide (purity 99.999%, particle size about 1 μm), 50 ml of distilled water is mixed, and the flow rate of hydrogen sulfide gas is 50 ml / min.
After bubbling for about 1 hour and stopping the gas, stirring for about 12 hours or more is optimal. After the above treatment, the resultant is subjected to suction filtration and distilled water washing with a membrane filter, and dried in a thermostat at 60 ° C.
【0047】次に、この方法で、本発明の光触媒である
硫化亜鉛微粒子層状物質が生成する過程について説明す
る。硫化亜鉛微粒子層が生成する過程は、光触媒製造方
法の第1の実施の形態の場合と同じであるが、酸化亜鉛
粒子と水の混合液に硫化水素を溶解するとイオウイオン
を含む弱酸性溶液となり、酸化亜鉛は弱酸性溶液に良く
溶けるため、硫化亜鉛微粒子層の成長が早くなる。Next, the process of forming a layered material of fine particles of zinc sulfide as the photocatalyst of the present invention by this method will be described. The process of forming the zinc sulfide fine particle layer is the same as that of the first embodiment of the photocatalyst manufacturing method. However, when hydrogen sulfide is dissolved in a mixture of zinc oxide particles and water, a weakly acidic solution containing sulfur ions is formed. On the other hand, zinc oxide dissolves well in a weakly acidic solution, so that the zinc sulfide fine particle layer grows faster.
【0048】光触媒製造方法の第4の実施の形態:溶融
石英容器に酸化亜鉛と硫化ナトリウム水溶液を入れ、硫
化水素ガスでバブリングし、同時に紫外線照射する。例
えば、酸化亜鉛が2gの場合、0.1モル硫化ナトリウ
ム水溶液50mlを混合し、硫化水素ガス流量50ml
/minでバブリングし、同時に500W超高圧水銀灯
照射1時間以上が最適である。上記処理後、メンブラン
フィルターで吸引濾過・蒸留水洗浄し、60℃の恒温槽
で乾燥する。Fourth Embodiment of Photocatalyst Manufacturing Method: A zinc oxide and an aqueous solution of sodium sulfide are put in a fused quartz container, bubbling is performed with hydrogen sulfide gas, and ultraviolet irradiation is performed at the same time. For example, when 2 g of zinc oxide is used, 50 ml of a 0.1 molar sodium sulfide aqueous solution is mixed, and a hydrogen sulfide gas flow rate of 50 ml is mixed.
/ Min, and at the same time, irradiation with a 500 W ultra-high pressure mercury lamp for 1 hour or more is optimal. After the above treatment, the resultant is subjected to suction filtration and distilled water washing with a membrane filter, and dried in a thermostat at 60 ° C.
【0049】この方法で、本発明の光触媒である硫化亜
鉛微粒子層状物質が生成する過程は、光触媒の製造方法
の第1の実施の形態の場合と同じであるが、第2及び第
3の光触媒製造方法の実施の形態で説明したように、酸
化亜鉛の溶解がさらに早くなり、またイオウイオンの供
給も増大することから、硫化亜鉛微粒子層の成長がさら
に早くなる。In this method, the process of forming the layered material of the zinc sulfide fine particles, which is the photocatalyst of the present invention, is the same as that of the first embodiment of the photocatalyst manufacturing method, except that the second and third photocatalysts are used. As described in the embodiment of the manufacturing method, the dissolution of zinc oxide is further accelerated, and the supply of sulfur ions is also increased, so that the growth of the zinc sulfide fine particle layer is further accelerated.
【0050】次に、本発明の光触媒、すなわち、硫化亜
鉛微粒子層状物質光触媒(ストラティファイドZnSナ
ノ微粒子光触媒と命名する。)の光触媒性能について説
明する。図4は、本発明の光触媒の性能を示すため、従
来の光触媒と、同一装置、同一条件で、硫化ナトリウム
水溶液を光分解し、水素ガスの発生量を比較した性能比
較結果である。Next, the photocatalyst performance of the photocatalyst of the present invention, that is, the photocatalyst of a layered substance of fine particles of zinc sulfide (named as a photocatalyst of stratified ZnS nanoparticle) will be described. FIG. 4 is a performance comparison result in which the photocatalyst of the present invention is subjected to photolysis of an aqueous sodium sulfide solution under the same apparatus and under the same conditions as the conventional photocatalyst, and the amount of hydrogen gas generated is compared.
【0051】性能比較に用いた装置を図5に示す。図5
に示すように、この装置は、石英ガラスで製作した光反
応部分6と、発生した水素の定量を行う水素定量部分7
と、発生した水素ガスの体積分の硫化ナトリウム水溶液
8を溜めることによって、水素圧の上昇を防ぐ溶液溜9
と、紫外線照射用の500W水銀灯10と、紫外線11
を集光するためのレンズLと、紫外線11を反射し、光
触媒12に照射するための反射鏡13とで構成されてい
る。光分解反応開始時に系全体を硫化ナトリウム水溶液
8で満たし、一定量の光触媒12を光反応部分6の底に
沈殿させ、発生ガス回収口14を閉じ、500W水銀灯
10を点灯する。水素定量部分7で一定照射時間ごとに
水素発生量を測定する。FIG. 5 shows an apparatus used for performance comparison. FIG.
As shown in the figure, the apparatus comprises a photoreaction section 6 made of quartz glass and a hydrogen quantification section 7 for quantifying generated hydrogen.
And a solution reservoir 9 for preventing an increase in hydrogen pressure by storing a sodium sulfide aqueous solution 8 corresponding to the volume of the generated hydrogen gas.
And a 500 W mercury lamp 10 for ultraviolet irradiation, and ultraviolet 11
And a reflecting mirror 13 for reflecting the ultraviolet light 11 and irradiating the photocatalyst 12 with it. At the start of the photolysis reaction, the entire system is filled with the aqueous sodium sulfide solution 8, a certain amount of the photocatalyst 12 is precipitated at the bottom of the photoreaction portion 6, the generated gas recovery port 14 is closed, and the 500W mercury lamp 10 is turned on. In the hydrogen determination section 7, the amount of generated hydrogen is measured at every constant irradiation time.
【0052】比較に用いた従来の光触媒は、ZnS(純
度99.999%)、CdS(純度90%)、CdSe
(純度99.99%)及びTiO2 (純度95%)であ
る。本発明の光触媒は、光触媒製造方法の第3の実施の
形態で説明した方法で製造した。用いた光触媒の量は各
々50mgである。硫化ナトリウム水溶液は0.1モル
濃度140mlである。The conventional photocatalysts used for comparison are ZnS (purity 99.999%), CdS (purity 90%), CdSe
(Purity 99.99%) and TiO 2 (purity 95%). The photocatalyst of the present invention was manufactured by the method described in the third embodiment of the photocatalyst manufacturing method. The amount of photocatalyst used is 50 mg each. The aqueous sodium sulfide solution has a 0.1 molar concentration of 140 ml.
【0053】この反応は以下の式であらわされる。 Na2 S + H2 O →← 2Na+ + HS- + OH- HS- + 2h+ → S + H+ 2H+ + 2e- → H2 ↑ ここで、e- ,h+ は、光照射によって光触媒が発生し
た自由電子,自由ホールを表す。「→←」は化学平衡反
応を表す。This reaction is represented by the following formula. Na 2 S + H 2 O → ← 2Na + + HS - + OH - HS - + 2h + → S + H + 2H + + 2e - → H 2 ↑ Here, e -, h + is a photocatalyst by light irradiation Represents free electrons and free holes in which. “→ ←” represents a chemical equilibrium reaction.
【0054】図4の性能比較を示すグラフから明らかな
ように、本発明の光触媒である硫化亜鉛微粒子層状物質
(ストラティファイドZnSナノ微粒子光触媒)は、従
来の光触媒に比べ、遥かに触媒活性が高い。As is clear from the graph showing the performance comparison of FIG. 4, the zinc sulfide fine particle layered material (the stratified ZnS nanoparticulate photocatalyst), which is the photocatalyst of the present invention, has much higher catalytic activity than the conventional photocatalyst. high.
【0055】このように触媒活性が高い理由は、前述し
たように、硫化亜鉛微粒子層の硫化亜鉛の成分比が層厚
方向に変化しているため、空間電荷が発生し、層厚方向
に電界が発生しているためである。この電界により、自
由電子と自由ホールが互いに離れる方向に移動するた
め、自由電子と自由ホールの再結合が減少し、また、酸
化反応の反応場所と還元反応の反応場所も離れることか
ら、酸化反応生成物と還元反応生成物との再結合も減少
するため、触媒活性が高くなる。The reason why the catalytic activity is high is that, as described above, since the zinc sulfide component ratio of the zinc sulfide fine particle layer changes in the layer thickness direction, space charge is generated, and an electric field is generated in the layer thickness direction. Is occurring. This electric field causes free electrons and free holes to move away from each other, reducing the recombination of free electrons and free holes, and also separating the reaction sites for oxidation and reduction from oxidation reactions. Since the recombination of the product and the reduction reaction product is also reduced, the catalytic activity is increased.
【0056】次に、硫化ナトリウム水溶液を、本発明の
光触媒である硫化亜鉛微粒子層状物質(ストラティファ
イドZnSナノ微粒子光触媒)の犠牲還元剤として用い
る、本発明の光触媒使用方法について説明する。Next, the method of using the photocatalyst of the present invention using an aqueous solution of sodium sulfide as a sacrificial reducing agent for the zinc sulfide fine particle layered material (Stratified ZnS nanoparticle photocatalyst) which is the photocatalyst of the present invention will be described.
【0057】図6はこの発明の光触媒である硫化亜鉛微
粒子層状物質の寿命を示す特性図である。図5に示した
装置を用い、0.1モル硫化ナトリウム水溶液に本発明
の光触媒を加え、紫外線を照射し、水素ガスの発生が一
段落したとき、すなわち、水溶液中のイオウイオンがす
べて還元されイオウ(S)になった時に、水素ガス量を
測定した後に水素ガスを排出し、新たに硫化ナトリウム
水溶液を追加し、光分解を継続する。図6において、黒
丸は新たな硫化ナトリウム水溶液の追加時点を示し、こ
の上の数値は追加した硫化ナトリウム水溶液の量を示し
ている。FIG. 6 is a characteristic diagram showing the life of the zinc sulfide fine particle layered material which is the photocatalyst of the present invention. Using the apparatus shown in FIG. 5, the photocatalyst of the present invention was added to a 0.1 molar sodium sulfide aqueous solution, and the mixture was irradiated with ultraviolet light to completely generate hydrogen gas, that is, when all the sulfur ions in the aqueous solution were reduced and the sulfur When (S) is reached, the hydrogen gas is discharged after measuring the amount of the hydrogen gas, and a new aqueous solution of sodium sulfide is added to continue the photolysis. In FIG. 6, the black circles indicate the point in time at which a new sodium sulfide aqueous solution is added, and the numerical value above this indicates the amount of the added sodium sulfide aqueous solution.
【0058】図6から明らかなように、本発明の光触媒
である硫化亜鉛微粒子層状物質は、40時間使用しても
触媒活性が変化しない。図6には示さないが、50時間
以上の使用にも光触媒活性の変化は観測されていない。As is clear from FIG. 6, the photocatalyst of the present invention, the zinc sulfide fine particle layered material, does not change its catalytic activity even after being used for 40 hours. Although not shown in FIG. 6, no change in photocatalytic activity was observed even after use for 50 hours or more.
【0059】このように寿命が長い理由は、下式に示す
硫化亜鉛が自由ホールによって酸化される溶解反応より
も、 ZnS+2h+ →Zn2++S 下式に示す、硫化ナトリウムが自由ホールによって酸化
される酸化反応の方が生じ易いため、 Na2 S+2h+ →2Na+ +S 硫化亜鉛に代わって、硫化ナトリウムが酸化され、硫化
亜鉛微粒子層状物質が溶出するのを防いでいるためであ
る。The reason why the lifetime is long is that ZnS + 2h + → Zn 2+ + S, as shown in the following equation, oxidizes sodium sulfide by free holes rather than the dissolution reaction in which zinc sulfide shown below is oxidized by free holes. Na 2 S + 2h + → 2Na + + S In place of zinc sulfide, sodium sulfide is oxidized to prevent the zinc sulfide fine particle layered material from being eluted.
【0060】すなわち、硫化ナトリウム(Na2 S)水
溶液を、硫化亜鉛微粒子層状物質から成る光触媒の犠牲
還元剤として用いれば、光触媒の寿命が長くなる。That is, when an aqueous solution of sodium sulfide (Na 2 S) is used as a sacrificial reducing agent for a photocatalyst composed of a layered material of zinc sulfide fine particles, the life of the photocatalyst is prolonged.
【0061】また、硫化亜鉛(ZnS)は、よく知られ
ているように毒性はない。従って、本発明の光触媒であ
る硫化亜鉛微粒子層状物質(ストラティファイドZnS
ナノ微粒子光触媒)は毒性がない。As is well known, zinc sulfide (ZnS) has no toxicity. Therefore, the zinc sulfide fine particle layered material (Stratified ZnS) which is the photocatalyst of the present invention is used.
Nanoparticulate photocatalyst) is non-toxic.
【0062】また本発明の光触媒である硫化亜鉛微粒子
層状物質は、前述したように貴金属を使用しないので、
廉価である。Since the zinc sulfide fine particle layered material as the photocatalyst of the present invention does not use a noble metal as described above,
It is cheap.
【0063】次に、本発明の光触媒使用方法の実施の形
態にかかる、本発明の光触媒である硫化亜鉛微粒子層状
物質を用いて、硫化水素を分解し、水素及びイオウを製
造する方法について説明する。Next, a method for producing hydrogen and sulfur by decomposing hydrogen sulfide using the layered material of fine particles of zinc sulfide as the photocatalyst according to the embodiment of the photocatalyst use method of the present invention will be described. .
【0064】この方法は下記の工程よりなる。 (イ)苛性ソーダ水溶液に硫化水素を溶解する工程。 (ロ)(イ)の工程後の溶液に光触媒を加え、紫外線を
照射し、水素ガスを回収する工程。 (ハ)(ロ)の工程後の該溶液からイオウを回収する工
程。 (ニ)(ハ)の工程後の該溶液を(イ)の工程の苛性ソ
ーダ水溶液として再利用する工程。This method comprises the following steps. (A) A step of dissolving hydrogen sulfide in an aqueous solution of caustic soda. (B) A step of adding a photocatalyst to the solution after the step (a), irradiating the solution with ultraviolet rays, and collecting hydrogen gas. (C) recovering sulfur from the solution after the step (b). (D) a step of reusing the solution after the step (c) as the aqueous caustic soda solution of the step (a).
【0065】上記工程の構成を模式的に表した図7を用
いてこの方法を説明する。図7において、15は苛性ソ
ーダ水溶液16を保持し、硫化水素ガスをバブリング等
により溶かし込むためのアルカリ溶解槽であり、(イ)
の工程を行う部分である。17は(イ)の工程によって
硫化水素を溶解させた苛性ソーダ水溶液16を保持し、
光触媒12を保持し、この光触媒12に外から紫外線1
1を照射できるように透明な底面を有し、かつ、発生す
る水素ガスを回収するようにした光触媒反応槽であり、
(ロ)の工程を行う部分である。18は(ロ)の工程に
よって光触媒反応槽17で光分解反応の完了した溶液1
6からイオウ(S)を回収する硫黄回収槽であり、
(ハ)の工程を行う部分である。10はこの光触媒12
を光触媒反応槽17の外から紫外線照射するように配置
した光源であり、11は紫外線である。This method will be described with reference to FIG. 7, which schematically shows the structure of the above steps. In FIG. 7, reference numeral 15 denotes an alkali dissolution tank for holding a caustic soda aqueous solution 16 and dissolving hydrogen sulfide gas by bubbling or the like.
This is the part where the process is performed. 17 holds the caustic soda aqueous solution 16 in which hydrogen sulfide is dissolved in the step (a),
The photocatalyst 12 is held, and ultraviolet light 1
1 is a photocatalytic reaction tank having a transparent bottom surface so as to be able to irradiate 1, and collecting the generated hydrogen gas;
This is a part for performing the step (b). Reference numeral 18 denotes the solution 1 in which the photolysis reaction has been completed in the photocatalyst
It is a sulfur recovery tank that recovers sulfur (S) from 6,
This is the part where the step (c) is performed. 10 is the photocatalyst 12
Is a light source arranged to irradiate ultraviolet light from outside the photocatalytic reaction tank 17, and 11 is ultraviolet light.
【0066】次に、図7の構成における動作について説
明する。(イ)の工程。アルカリ溶解槽15において、
硫化水素を溶け込ませると、苛性ソーダ水溶液16は次
式に示す反応により硫化ナトリウム水溶液16になる。 2NaOH +H2 S →← 2Na+ +HS- +H2
O +OH- 2Na+ +HS- +OH- →← Na2 S +H2 ONext, the operation in the configuration of FIG. 7 will be described. Step (a). In the alkali dissolution tank 15,
When hydrogen sulfide is dissolved, the aqueous caustic soda solution 16 becomes an aqueous sodium sulfide solution 16 by a reaction represented by the following equation. 2NaOH + H 2 S → ← 2Na + + HS - + H 2
O + OH - 2Na + + HS - + OH - → ← Na 2 S + H 2 O
【0067】(ロ)の工程。この硫化ナトリウム水溶液
16を光触媒反応槽17に移し、光源10からの紫外線
11により光触媒12を光照射すると、自由電子、自由
ホールが生成し、次式に示す反応により硫化ナトリウム
水溶液16を酸化還元し、水素ガスとイオウを生成す
る。水素ガスは、発生と同時に回収する。 Na2 S + H2 O →← 2Na+ + HS- +
OH- HS- + 2h+ → S + H+ 2H+ + 2e- → H2 ↑Step (b). When the aqueous sodium sulfide solution 16 is transferred to the photocatalyst reaction tank 17 and the photocatalyst 12 is irradiated with the ultraviolet light 11 from the light source 10, free electrons and free holes are generated, and the sodium sulfide aqueous solution 16 is oxidized and reduced by a reaction represented by the following formula. Produces hydrogen gas and sulfur. Hydrogen gas is recovered as it is generated. Na 2 S + H 2 O → ← 2Na + + HS - +
OH - HS - + 2h + → S + H + 2H + + 2e - → H 2 ↑
【0068】(ハ)及び(ニ)の工程。この硫化ナトリ
ウム水溶液16は、酸化還元反応が終了すると、すなわ
ち、全てのイオウイオンがイオウに還元されると、上式
から明らかな通り、イオウを含む苛性ソーダ水溶液16
となる。この苛性ソーダ水溶液16をイオウ回収槽18
に移し、イオウを回収し、イオウの無くなったこの苛性
ソーダ水溶液16をアルカリ溶解槽15に戻し、再び
(イ)の工程の苛性ソーダ水溶液16として用いる。Steps (c) and (d). When the oxidation-reduction reaction is completed, that is, when all the sulfur ions are reduced to sulfur, the sodium sulfide aqueous solution 16 containing sulfur as shown in the above formula is used.
Becomes This caustic soda aqueous solution 16 is supplied to a sulfur recovery tank 18.
Then, the sulfur is recovered, and the aqueous caustic soda solution 16 having no sulfur is returned to the alkali dissolving tank 15 and used again as the aqueous caustic soda solution 16 in the step (a).
【0069】したがって、本発明の光触媒使用方法の実
施の形態にかかる、本発明の光触媒である硫化亜鉛微粒
子層状物質を用いて、硫化水素を分解し、水素及びイオ
ウを製造する方法を用いれば、上記で述べたように、環
境有害物質である硫化水素を紫外線光源に必要なエネル
ギー以外なにも必要とせずに、また有害物質をなにも発
生させずに分解し、有用物質である水素とイオウを製造
することができる。Therefore, according to the embodiment of the method for using a photocatalyst of the present invention, the method of decomposing hydrogen sulfide using the zinc sulfide fine particle layered material as the photocatalyst of the present invention to produce hydrogen and sulfur is used. As described above, hydrogen sulfide, which is an environmentally harmful substance, is decomposed without requiring any other energy than the energy required for an ultraviolet light source and without generating any harmful substance, and hydrogen, which is a useful substance, is decomposed. Sulfur can be produced.
【0070】[0070]
【発明の効果】以上の説明から理解されるように、本発
明の光触媒は、光触媒としての触媒活性が高く、毒性が
なく、廉価で寿命が長い。そして、本発明の、硫化水素
を分解し水素とイオウを製造する方法を用いれば、環境
問題の解決に寄与し、かつ、有用物質を安く生産できる
等々の実用的効果も奏し得る。As will be understood from the above description, the photocatalyst of the present invention has high catalytic activity as a photocatalyst, has no toxicity, is inexpensive and has a long life. The use of the method of the present invention for decomposing hydrogen sulfide to produce hydrogen and sulfur can contribute to solving environmental problems, and can also provide practical effects such as production of useful substances at low cost.
【図1】本発明光触媒の構造を示す構造模式図である。FIG. 1 is a schematic structural view showing the structure of a photocatalyst of the present invention.
【図2】(A)は本発明の光触媒構造の電子顕微鏡写真
の模写図、(B)は原料である酸化亜鉛粒子の電子顕微
鏡写真の模写図である。FIG. 2A is an electron micrograph of a photocatalyst structure of the present invention, and FIG. 2B is an electron micrograph of zinc oxide particles as a raw material.
【図3】(A)は本発明による光触媒の生成課程を示す
電子顕微鏡写真の模写図、(B)はその構造模式図であ
る。FIG. 3A is a simulated view of an electron micrograph showing a process of producing a photocatalyst according to the present invention, and FIG. 3B is a schematic structural view thereof.
【図4】本発明の光触媒と従来の光触媒の性能比較図で
ある。FIG. 4 is a performance comparison diagram of the photocatalyst of the present invention and a conventional photocatalyst.
【図5】図4の性能比較に用いた装置の構成図である。FIG. 5 is a configuration diagram of an apparatus used for performance comparison of FIG. 4;
【図6】本発明光触媒の寿命を示す特性図である。FIG. 6 is a characteristic diagram showing the life of the photocatalyst of the present invention.
【図7】本発明の実施の形態による、硫化水素を分解し
水素及びイオウを製造する方法の工程図である。FIG. 7 is a process diagram of a method for decomposing hydrogen sulfide to produce hydrogen and sulfur according to an embodiment of the present invention.
【図8】図2(A)に示す模写図に対応する本発明の光
触媒の電子顕微鏡写真である。FIG. 8 is an electron micrograph of the photocatalyst of the present invention corresponding to the schematic diagram shown in FIG. 2 (A).
【図9】図2(B)に示す模写図に対応する本発明の光
触媒の原料である酸化亜鉛粒子の電子顕微鏡写真であ
る。FIG. 9 is an electron micrograph of zinc oxide particles as a raw material of the photocatalyst of the present invention corresponding to the schematic diagram shown in FIG. 2 (B).
【図10】図3(A)に示す模写図に対応する光触媒の
生成途中を示す電子顕微鏡写真である。10 is an electron micrograph showing a photocatalyst in the course of generation corresponding to the mimic diagram shown in FIG. 3 (A).
【図11】従来技術による原油の脱硫工程図である。FIG. 11 is a diagram of a crude oil desulfurization process according to the prior art.
【符号の説明】 1 硫化亜鉛微粒子層から成る外殻 2 空洞 3 穴 4 酸化亜鉛粒子 5 雲状物質 6 光反応部分 7 水素定量部分 8 硫化ナトリウム水溶液 9 溶液溜 10 500W水銀灯 11 紫外線 12 光触媒 13 反射鏡 14 発生ガス回収口 15 アルカリ溶解槽 16 苛性ソーダ水溶液、又は硫化ナトリウム水溶液、
又はイオウを含む苛性ソーダ水溶液 17 光触媒反応槽 18 硫黄回収槽[Description of Signs] 1 Outer shell composed of zinc sulfide fine particle layer 2 Cavity 3 Hole 4 Zinc oxide particle 5 Cloud material 6 Photoreactive part 7 Hydrogen quantitative part 8 Sodium sulfide aqueous solution 9 Solution reservoir 10 500W mercury lamp 11 Ultraviolet 12 Photocatalyst 13 Reflection Mirror 14 generated gas recovery port 15 alkali dissolving tank 16 caustic soda aqueous solution or sodium sulfide aqueous solution,
Or caustic soda aqueous solution containing sulfur 17 photocatalytic reaction tank 18 sulfur recovery tank
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/32 B01D 53/36 ZABJ (72)発明者 柳澤 恒徳 宮城県仙台市青葉区荒巻字青葉01 東北大 学内 (72)発明者 荒井 健男 宮城県仙台市青葉区荒巻字青葉01 東北大 学内 (72)発明者 咲間 修平 宮城県仙台市青葉区荒巻字青葉01 東北大 学内 (72)発明者 粕谷 厚生 宮城県仙台市青葉区荒巻字青葉01 東北大 学内 Fターム(参考) 4D037 AA15 AB13 BA18 BB09 4D048 AA22 AB01 AB03 BA16X BA46X BB12 BB16 BB17 EA01 4G069 AA02 AA03 AA08 AA09 AA11 BA48A BA48C BB09A BB09B BB09C BC35A BC35B BC35C BD08A BD08B BD08C BD09A BD10A CA02 CA03 CA07 CA10 CA17 CB81 DA05 EA01X EA01Y EA02X EA02Y EB10 EB18X EB18Y EC29 FB50──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/32 B01D 53/36 ZABJ (72) Inventor Tsunetori Yanagisawa 01 Aoba Aramaki Aoba-ku, Aoba-ku, Sendai City, Miyagi Prefecture. Tohoku University Campus (72) Inventor Takeo Arai 01 Aoba Aramaki, Aoba Ward, Sendai City, Miyagi Prefecture Tohoku University Campus (72) Inventor Shuhei Sakima Aramaki Aoba 01 Aoba Ward, Aoba Ward, Sendai City, Miyagi Prefecture Tohoku Univ. Welfare 01 Aoba, Aramaki, Aoba-ku, Sendai-shi, Miyagi F-term (reference) 4D037 AA15 AB13 BA18 BB09 4D048 AA22 AB01 AB03 BA16X BA46X BB12 BB16 BB17 EA01 4G069 AA02 AA02 AA03 AA08 AA09 BC48AB BCB BCB BCBA BCB BC BD08C BD09A BD10A CA02 CA03 CA07 CA10 CA17 CB81 DA05 EA01X EA01Y EA02X EA02Y EB10 EB18X EB18Y EC29 FB50
Claims (14)
の層の厚み方向に、該化合物の成分比が変化しているこ
とを特徴とする光触媒。1. A photocatalyst wherein compound semiconductor fine particles are aggregated in a layer, and the component ratio of the compound changes in the thickness direction of the layer.
nmの粒径を有することを特徴とする、請求項1記載の
光触媒。2. The method according to claim 1, wherein the compound semiconductor fine particles are 5 to 10
2. The photocatalyst according to claim 1, having a particle size of nm.
この外殻は穴を有していることを特徴とする、請求項1
記載の光触媒。3. An outer shell comprising the layered assembly,
2. The shell according to claim 1, wherein said shell has a hole.
The photocatalyst as described.
セル形状又は球形状であることを特徴とする、請求項3
記載の光触媒。4. An outer shape of the photocatalyst having the outer shell is a capsule shape or a spherical shape.
The photocatalyst as described.
半導体であることを特徴とする、請求項1又は請求項3
記載の光触媒。5. The compound semiconductor according to claim 1, wherein the compound semiconductor is a II-VI group compound semiconductor.
The photocatalyst as described.
を特徴とする、請求項1又は請求項3記載の光触媒。6. The photocatalyst according to claim 1, wherein the compound semiconductor is zinc sulfide.
I族元素の酸化物粒子を、イオウイオンを含む水溶液中
で溶解し、生成するII族元素の硫化物をこの酸化物粒
子上に析出して生成する、光触媒の製造方法。7. I constituting a II-VI compound semiconductor
A method for producing a photocatalyst, comprising dissolving oxide particles of a group I element in an aqueous solution containing sulfur ions and depositing and generating a sulfide of a group II element formed on the oxide particles.
であることを特徴とする、請求項7記載の光触媒の製造
方法。8. The method for producing a photocatalyst according to claim 7, wherein the oxide particles of the group II element are zinc oxide.
とを混合する工程と、この混合液を攪拌する工程とから
なる、請求項8の光触媒の製造方法。9. The method for producing a photocatalyst according to claim 8, comprising a step of mixing the zinc oxide fine particles with an aqueous solution of sodium sulfide, and a step of stirring the mixture.
液とを混合する工程と、この混合液に紫外線を照射しな
がら攪拌する工程とからなる、請求項8の光触媒の製造
方法。10. The method for producing a photocatalyst according to claim 8, comprising a step of mixing the zinc oxide fine particles and an aqueous solution of sodium sulfide, and a step of stirring the mixture while irradiating the mixture with ultraviolet rays.
液とを混合する工程と、この混合液に硫化水素をバブリ
ングしながら攪拌する工程と、硫化水素ガスを止め、さ
らに一定時間攪拌する工程とからなる請求項8の光触媒
の製造方法。11. A method comprising: mixing zinc oxide fine particles and an aqueous solution of sodium sulfide; stirring hydrogen sulfide while bubbling the mixture; stopping hydrogen sulfide gas, and further stirring for a certain period of time. Item 10. A method for producing a photocatalyst according to Item 8.
液とを混合する工程と、この混合液に紫外線を照射し、
かつ、硫化水素をバブリングする工程とからなる、請求
項8の光触媒の製造方法。12. A step of mixing zinc oxide fine particles and an aqueous solution of sodium sulfide, and irradiating the mixed liquid with ultraviolet rays.
9. The method for producing a photocatalyst according to claim 8, comprising a step of bubbling hydrogen sulfide.
載の硫化亜鉛からなる光触媒の犠牲還元剤として用い
る、光触媒使用方法。13. A method for using a photocatalyst, wherein an aqueous solution of sodium sulfide is used as a sacrificial reducing agent for the photocatalyst comprising zinc sulfide according to claim 6.
の光触媒使用方法。 (イ)苛性ソーダ水溶液に硫化水素を溶解する工程、
(ロ)該溶液に光触媒を加え、紫外線を照射し、水素ガ
スを回収する工程、(ハ)(ロ)の工程後の該溶液から
イオウを回収する工程、(ニ)(ハ)の工程後の該溶液
を(イ)の工程の苛性ソーダ水溶液として再利用する工
程。14. The method for using a photocatalyst according to claim 13, comprising the following steps. (A) dissolving hydrogen sulfide in caustic soda aqueous solution,
(B) adding a photocatalyst to the solution, irradiating ultraviolet rays to recover hydrogen gas, (c) recovering sulfur from the solution after the step (b), (d) after the step (c) Recycling the solution as the aqueous solution of caustic soda in the step (a).
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002083308A1 (en) * | 2001-04-11 | 2002-10-24 | Japan Science And Technology Corporation | Method for preparing high active photocatalyst and method for treating hydrogen sulfide using the high active photocatalyst |
| WO2003051512A1 (en) * | 2001-12-19 | 2003-06-26 | Japan Science And Technology Corporation | Thin-film photocatalyst, its production method, hydrogen sulfide processing method using the thin-film optical catalyst, and hydrogen producing method |
| WO2003078061A1 (en) * | 2002-03-18 | 2003-09-25 | Nittetsu Mining Co., Ltd. | Photocatalyst and process for producing the same |
| WO2004000459A1 (en) | 2002-06-25 | 2003-12-31 | Nittetsu Mining Co., Ltd. | Highly active photocatalyst and process for producing the same |
| US6964755B2 (en) * | 2000-09-01 | 2005-11-15 | Japan Science And Technology Agency | Method for producing high activity photocatalyst, photoactivity catalyst, and method for treating hydrogen sulfide for recovering hydrogen gas under low energy by using high activity photocatalyst |
| US7985397B2 (en) | 2005-03-31 | 2011-07-26 | Nittetsu Mining Co., Ltd. | Method of treating hydrogen sulfide, method of producing hydrogen, and photocatalytic-reaction apparatus |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59128339A (en) * | 1983-01-05 | 1984-07-24 | Shozo Yanagida | Photocatalyst reaction using zinc sulfide |
| JPS6265743A (en) * | 1985-09-14 | 1987-03-25 | Agency Of Ind Science & Technol | Zinc compound having photocatalytic activity |
| JPH08224289A (en) * | 1995-02-23 | 1996-09-03 | Mitsui Mining & Smelting Co Ltd | Antibacterial / deodorant |
| JPH08291280A (en) * | 1995-04-21 | 1996-11-05 | Ykk Kk | Watertight airtight material for construction |
| JPH1071337A (en) * | 1996-08-29 | 1998-03-17 | Bridgestone Corp | Photocatalyst and its production |
-
2000
- 2000-01-06 JP JP2000005812A patent/JP4496444B2/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59128339A (en) * | 1983-01-05 | 1984-07-24 | Shozo Yanagida | Photocatalyst reaction using zinc sulfide |
| JPS6265743A (en) * | 1985-09-14 | 1987-03-25 | Agency Of Ind Science & Technol | Zinc compound having photocatalytic activity |
| JPH08224289A (en) * | 1995-02-23 | 1996-09-03 | Mitsui Mining & Smelting Co Ltd | Antibacterial / deodorant |
| JPH08291280A (en) * | 1995-04-21 | 1996-11-05 | Ykk Kk | Watertight airtight material for construction |
| JPH1071337A (en) * | 1996-08-29 | 1998-03-17 | Bridgestone Corp | Photocatalyst and its production |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6964755B2 (en) * | 2000-09-01 | 2005-11-15 | Japan Science And Technology Agency | Method for producing high activity photocatalyst, photoactivity catalyst, and method for treating hydrogen sulfide for recovering hydrogen gas under low energy by using high activity photocatalyst |
| WO2002083308A1 (en) * | 2001-04-11 | 2002-10-24 | Japan Science And Technology Corporation | Method for preparing high active photocatalyst and method for treating hydrogen sulfide using the high active photocatalyst |
| WO2003051512A1 (en) * | 2001-12-19 | 2003-06-26 | Japan Science And Technology Corporation | Thin-film photocatalyst, its production method, hydrogen sulfide processing method using the thin-film optical catalyst, and hydrogen producing method |
| WO2003078061A1 (en) * | 2002-03-18 | 2003-09-25 | Nittetsu Mining Co., Ltd. | Photocatalyst and process for producing the same |
| US7704914B2 (en) | 2002-03-18 | 2010-04-27 | Nittetsu Mining Co., Ltd. | Photocatalyst and process for producing the same |
| WO2004000459A1 (en) | 2002-06-25 | 2003-12-31 | Nittetsu Mining Co., Ltd. | Highly active photocatalyst and process for producing the same |
| CN100357028C (en) * | 2002-06-25 | 2007-12-26 | 日铁矿业株式会社 | Highly active photocatalyst and process for producing the same |
| EA009448B1 (en) * | 2002-06-25 | 2007-12-28 | Ниттецу Майнинг Ко., Лтд. | PHOTOCATALIZER WITH HIGH ACTIVITY AND METHOD FOR ITS OBTAINING |
| US7608557B2 (en) | 2002-06-25 | 2009-10-27 | Nittetsu Mining Co., Ltd. | Highly active photocatalyst and process for producing the same |
| US7985397B2 (en) | 2005-03-31 | 2011-07-26 | Nittetsu Mining Co., Ltd. | Method of treating hydrogen sulfide, method of producing hydrogen, and photocatalytic-reaction apparatus |
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| JP4496444B2 (en) | 2010-07-07 |
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