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JP4496444B2 - Photocatalyst, method for producing the same, and method for decomposing hydrogen sulfide using the photocatalyst - Google Patents
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JP4496444B2 - Photocatalyst, method for producing the same, and method for decomposing hydrogen sulfide using the photocatalyst - Google Patents

Photocatalyst, method for producing the same, and method for decomposing hydrogen sulfide using the photocatalyst Download PDF

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JP4496444B2
JP4496444B2 JP2000005812A JP2000005812A JP4496444B2 JP 4496444 B2 JP4496444 B2 JP 4496444B2 JP 2000005812 A JP2000005812 A JP 2000005812A JP 2000005812 A JP2000005812 A JP 2000005812A JP 4496444 B2 JP4496444 B2 JP 4496444B2
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photocatalyst
sulfide
zinc
solution
fine particle
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JP2001190964A (en
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和幸 田路
恒徳 柳澤
健男 荒井
修平 咲間
厚生 粕谷
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Dowa Holdings Co Ltd
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Dowa Holdings Co Ltd
Dowa Mining Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

【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硫化水素の分解方法に関するものである。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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硫化水素の分解方法を提供することを目的とする。
【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、硫化亜鉛からなる5から10nmの粒径を有する化合物半導体微粒子が層状に集合し、この層状の集合体から成る外殻と空洞とを有し、かつ、この外殻は穴を有しており、この層の厚み方向に、硫化亜鉛の成分である亜鉛(Zn)と硫黄(S)の成分比が変化していることを特徴とする光触媒である。好適には、外殻の形状がカプセル状又は球形状である。
【0013】
さらに、この光触媒を製造するには、酸化亜鉛からなる酸化物粒子を、イオウイオンを含む水溶液中で溶解し、生成する亜鉛の硫化物微粒子を、この酸化亜鉛からなる酸化物粒子上に析出させて製造する
【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。
【0016】
この発明の硫化亜鉛からなる光触媒を用いた硫化水素の分解方法は、本発明の光触媒を使用して、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)該溶液に硫化亜鉛からなる光触媒を加え、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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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 Dispersive 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。
【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。
【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。
【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。
【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。
【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(ZnO)が、酸化亜鉛粒子4の表面から、亜鉛酸イオン(ZnO2-)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。
【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。
【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。
【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。
【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。
【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(Na2 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0.1μm)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(Na2 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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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11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16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。
【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
【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
【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。
【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。
【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。
【図面の簡単な説明】
【図1】本発明光触媒の構造を示す構造模式図である。
【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。
【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。
【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。
【図5】図4の性能比較に用いた装置の構成図である。
【図6】本発明光触媒の寿命を示す特性図である。
【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。
【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。
【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。
【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。
【図11】従来技術による原油の脱硫工程図である。
【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
[0001]
BACKGROUND OF THE INVENTION
The present invention is used in the chemical industry field that produces a useful chemical substance using a photocatalyst, and in the environmental conservation field that removes malodorous substances and air pollutants using a photocatalyst. To produce sulfur and sulfur, a method for producing the photocatalyst, and the photocatalystTheHydrogen sulfideDecompositionIt is about the method.
[0002]
[Prior art]
The application of photocatalyst technology promotes various chemical reactions such as decomposition of environmental pollutants, malodorous components and bacteria, so it can be used for antibacterial tiles and antibacterial / deodorizing filters for air cleaners. Has begun.
On the other hand, there are studies aimed at obtaining hydrogen by causing photocatalysts to act on water and the like, but the application of photocatalytic 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 may be applied to a crude oil desulfurization process.
[0003]
FIG. 11 shows a crude oil desulfurization process which is generally performed at present.
As shown in FIG. 11, when crude oil is distilled, heavy naphtha is hydrogenated and all sulfur components contained in the crude oil are recovered as hydrogen sulfide. This hydrogen sulfide passes through a process called the Claus method and oxidizes and recovers sulfur. The Claus method is a process in which one third of hydrogen sulfide is oxidized to sulfurous acid gas, and this is reacted with the remaining hydrogen sulfide to form elemental sulfur.
[0004]
In this process, enormous energy is required not only for the catalytic reaction of sulfurous acid gas and hydrogen sulfide, but also for repeated heating and condensation. In addition, there is a problem such as costly management of sulfurous acid gas.
[0005]
A photocatalyst is added to alkaline water in which hydrogen sulfide is dissolved, and ultraviolet light is irradiated. The free water and free holes generated by the photocatalyst are absorbed by the ultraviolet light, and the alkaline water in which hydrogen sulfide is dissolved is oxidized and reduced. If a method for obtaining hydrogen and sulfur by decomposing hydrogen sulfide with a photocatalyst and producing hydrogen and sulfur can be put to practical use, hydrogen sulfide which is a harmful substance can be decomposed with much less energy, and hydrogen and sulfur which are useful substances Can be produced. That is, it contributes to solving environmental problems and can produce useful substances at low cost.
[0006]
However, conventional photocatalysts have the following problems to be solved in order to use them for the purpose of decomposing hydrogen sulfide and obtaining hydrogen and sulfur.
First, the catalytic activity is low.
Second, the photocatalyst is toxic.
Third, it uses a promoter such as a noble metal and is expensive.
[0007]
When the photocatalyst is irradiated with light, free electrons and free holes are generated, but the probability of recombination is high, and the probability that the chemical substance decomposed by the redox reaction will recombine and return to the original compound. The catalytic activity is low. For this reason, conventionally, a decrease in catalytic activity is prevented by supporting a noble metal on a part of the surface of the photocatalyst. For example, a titanium oxide TiO 2 photocatalyst carries platinum (Pt) on a part of its surface to increase the catalytic activity, but this makes the catalyst expensive.
[0008]
Fourth, the life of the catalyst is short.
When photocatalyst is irradiated with light, free electrons and free holes are generated, but due to its strong redox reaction, the catalyst itself is oxidized and reduced in addition to the target chemical substance and dissolved, resulting in loss of catalytic action. There is a problem. For this reason, a substance called a sacrificial reducing agent is generally used to prevent dissolution of the catalyst, but a combination of a photocatalyst and a sacrificial reducing agent having a practically sufficient lifetime has not yet been obtained.
[0009]
[Problems to be solved by the invention]
As described above, conventional photocatalysts have problems to be solved such as low catalytic activity, toxicity, high cost, and short life, and environment such as production of useful chemicals and removal of air pollutants. It is still insufficient for use for conservation purposes.
[0010]
  Therefore, in view of the above problems, the present invention uses a new photocatalyst having high catalytic activity, non-toxicity, low cost and long life, its production method, and its photocatalyst.TheHydrogen sulfideDecompositionIt aims to provide a method.
[0011]
[Means for Solving the Problems]
  In order to achieve the above object, the invention of the photocatalyst of the present invention is:Having a particle size of 5 to 10 nm made of zinc sulfideCompound semiconductor fine particles gather in layers,An outer shell composed of this layered assembly and a cavity, and the outer shell has a hole;In the thickness direction of this layer,Zinc (Zn) and sulfur (S), components of zinc sulfideThe photocatalyst is characterized in that the component ratio ofThePreferably, the outer shell has a capsule shape or a spherical shape.
[0013]
  Furthermore, to produce this photocatalyst,Made of zinc oxideDissolve the oxide particles in an aqueous solution containing sulfur ions,Generated zincOf sulfide fine particlesOn the oxide particles made of zinc oxidePrecipitate and manufacture.
[0014]
This photocatalyst production method is optimally a photocatalyst production method comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, and a step of stirring this mixed solution. Furthermore, it is a method for producing a photocatalyst comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, and a step of stirring the mixture while irradiating ultraviolet rays. Furthermore, the production of a photocatalyst comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, a step of stirring while bubbling hydrogen sulfide into the mixed solution, and a step of stopping the hydrogen sulfide gas and further stirring for a predetermined time. Is the method. Furthermore, it is a method for producing a photocatalyst comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, and a step of irradiating the mixture with ultraviolet rays and bubbling hydrogen sulfide.
[0016]
  Of this inventionMade of zinc sulfidephotocatalystOf hydrogen sulfide using waterThe method comprises the following steps using the photocatalyst of the present invention.
(A) A step of dissolving hydrogen sulfide in an aqueous caustic soda solution.
(B) In the solutionMade of zinc sulfideA process of collecting hydrogen gas by adding a photocatalyst and irradiating it with ultraviolet rays.
(C) A step of recovering sulfur from the solution after the step (B).
(D) A step of reusing the solution after step (c) as the aqueous caustic soda solution of step (a).
[0017]
Next, 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 an electric field in the layer thickness direction because the ratio of the number of zinc atoms to the number of sulfur atoms in the zinc sulfide, that is, the component ratio, changes in the thickness direction of the layer. Has occurred. For this reason, free electrons and free holes generated by light irradiation move away from each other. This reduces the recombination of free electrons and free holes, and also separates the reaction site for the oxidation reaction and the reaction site for the reduction reaction, thereby reducing the recombination of the oxidation reaction product and the reduction reaction product. .
[0018]
As a result, free electrons and free holes generated by light irradiation are effectively used for the target oxidation-reduction reaction, so that the zinc sulfide fine particle layer of the present invention has high photocatalytic activity.
[0019]
Next, features of the photocatalyst production method of the present invention will be described.
When zinc oxide fine particles as a raw material are mixed with a sodium sulfide aqueous solution and this mixed solution is stirred, zinc oxide reacts with water to become zincate ions and is eluted into the aqueous solution. This zincate ion reacts with sulfur ions in the aqueous sodium sulfide solution to become zinc sulfide. This zinc sulfide is deposited on the surface of zinc oxide particles as a raw material 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 zinc oxide as a raw material, reacts with zinc oxide, and generates zincate ions. The zincate ions diffuse through the zinc sulfide fine particle layer, reach the surface, react with sulfur ions, become zinc sulfide, and deposit 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 having a composition deviating from the stoichiometric ratio is deposited.
[0020]
Ultraviolet irradiation is effective for increasing the formation rate of the zinc sulfide fine particle layer. That is, if zinc oxide fine particles and an aqueous solution of sodium sulfide are mixed and irradiated with ultraviolet rays, zinc oxide is photodissolved, so that zincate ions are easily eluted and the growth of the zinc sulfide fine particle layer is accelerated.
[0021]
In order to increase the production rate of the zinc sulfide fine particle layer, dissolution of hydrogen sulfide is effective. That is, when hydrogen sulfide is dissolved in a mixed solution of zinc oxide fine particles and water, a weakly acidic solution containing sulfur ions is obtained, and zinc oxide is well dissolved in the weakly acidic solution, so that the growth of the zinc sulfide fine particle layer is similarly accelerated.
[0022]
In order to increase the generation rate of the zinc sulfide fine particle layer, ultraviolet irradiation and hydrogen sulfide dissolution 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, the growth of the zinc sulfide fine particle layer is further accelerated.
[0023]
By these methods described above, the zinc sulfide fine particle layer which is the photocatalyst of the present invention can be produced.
[0024]
Next, the method for using the photocatalyst of the present invention will be described.
When using a zinc sulfide fine particle layer that is a photocatalyst of the present invention, if a sodium sulfide aqueous solution is used as a sacrificial reducing agent, sodium in the sodium sulfide aqueous solution is oxidized in place of zinc in the zinc sulfide fine particle layer. Zinc in the zinc fine particle layer can be prevented from eluting into the aqueous solution, and the photocatalytic properties of the zinc sulfide fine particle layer do not deteriorate.
[0025]
Next, of the photocatalyst use method of the present invention, the characteristics of a 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 effective as a sacrificial reducing agent are produced. When the zinc sulfide fine particle layer of the present invention is added to this solution and irradiated with ultraviolet rays, hydrogen gas and sulfur are produced. If hydrogen gas and sulfur are recovered, the solution returns to caustic soda. This solution can be reused in caustic soda for dissolving hydrogen sulfide.
[0026]
If this method is used, hydrogen sulfide can be decomposed and hydrogen and sulfur can be obtained without requiring anything other than energy necessary for the ultraviolet light source.
[0027]
DETAILED DESCRIPTION OF THE INVENTION
The preferred embodiments of the photocatalyst, the method for producing the same, and the method for using the photocatalyst according to the present invention will be described below with reference to FIGS.
[0028]
Among the photocatalysts of the present invention, the structure of a photocatalyst in which the compound semiconductor is a II-VI group compound semiconductor and the II-VI group compound semiconductor is zinc sulfide, that is, a zinc sulfide fine particle layered substance will be described with reference to FIG. .
FIG. 1 is a structural schematic diagram 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 a zinc sulfide fine particle layered material, and FIG. 1B is a schematic diagram of a cross section in the direction indicated by the arrow in FIG.
[0029]
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), a zinc sulfide fine particle layered substance that is a photocatalyst according to the present invention comprises an outer shell 1 composed of a zinc sulfide (ZnS) fine particle layer having a particle diameter of 5 nm to 10 nm, The outer shell 1 has a cavity 2 and a hole 3.
Further, the zinc sulfide fine particle layered material has an outer shell reflecting the outer shape of the zinc oxide particles as the raw material.
Feature (2): The zinc sulfide fine particle layer which is a photocatalyst according to the present invention has a structure in which the component ratio of zinc (Zn) and sulfur (S) is changed in the layer thickness direction.
[0030]
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]
Feature (1) will be described with reference to FIG.
FIG. 2A shows a transmission electron photographed by irradiating an electron beam from the direction perpendicular to the cross section of FIG. 1B to the Y direction of FIG. It is a copy figure of a microscope picture (this photograph is shown as FIG. 8). A black portion 1 and a gray portion 1 seen in FIG. 2A correspond to the edges and surfaces of the rectangular parallelepiped in FIG.
[0032]
As shown in FIG. 2 (A), the black portion 1 and the gray portion 1 are measured by using a micro area EDX (Energy Dispersive X-ray Spectroscopy). As a result, both of the zinc sulfide fine particles having a particle diameter of 5 nm to 10 nm are measured. Confirmed to be a layer. The difference in the intensity of the transmission electron beam between the edge and the surface of the rectangular parallelepiped made of the same material indicates that there is a cavity inside the rectangular parallelepiped.
[0033]
That is, the zinc sulfide fine particle layered substance which is a photocatalyst according to the present invention includes an outer shell 1 composed of a zinc sulfide (ZnS) fine particle layer having a particle diameter of 5 nm to 10 nm and a cavity as shown in the schematic diagram of FIG. 2, and the outer shell 1 has a hole 3.
[0034]
FIG. 2B is a copy of a scanning electron micrograph (this photograph is shown in FIG. 9) of the raw material zinc oxide particles 4 used to produce the zinc sulfide fine particle layered material. As is clear from this figure, the zinc sulfide fine particle layered substance which is a photocatalyst according to the present invention has an outer shape reflecting the shape of the zinc oxide particles used as a raw material. In this example, the shape of the rectangular parallelepiped is shown, but it may be a capsule shape or a spherical shape.
[0035]
In addition, the zinc sulfide fine particle layered material which is the photocatalyst according to the present invention used in the transmission electron micrograph is the same as the zinc sulfide fine particle layered material produced by the production method described in the embodiment of the method for producing the photocatalyst of the present invention. .1 molar sodium sulfide (Na2S) In addition to the aqueous solution, the photodecomposition reaction was caused by ultraviolet irradiation for 50 hours.
[0036]
The feature (2) will be described with reference to FIG.
FIG. 3A is a copy of a transmission electron micrograph (this photograph is shown in FIG. 10) obtained by photographing the zinc sulfide fine particle layered substance, which is the photocatalyst of the present invention in the process of production, under the same conditions as in FIG. is there. FIG. 3B is a structural schematic diagram in the cross-sectional direction.
The black portion 4 seen in the center of FIG. 3 (A) is confirmed to be zinc oxide as a result of measurement by the minute region EDX, and corresponds to the zinc oxide particles 4 of FIG. 3 (B). The gray strip portion 2 outside the black portion 4 seen in the center of FIG. 3A corresponds to the cavity 2 of FIG. The black portion 1 outside the strip-like gray portion 2 in FIG. 3 (A) is confirmed to be a zinc sulfide fine particle layer as measured by the microscopic region EDX, and corresponds to the outer shell 1 in FIG. 3 (B). . The microscopic region EDX analyzer indicates that the cloud-like substance 5 distributed on the outside of the black portion 1 in FIG. 3A, on the cavity 2 and on the zinc oxide particles 4 is an aggregate of zinc sulfide. It is confirmed by the measurement by
[0037]
As seen in FIG. 3A, the presence of the cavity 2 between the zinc oxide particle 4 and the outer shell 1 made of the zinc sulfide fine particle layer is generated in the formation process described below. It is shown that.
That is, sodium sulfide (Na2S) In the aqueous solution, zinc oxide (ZnO) is transferred from the surface of the zinc oxide particles 4 to zincate ions (ZnO).2-Elution). This zincate ion is sodium sulfide (Na2S) Sulfur ions in aqueous solution (S2-To zinc sulfide (ZnS). This zinc sulfide is deposited 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 which is a raw material, and reacts with the zinc oxide 4 to generate zincate ions. The zincate ions diffuse in the zinc sulfide fine particle layer, and 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 become zinc sulfide, which is deposited on the zinc sulfide fine particle layer, and the zinc sulfide fine particle layer grows.
[0038]
Since it is such a generation process, a part of the zinc oxide particles 4 is eluted as a zincate ion and a volume defect is generated, so that a cavity 2 as shown in FIG. 3A is generated.
[0039]
As described above, when one component of a chemical reaction is supplied by diffusion and the reaction product forms this diffusion layer, the supply amount of one component gradually decreases as the diffusion layer grows. A layer with a changed chemical component ratio is formed. That is, the zinc sulfide fine particle layer that is a photocatalyst according to the present invention has a structure in which the component ratio of zinc (Zn) and sulfur (S) is changed in the layer thickness direction.
[0040]
In addition, the cloud-like substance 5 seen in FIG. 3A, that is, an aggregate of zinc sulfide is generated as follows.
At the stage where the zinc sulfide fine particle layer has grown considerably, it becomes difficult for zincate ions to diffuse through the zinc sulfide fine particle layer, so that the pressure of the eluted zincate ion increases inside the zinc sulfide fine particle layer, breaking the zinc sulfide fine particle layer. Erupt. The jetted zincate ions react with surrounding sulfur ions to become cloud-like substances 5 that are aggregates of zinc sulfide. The hole 3 shown in FIG. 1B is made in this way.
[0041]
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 by being produced from zinc oxide particles. That is, when producing ZnS, a chemical reaction process of a zinc ion solution and hydrogen sulfide is generally used. In contrast, in the present invention, zinc sulfide is generated from zinc oxide particles. A specific manufacturing method will be described below.
[0042]
First embodiment of photocatalyst production method:
Zinc oxide (ZnO) and sodium sulfide (Na2S) Mix aqueous solution and stir at room temperature. After the above treatment, the membrane is filtered with suction through a nitrocellulose membrane filter (pore size: 0.1 μm) and washed with distilled water, and then dried in a constant temperature bath 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 (Na2S • 9H2O, purity 98%) It is optimal to mix 100 ml of aqueous solution and stir for 15 hours or more.
[0043]
Next, the process in which the zinc sulfide fine particle layer that is the photocatalyst of the present invention is formed by this method will be described.
Zinc oxide particles (ZnO) and sodium sulfide (Na2S) When an aqueous solution is mixed and this mixed solution is stirred, zinc oxide reacts with water, and zincate ions (ZnO2 2-) In the form of sulfur ions (S2-) To form zinc sulfide (ZnS), which 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 that has permeated the zinc sulfide fine particle layer diffuse into the zinc sulfide fine particle layer that has already been generated, reach the surface of the zinc sulfide fine particle layer, and react with sulfur ions. Thus, zinc sulfide is formed and deposited 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 the zinc sulfide fine particles having a composition with a shifted component ratio of zinc sulfide are deposited. A layered material is formed.
[0044]
Second embodiment of photocatalyst production method:
Put zinc oxide and aqueous sodium sulfide solution in a fused quartz container and irradiate with ultraviolet rays. For example, in the case of 50 mg of zinc oxide (purity 99.999%, particle size of about 1 μm), 5 ml of a 0.1 molar sodium sulfide aqueous solution is mixed, and irradiation with a 500 W ultrahigh pressure mercury lamp for 1 hour or more is optimal.
After the above treatment, the membrane filter is subjected to suction filtration / distilled water washing and dried in a thermostatic bath at 60 ° C.
[0045]
Next, the process in which the zinc sulfide fine particle layer that is the photocatalyst of the present invention is formed by this method will be described. The process of forming the zinc sulfide fine particle layer is the same as that in the first embodiment of the photocatalyst production method. However, when irradiated with ultraviolet rays, zinc oxide is photodissolved and zincate ions are likely to be eluted. The zinc sulfide fine particle layer grows faster.
[0046]
Third embodiment of photocatalyst production method:
Mix zinc oxide particles and distilled water to form hydrogen sulfide (H2S) Stirring while bubbling with gas, stop hydrogen sulfide gas after a certain time, and further stir for a certain time.
For example, in the case of 2 g of zinc oxide (purity 99.999%, particle size of about 1 μm), 50 ml of distilled water is mixed, bubbled at a hydrogen sulfide gas flow rate of 50 ml / min for about 1 hour, and after stopping the gas, about 12 Stirring over time is optimal.
After the above treatment, the membrane filter is subjected to suction filtration / distilled water washing and dried in a thermostatic bath at 60 ° C.
[0047]
Next, the process in which the zinc sulfide fine particle layered material which is the photocatalyst of the present invention is generated by this method will be described. The process of forming the zinc sulfide fine particle layer is the same as that in the first embodiment of the photocatalyst production 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. Since zinc oxide dissolves well in weakly acidic solutions, the growth of the zinc sulfide fine particle layer is accelerated.
[0048]
Fourth embodiment of photocatalyst production method:
Zinc oxide and sodium sulfide aqueous solution are put into a fused quartz container, bubbled with hydrogen sulfide gas, and simultaneously irradiated with ultraviolet rays. For example, in the case of 2 g of zinc oxide, 50 ml of a 0.1 molar sodium sulfide aqueous solution is mixed and bubbled at a hydrogen sulfide gas flow rate of 50 ml / min. After the above treatment, the membrane filter is subjected to suction filtration / distilled water washing and dried in a thermostatic bath at 60 ° C.
[0049]
In this method, the process of generating the zinc sulfide fine particle layered material which is the photocatalyst of the present invention is the same as that of the first embodiment of the photocatalyst production method. However, the second and third photocatalyst production methods are the same. As described in the embodiment, since zinc oxide is further dissolved and the supply of sulfur ions is increased, the growth of the zinc sulfide fine particle layer is further accelerated.
[0050]
Next, the photocatalytic performance of the photocatalyst of the present invention, that is, the zinc sulfide fine particle layered material photocatalyst (named as a stratified ZnS nanoparticle photocatalyst) will be described. FIG. 4 is a performance comparison result of comparing the amount of hydrogen gas generated by photodecomposing a sodium sulfide aqueous solution under the same apparatus and under the same conditions as a conventional photocatalyst in order to show the performance of the photocatalyst of the present invention.
[0051]
The apparatus used for the performance comparison is shown in FIG. As shown in FIG. 5, this apparatus stores a photoreaction portion 6 made of quartz glass, a hydrogen determination portion 7 for quantifying generated hydrogen, and a sodium sulfide aqueous solution 8 corresponding to the volume of generated hydrogen gas. Thus, a solution reservoir 9 that prevents an increase in hydrogen pressure, a 500 W mercury lamp 10 for irradiating ultraviolet rays, a lens L for condensing the ultraviolet rays 11, and a reflecting mirror 13 for reflecting the ultraviolet rays 11 and irradiating the photocatalyst 12 thereon. It consists of and. At the start of the photolysis reaction, the entire system is filled with the sodium sulfide aqueous solution 8, a certain amount of photocatalyst 12 is precipitated at the bottom of the photoreaction portion 6, the generated gas recovery port 14 is closed, and the 500 W mercury lamp 10 is turned on. The amount of hydrogen generation is measured at a fixed amount of time in the hydrogen determination portion 7.
[0052]
Conventional photocatalysts used for comparison were ZnS (purity 99.999%), CdS (purity 90%), CdSe (purity 99.99%) and TiO.2(Purity 95%). The photocatalyst of the present invention was produced by the method described in the third embodiment of the photocatalyst production 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]
This reaction is represented by the following formula.
Na2S + H2O → ← 2Na++ HS-+ OH-
HS-+ 2h+  → S + H+
2H+  + 2e-  → H2
Where e-, H+Represents free electrons and free holes generated by photocatalysis by light irradiation. “→ ←” represents a chemical equilibrium reaction.
[0054]
As is clear from the graph showing the performance comparison in FIG. 4, the zinc sulfide fine particle layered material (stratified ZnS nanoparticle photocatalyst) which is the photocatalyst of the present invention has much higher catalytic activity than the conventional photocatalyst.
[0055]
As described above, the reason why the catalytic activity is high is that, as described above, since the component ratio of zinc sulfide in the zinc sulfide fine particle layer changes in the layer thickness direction, space charges are generated, and an electric field is generated in the layer thickness direction. This is because. This electric field causes the 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 site for the oxidation reaction and the reaction site for the reduction reaction. Since the recombination between the product and the reduction reaction product is also reduced, the catalytic activity is increased.
[0056]
Next, the method for using the photocatalyst of the present invention, in which an aqueous sodium sulfide solution is used as a sacrificial reducing agent for the zinc sulfide fine particle layered material (stratified ZnS nanoparticle photocatalyst) that is the photocatalyst of the present invention, will be described.
[0057]
FIG. 6 is a characteristic diagram showing the lifetime of the zinc sulfide fine particle layered material which is the photocatalyst of the present invention. When the apparatus shown in FIG. 5 is used, the photocatalyst of the present invention is added to a 0.1 molar sodium sulfide aqueous solution and irradiated with ultraviolet rays, and the generation of hydrogen gas is completed, that is, all the sulfur ions in the aqueous solution are reduced. When (S) is reached, after measuring the amount of hydrogen gas, the hydrogen gas is discharged, a sodium sulfide aqueous solution is newly added, and photolysis is continued. In FIG. 6, black circles indicate the time when 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]
As is apparent from FIG. 6, the catalytic activity of the zinc sulfide fine particle layered material, which is the photocatalyst of the present invention, does not change even when used for 40 hours. Although not shown in FIG. 6, no change in the photocatalytic activity was observed even after 50 hours of use.
[0059]
The reason for such a long life is that, rather than the dissolution reaction in which zinc sulfide shown in the following formula is oxidized by free holes,
ZnS + 2h+→ Zn2++ S
Since the oxidation reaction in which sodium sulfide is oxidized by free holes is more likely to occur,
Na2S + 2h+→ 2Na++ S
This is because sodium sulfide is oxidized in place of zinc sulfide to prevent the zinc sulfide fine particle layered material from eluting.
[0060]
That is, sodium sulfide (Na2If the S) aqueous solution is used as a sacrificial reducing agent for a photocatalyst composed of a zinc sulfide fine particle layered material, the life of the photocatalyst is extended.
[0061]
Zinc sulfide (ZnS) is not toxic as is well known. Therefore, the zinc sulfide fine particle layered material (stratified ZnS nanoparticle photocatalyst) which is the photocatalyst of the present invention is not toxic.
[0062]
In addition, the zinc sulfide fine particle layered material which is the photocatalyst of the present invention is inexpensive because no precious metal is used as described above.
[0063]
Next, a method for producing hydrogen and sulfur by decomposing hydrogen sulfide using the zinc sulfide fine particle layered material, which is the photocatalyst of the present invention, according to an embodiment of the photocatalyst using method of the present invention will be described.
[0064]
This method comprises the following steps.
(A) A step of dissolving hydrogen sulfide in an aqueous caustic soda solution.
(B) A step of adding a photocatalyst to the solution after the step (a), irradiating with ultraviolet rays, and recovering hydrogen gas.
(C) A step of recovering sulfur from the solution after the step (B).
(D) A step of reusing the solution after step (c) as the aqueous caustic soda solution of step (a).
[0065]
This method will be described with reference to FIG. 7 schematically showing the configuration of the above steps.
In FIG. 7, 15 is an alkali dissolution tank for holding the caustic soda aqueous solution 16 and dissolving hydrogen sulfide gas by bubbling or the like, and is a part for performing the step (a). 17 holds a caustic soda aqueous solution 16 in which hydrogen sulfide is dissolved by the step (a), holds a photocatalyst 12, and has a transparent bottom so that the photocatalyst 12 can be irradiated with ultraviolet rays 11 from the outside, and is generated. This is a photocatalytic reaction tank in which the hydrogen gas to be collected is recovered, and is a part for performing the step (b). Reference numeral 18 denotes a sulfur recovery tank that recovers sulfur (S) from the solution 16 that has undergone the photodecomposition reaction in the photocatalytic reaction tank 17 by the process (b), and is a part that performs the process (c). Reference numeral 10 denotes a light source in which the photocatalyst 12 is disposed so as to be irradiated with ultraviolet rays from outside the photocatalytic reaction tank 17, and 11 is ultraviolet rays.
[0066]
Next, the operation in the configuration of FIG. 7 will be described.
Step (a). When hydrogen sulfide is dissolved in the alkali dissolution tank 15, the sodium hydroxide aqueous solution 16 becomes the sodium sulfide aqueous solution 16 by the reaction shown in the following formula.
2NaOH + H2S → ← 2Na++ HS-+ H2O + OH-
2Na++ HS-+ OH-  → ← Na2S + H2O
[0067]
Step (b). When this sodium sulfide aqueous solution 16 is transferred to the photocatalytic reaction tank 17 and irradiated with the photocatalyst 12 by the ultraviolet rays 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 the reaction shown in the following formula. , Produces hydrogen gas and sulfur. Hydrogen gas is recovered as soon as it is generated.
Na2S + H2O → ← 2Na++ HS-+ OH-
HS-+ 2h+  → S + H+
2H+  + 2e-  → H2
[0068]
Steps (c) and (d). When the redox reaction is completed, that is, when all the sulfur ions are reduced to sulfur, the sodium sulfide aqueous solution 16 becomes a caustic soda aqueous solution 16 containing sulfur as is apparent from the above formula. This caustic soda aqueous solution 16 is transferred to the sulfur recovery tank 18, and sulfur is recovered. This caustic soda aqueous solution 16, which is free of sulfur, is returned to the alkali dissolution tank 15 and used again as the caustic soda aqueous solution 16 in the step (a).
[0069]
Therefore, according to the embodiment of the method of using the photocatalyst of the present invention, the method of decomposing hydrogen sulfide and producing hydrogen and sulfur using the zinc sulfide fine particle layered substance which is the photocatalyst of the present invention is described above. As described above, hydrogen sulfide, which is an environmentally hazardous substance, is decomposed without requiring any energy other than that required for ultraviolet light sources, and without generating any harmful substances, producing hydrogen and sulfur, which are useful substances. can do.
[0070]
【The invention's effect】
As understood from the above description, the photocatalyst of the present invention has high catalytic activity as a photocatalyst, is not toxic, is inexpensive and has a long life. If the method for decomposing hydrogen sulfide and producing hydrogen and sulfur according to the present invention is used, it can contribute to the solution of environmental problems and can produce useful effects such as being able to produce useful substances at a low cost.
[Brief description of the drawings]
FIG. 1 is a structural schematic diagram showing the structure of a photocatalyst of the present invention.
2A is a copy of an electron micrograph of a photocatalytic structure of the present invention, and FIG. 2B is a copy of an electron micrograph of zinc oxide particles as a raw material.
FIG. 3A is a copy of an electron micrograph showing the process of producing a photocatalyst according to the present invention, and FIG. 3B is a structural schematic diagram thereof.
FIG. 4 is a performance comparison diagram of the photocatalyst of the present invention and a conventional photocatalyst.
5 is a configuration diagram of an apparatus used for performance comparison in FIG. 4;
FIG. 6 is a characteristic diagram showing the lifetime of the photocatalyst of the present invention.
FIG. 7 is a process diagram of a method for producing hydrogen and sulfur by decomposing hydrogen sulfide according to an embodiment of the present invention.
FIG. 8 is an electron micrograph of the photocatalyst of the present invention corresponding to the copy shown in FIG.
FIG. 9 is an electron micrograph of zinc oxide particles that are the raw material of the photocatalyst of the present invention corresponding to the copy shown in FIG. 2 (B).
FIG. 10 is an electron micrograph showing a photocatalyst being generated corresponding to the copy shown in FIG.
FIG. 11 is a process diagram of desulfurization of crude oil according to the prior art.
[Explanation of symbols]
1 Outer shell made of zinc sulfide fine particle layer
2 cavity
3 holes
4 Zinc oxide particles
5 Cloudy material
6 Photoreactive part
7 Hydrogen determination part
8 Sodium sulfide aqueous solution
9 Solution reservoir
10 500W mercury lamp
11 UV
12 Photocatalyst
13 Reflector
14 Generated gas recovery port
15 Alkali dissolution tank
16 Caustic soda aqueous solution, sodium sulfide aqueous solution, or caustic soda aqueous solution containing sulfur
17 Photocatalytic reactor
18 Sulfur recovery tank

Claims (9)

硫化亜鉛からなる5から10nmの粒径を有する化合物半導体微粒子が層状に集合し、該層状の集合体から成る外殻と空洞とを有し、かつ、該外殻は穴を有しており、上記層の厚み方向に、上記硫化亜鉛の成分である亜鉛(Zn)と硫黄(S)の成分比が変化していることを特徴とする光触媒。Compound semiconductor fine particles made of zinc sulfide having a particle diameter of 5 to 10 nm are gathered in layers , and have an outer shell and a cavity made of the layered aggregate , and the outer shell has holes. A photocatalyst characterized in that the component ratio of zinc (Zn) and sulfur (S) , which are components of the zinc sulfide , changes in the thickness direction of the layer. 前記外殻を有する光触媒の外形が、カプセル形状又は球形状であることを特徴とする、請求項記載の光触媒。The outer shape of the photocatalyst with the outer shell, characterized in that it is a capsule-shaped or spherical shape, according to claim 1 of the photocatalyst. 酸化亜鉛からなる酸化物粒子を、イオウイオンを含む水溶液中で溶解し、生成する亜鉛の硫化物をこの酸化亜鉛からなる酸化物粒子上に析出して生成する、光触媒の製造方法。 A method for producing a photocatalyst, wherein oxide particles made of zinc oxide are dissolved in an aqueous solution containing sulfur ions, and the generated zinc sulfide is deposited on the oxide particles made of zinc oxide. 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、請求項3記載の光触媒の製造方法。The method for producing a photocatalyst according to claim 3 , comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution and a step of stirring the mixed solution. 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、請求項3記載の光触媒の製造方法。The method for producing a photocatalyst according to claim 3 , comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, and a step of stirring the mixture while irradiating with ultraviolet rays. 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、請求項3記載の光触媒の製造方法。4. The method according to claim 3 , comprising: a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution; a step of stirring hydrogen sulfide in the mixed solution; and a step of stopping hydrogen sulfide gas and further stirring for a predetermined time. A method for producing a photocatalyst. 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、かつ、硫化水素をバブリングする工程とからなる、請求項3記載の光触媒の製造方法。The method for producing a photocatalyst according to claim 3 , comprising a step of mixing zinc oxide fine particles and an aqueous sodium sulfide solution, and a step of irradiating the mixture with ultraviolet light and bubbling hydrogen sulfide. 次の各工程よりなる、請求項1記載の硫化亜鉛からなる光触媒用いた硫化水素の分解方法。
(イ)苛性ソーダ水溶液に硫化水素を溶解する工程、
(ロ)該溶液に上記硫化亜鉛からなる光触媒を加え、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。
Consisting subsequent steps, the method for decomposing hydrogen sulfide with a photocatalyst consisting of zinc sulfide of claim 1, wherein.
(A) a process of dissolving hydrogen sulfide in an aqueous caustic soda solution,
(B) adding a photocatalyst made of zinc sulfide to the solution, irradiating with ultraviolet rays, and recovering hydrogen gas;
(C) recovering sulfur from the solution after step (b);
(D) A step of reusing the solution after step (c) as the aqueous caustic soda solution of step (a).
前記光触媒の外形が、カプセル形状又は球形状であることを特徴とする、請求項8記載の光触媒を用いた硫化水素の分解方法。9. The method for decomposing hydrogen sulfide using a photocatalyst according to claim 8, wherein the outer shape of the photocatalyst is a capsule shape or a spherical shape.
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