JPH0663178A - Method of decomposing organic compound - Google Patents
Method of decomposing organic compoundInfo
- Publication number
- JPH0663178A JPH0663178A JP4222455A JP22245592A JPH0663178A JP H0663178 A JPH0663178 A JP H0663178A JP 4222455 A JP4222455 A JP 4222455A JP 22245592 A JP22245592 A JP 22245592A JP H0663178 A JPH0663178 A JP H0663178A
- Authority
- JP
- Japan
- Prior art keywords
- organic compound
- titanium oxide
- liquid
- oxidative decomposition
- perfluorinated
- 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
- 150000002894 organic compounds Chemical class 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 26
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 19
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims abstract description 17
- 230000001678 irradiating effect Effects 0.000 claims abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 12
- 239000001301 oxygen Substances 0.000 claims description 12
- 229910052760 oxygen Inorganic materials 0.000 claims description 12
- IYVLHQRADFNKAU-UHFFFAOYSA-N oxygen(2-);titanium(4+);hydrate Chemical compound O.[O-2].[O-2].[Ti+4] IYVLHQRADFNKAU-UHFFFAOYSA-N 0.000 claims 1
- 238000006864 oxidative decomposition reaction Methods 0.000 abstract description 22
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 14
- 239000013067 intermediate product Substances 0.000 abstract description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 7
- 239000001569 carbon dioxide Substances 0.000 abstract description 7
- 239000007791 liquid phase Substances 0.000 abstract description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 6
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 6
- 239000012071 phase Substances 0.000 abstract description 5
- 238000007254 oxidation reaction Methods 0.000 abstract description 3
- 150000003071 polychlorinated biphenyls Chemical group 0.000 abstract description 3
- 125000004432 carbon atom Chemical group C* 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 230000003647 oxidation Effects 0.000 abstract description 2
- 239000012429 reaction media Substances 0.000 abstract description 2
- 238000011109 contamination Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 10
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 8
- 150000001875 compounds Chemical class 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 7
- -1 titanium alkoxide Chemical class 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229910001882 dioxygen Inorganic materials 0.000 description 3
- 229910052731 fluorine Inorganic materials 0.000 description 3
- 125000001153 fluoro group Chemical group F* 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- RVZRBWKZFJCCIB-UHFFFAOYSA-N perfluorotributylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F RVZRBWKZFJCCIB-UHFFFAOYSA-N 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- 229920001774 Perfluoroether Polymers 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- QARVLSVVCXYDNA-UHFFFAOYSA-N bromobenzene Chemical compound BrC1=CC=CC=C1 QARVLSVVCXYDNA-UHFFFAOYSA-N 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 150000008282 halocarbons Chemical class 0.000 description 2
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- UJMWVICAENGCRF-UHFFFAOYSA-N oxygen difluoride Chemical compound FOF UJMWVICAENGCRF-UHFFFAOYSA-N 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- 150000003609 titanium compounds Chemical class 0.000 description 2
- 229910000349 titanium oxysulfate Inorganic materials 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- UVWPNDVAQBNQBG-UHFFFAOYSA-N 1,1,1,2,2,3,3,4,4,5,5,6,6,7,7,8,8,9,9,9-icosafluorononane Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F UVWPNDVAQBNQBG-UHFFFAOYSA-N 0.000 description 1
- SLGOCMATMKJJCE-UHFFFAOYSA-N 1,1,1,2-tetrachloro-2,2-difluoroethane Chemical compound FC(F)(Cl)C(Cl)(Cl)Cl SLGOCMATMKJJCE-UHFFFAOYSA-N 0.000 description 1
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- RKIMETXDACNTIE-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,5,5,6,6-dodecafluorocyclohexane Chemical compound FC1(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F RKIMETXDACNTIE-UHFFFAOYSA-N 0.000 description 1
- QIROQPWSJUXOJC-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,5,5,6-undecafluoro-6-(trifluoromethyl)cyclohexane Chemical compound FC(F)(F)C1(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F QIROQPWSJUXOJC-UHFFFAOYSA-N 0.000 description 1
- LIXDPHHZLNLBGW-UHFFFAOYSA-N 1,2,2,3,3,4,4,5,5,6,6-undecafluoro-N,N-bis(trifluoromethyl)cyclohexan-1-amine Chemical compound FC(F)(F)N(C(F)(F)F)C1(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F LIXDPHHZLNLBGW-UHFFFAOYSA-N 0.000 description 1
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- CXBDYQVECUFKRK-UHFFFAOYSA-N 1-methoxybutane Chemical compound CCCCOC CXBDYQVECUFKRK-UHFFFAOYSA-N 0.000 description 1
- PQMAKJUXOOVROI-UHFFFAOYSA-N 2,2,3,3,5,5,6,6-octafluoro-4-(trifluoromethyl)morpholine Chemical compound FC(F)(F)N1C(F)(F)C(F)(F)OC(F)(F)C1(F)F PQMAKJUXOOVROI-UHFFFAOYSA-N 0.000 description 1
- YHQBBDKFBJYMPJ-UHFFFAOYSA-N 2-propyloxane Chemical compound CCCC1CCCCO1 YHQBBDKFBJYMPJ-UHFFFAOYSA-N 0.000 description 1
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- CCPHAMSKHBDMDS-UHFFFAOYSA-N Chetoseminudin B Natural products C=1NC2=CC=CC=C2C=1CC1(SC)NC(=O)C(CO)(SC)N(C)C1=O CCPHAMSKHBDMDS-UHFFFAOYSA-N 0.000 description 1
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- XOBKSJJDNFUZPF-UHFFFAOYSA-N Methoxyethane Chemical compound CCOC XOBKSJJDNFUZPF-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- INNSZZHSFSFSGS-UHFFFAOYSA-N acetic acid;titanium Chemical compound [Ti].CC(O)=O.CC(O)=O.CC(O)=O.CC(O)=O INNSZZHSFSFSGS-UHFFFAOYSA-N 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229960004624 perflexane Drugs 0.000 description 1
- 229950008618 perfluamine Drugs 0.000 description 1
- 229950011087 perflunafene Drugs 0.000 description 1
- FYJQJMIEZVMYSD-UHFFFAOYSA-N perfluoro-2-butyltetrahydrofuran Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)OC(F)(F)C(F)(F)C1(F)F FYJQJMIEZVMYSD-UHFFFAOYSA-N 0.000 description 1
- UWEYRJFJVCLAGH-IJWZVTFUSA-N perfluorodecalin Chemical compound FC1(F)C(F)(F)C(F)(F)C(F)(F)[C@@]2(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)[C@@]21F UWEYRJFJVCLAGH-IJWZVTFUSA-N 0.000 description 1
- LGUZHRODIJCVOC-UHFFFAOYSA-N perfluoroheptane Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F LGUZHRODIJCVOC-UHFFFAOYSA-N 0.000 description 1
- ZJIJAJXFLBMLCK-UHFFFAOYSA-N perfluorohexane Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F ZJIJAJXFLBMLCK-UHFFFAOYSA-N 0.000 description 1
- QKENRHXGDUPTEM-UHFFFAOYSA-N perfluorophenanthrene Chemical compound FC1(F)C(F)(F)C(F)(F)C(F)(F)C2(F)C3(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C3(F)C(F)(F)C(F)(F)C21F QKENRHXGDUPTEM-UHFFFAOYSA-N 0.000 description 1
- AQZYBQIAUSKCCS-UHFFFAOYSA-N perfluorotripentylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F AQZYBQIAUSKCCS-UHFFFAOYSA-N 0.000 description 1
- JAJLKEVKNDUJBG-UHFFFAOYSA-N perfluorotripropylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)F JAJLKEVKNDUJBG-UHFFFAOYSA-N 0.000 description 1
- 238000007539 photo-oxidation reaction Methods 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- IJNJLGFTSIAHEA-UHFFFAOYSA-N prop-2-ynal Chemical compound O=CC#C IJNJLGFTSIAHEA-UHFFFAOYSA-N 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fire-Extinguishing Compositions (AREA)
- Treating Waste Gases (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Catalysts (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、有機化合物を分解する
方法に関するものであって、より詳しくは、液相状態
で、有毒物質を生成することなく有機化合物を酸化分解
する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing an organic compound, and more particularly to a method for oxidatively decomposing an organic compound in a liquid phase without producing toxic substances.
【０００２】[0002]
【従来の技術およびその問題点】従来より有機化合物の
分解方法としては、例えば、ジャーナル・オブ・フィジ
カル・ケミストリー（Ｊ．Ｐｈｙｓ．Ｃｈｅｍ．）９３
巻４１２８ページ（１９８９年）に開示されているよう
に、気相中において、酸化チタンを触媒として酸素の存
在下に光を照射して、メタンやエタン等の炭化水素を酸
化分解する方法が知られている。上記の方法は気相法で
あるために、分解反応温度で気体である化合物の酸化分
解には適用が容易であるが、液体である化合物の場合
は、該化合物の沸点以上の温度に加熱して気化させなけ
ればならず、また、該化合物が気体を保つ温度で酸化分
解を行わなければならないという問題があった。2. Description of the Related Art Conventional methods for decomposing organic compounds include, for example, Journal of Physical Chemistry (J. Phys. Chem.) 93.
As disclosed in Volume 4128 (1989), there is known a method of oxidatively decomposing hydrocarbons such as methane and ethane by irradiating light in the presence of oxygen using titanium oxide as a catalyst in a gas phase. Has been. Since the above method is a gas phase method, it is easy to apply to the oxidative decomposition of a compound that is a gas at the decomposition reaction temperature, but in the case of a liquid compound, heating it to a temperature above the boiling point of the compound There is a problem in that the compound must be vaporized and the oxidative decomposition must be carried out at a temperature at which the compound maintains a gas.
【０００３】そこで、本発明者らは、分解反応温度で気
体または液体のいずれであっても容易に分解が可能なよ
うに液相中で酸化分解反応を行うことを試みた。そし
て、酸化分解の対象となる有機化合物として、分解反応
温度で液体である有機化合物を用い、該有機化合物自体
を媒体とする液相中で酸化分解を行った結果、今度は、
有機化合物の酸化分解による中間生成物が生成するとい
う新たな問題が発生した。Therefore, the present inventors have tried to carry out the oxidative decomposition reaction in the liquid phase so that the decomposition can be easily carried out in either gas or liquid at the decomposition reaction temperature. Then, as an organic compound to be subjected to oxidative decomposition, an organic compound that is liquid at the decomposition reaction temperature is used, and as a result of oxidative decomposition in a liquid phase using the organic compound itself as a medium, this time,
A new problem has arisen that an intermediate product is produced by the oxidative decomposition of the organic compound.
【０００４】[0004]
【問題点を解決するための手段】本発明者らは、中間生
成物を生成することなく、各種の有機化合物を液相中で
酸化分解する方法について検討した結果、反応媒体とし
てペルフルオロ不活性液体を使用することにより、それ
が可能になるという知見を得、本発明を提案するに至っ
た。すなわち、本発明によれば、ペルフルオロ不活性液
体中において、酸化チタンおよび／または含水酸化チタ
ンと酸素の存在下に有機化合物に光を照射することを特
徴とする有機化合物の分解方法が提供される。[Means for Solving the Problems] The present inventors have studied a method of oxidatively decomposing various organic compounds in a liquid phase without producing an intermediate product. It was found that this can be achieved by using, and the present invention was proposed. That is, the present invention provides a method for decomposing an organic compound, which comprises irradiating the organic compound with light in the presence of titanium oxide and / or hydrous titanium oxide and oxygen in a perfluoroinert liquid. .
【０００５】[0005]
【発明の具体的説明】本発明において使用されるペルフ
ルオロ不活性液体とは、炭素−水素結合を有する有機化
合物の水素原子の全部がフッ素原子によって置換された
化合物、あるいは、炭素−水素結合を有する有機化合物
に不飽和結合がある場合には、フッ素原子の置換と不飽
和結合へのフッ素原子の付加とによって得られた化合物
であって、分解反応条件において液体である化合物を何
等制限なく採用することができる。とくに本発明におい
ては、酸素をよく溶解し、さらに、紫外線によって分解
し難いペルフルオロ不活性液体が好適に使用される。こ
のようなペルフルオロ不活性液体としては、例えば、ペ
ルフルオロ不活性液体１００ｍｌに、２５℃、１気圧に
おいて、酸素を１５ｍｌ以上、好ましくは２５ｍｌ以上
溶解するようなペルフルオロ不活性液体が、酸化分解反
応の速度が早いために好適に使用できる。DETAILED DESCRIPTION OF THE INVENTION The perfluoroinert liquid used in the present invention is a compound in which all the hydrogen atoms of an organic compound having a carbon-hydrogen bond are replaced by fluorine atoms, or a carbon-hydrogen bond. When the organic compound has an unsaturated bond, a compound obtained by substitution of a fluorine atom and addition of a fluorine atom to the unsaturated bond, which is a liquid under the decomposition reaction condition, is adopted without any limitation. be able to. Particularly, in the present invention, a perfluoroinert liquid that dissolves oxygen well and is hardly decomposed by ultraviolet rays is preferably used. As such a perfluoro-inert liquid, for example, a perfluoro-inert liquid in which 100 ml of the perfluoro-inert liquid dissolves 15 ml or more, preferably 25 ml or more of oxygen at 25 ° C. and 1 atm, is used. Since it is fast, it can be preferably used.
【０００６】本発明において好適に使用されるペルフル
オロ不活性液体を具体的に示すと、例えば、ペルフルオ
ロヘキサン、ペルフルオロヘプタン、ペルフルオロノナ
ン等のペルフルオロアルカン類；ペルフルオロシクロヘ
キサン、ペルフルオロメチルシクロヘキサン等のペルフ
ルオロシクロアルカン類；ペルフルオロペルヒドロフェ
ナントレン、ペルフルオロデカリン等のペルフルオロ多
環式化合物；ペルフルオロトリプロピルアミン、ペルフ
ルオロトリブチルアミン、ペルフルオロトリペンチルア
ミン、ペルフルオロ−Ｎ，Ｎ−ジメチルシクロヘキシル
アミン等のペルフルオロトリアルキルアミン類；ペルフ
ルオロ−２ｎ−プロピルテトラヒドロピラン、ペルフル
オロ−２ｎ−ブチルテトラヒドロフラン等のペルフルオ
ロシクロエーテル類；ヘキサフルオロプロピレンオリゴ
マー、ヘキサフルオロプロピレンを光酸化と同時に重合
させて得られたオリゴマーにフッ素ガスを反応させて得
られるペルフルオロエーテル等のペルフルオロエーテル
類；ペルフルオロ−Ｎ−メチルモルホリン等を挙げるこ
とができる。Specific examples of the perfluoroinert liquid preferably used in the present invention include perfluoroalkanes such as perfluorohexane, perfluoroheptane and perfluorononane; perfluorocycloalkanes such as perfluorocyclohexane and perfluoromethylcyclohexane. Perfluoropolycyclic compounds such as perfluoroperhydrophenanthrene, perfluorodecalin; perfluorotrialkylamines such as perfluorotripropylamine, perfluorotributylamine, perfluorotripentylamine, perfluoro-N, N-dimethylcyclohexylamine; perfluoro-2n -Perfluorocycloethers such as propyltetrahydropyran and perfluoro-2n-butyltetrahydrofuran A hexafluoropropylene oligomer, a perfluoroether such as a perfluoroether obtained by reacting a fluorine gas with an oligomer obtained by polymerizing hexafluoropropylene at the same time as photooxidation; perfluoro-N-methylmorpholine and the like. .
【０００７】本発明において使用される酸化チタンおよ
び／または含水酸化チタンは、ルチル型、アナターゼ
型、およびそれらの混合物を問わず公知のものを何等制
限なく使用することができる。例えば、硫酸チタニル、
塩化チタン、チタンアルコキシドなどのチタン化合物
を、必要に応じてシードの存在下で液相加水分解または
気相加水分解したり、硫酸チタニル、塩化チタン、酢酸
チタンなどのチタン化合物をアルカリで中和するなどし
て得ることができる。このようにして得られたものをそ
のまま使用してもよいし、焼成した後使用してもよい。
このような酸化チタンおよび／または含水酸化チタンの
平均粒径は５ないし２５０ｎｍ、特に１０ないし１００
ｎｍであることが好ましい。酸化チタンおよび／または
含水酸化チタンの使用量は特に制限されないが、酸化分
解の対象となる有機化合物１ｍｏｌに対して、通常、
０．１ないし２００ｇの範囲で、特に１ないし１００ｇ
の範囲で選ぶことが好ましい。As the titanium oxide and / or hydrous titanium oxide used in the present invention, known ones can be used without any limitation regardless of rutile type, anatase type, and a mixture thereof. For example, titanyl sulfate,
Liquid-phase or gas-phase hydrolysis of titanium compounds such as titanium chloride and titanium alkoxide in the presence of seeds as necessary, and neutralization of titanium compounds such as titanyl sulfate, titanium chloride and titanium acetate with alkali It can be obtained by doing. The product thus obtained may be used as it is, or may be used after firing.
The average particle size of such titanium oxide and / or hydrous titanium oxide is 5 to 250 nm, especially 10 to 100 nm.
It is preferably nm. The amount of titanium oxide and / or hydrous titanium oxide used is not particularly limited, but is usually about 1 mol of the organic compound to be subjected to oxidative decomposition.
In the range of 0.1 to 200 g, especially 1 to 100 g
It is preferable to select within the range.
【０００８】本発明において使用される酸素は、酸素ガ
ス単独であってもよく、また、他のガスとの混合ガスで
使用してもよい。混合ガスを使用するときは、酸素の含
有量が２０容量％以上であることが、充分な酸化反応を
行う上で好ましい。酸素は、通常、ペルフルオロ不活性
液体中に吹き込む方法で供給される。酸化分解反応の前
にペルフルオロ不活性液体に酸素を吹き込んで溶解さ
せ、その後の酸化分解反応中には酸素を供給しない方法
を採用してもよく、また、酸化分解反応中も引き続き酸
素の吹き込みを継続して行ってもよく、さらに、酸化分
解反応中のみ酸素の吹き込みを行う方法を採用してもよ
い。The oxygen used in the present invention may be oxygen gas alone or a mixed gas with other gas. When using a mixed gas, it is preferable that the oxygen content is 20% by volume or more in order to perform a sufficient oxidation reaction. Oxygen is usually supplied by bubbling into a perfluoroinert liquid. A method may be adopted in which oxygen is blown into the perfluoro-inert liquid to dissolve it before the oxidative decomposition reaction, and oxygen is not supplied during the subsequent oxidative decomposition reaction. It may be carried out continuously, or a method of blowing oxygen only during the oxidative decomposition reaction may be adopted.
【０００９】本発明において、酸化分解の対象となる有
機化合物は、前記したペルフルオロ不活性液体を除く公
知の有機化合物を何等制限なく用いることができる。例
えば、メタン、エタン、プロパン、エチレン、プロピレ
ン等の脂肪族炭化水素：ベンゼン、トルエン、キシレン
等の芳香族炭化水素：メタノール、エタノール、プロパ
ノール等のアルコール：ホルムアルデヒド、アセトアル
デヒド、プロピオアルデヒド等のアルデヒド：ジメチル
エーテル、メチルエチルエーテル、メチルブチルエーテ
ル等のエーテル：塩化メチル、塩化メチレン、クロロホ
ルム、四塩化炭素、トリクロロエチレン、トリクロルエ
タン、パークロルエチレン、クロルベンゼン、ブロモベ
ンゼン、トリクロロフルオロメタン、ジクロロジフルオ
ロメタン、トリクロロトリフルオロエタン、テトラクロ
ロジフルオロエタン、ポリ塩化ビフェニル等のハロゲン
化炭化水素：ジメチルアミン、トリメチルアミン、アニ
リン、ピリジン等のアミン等の有機化合物：さらにダイ
オキシン等の有機化合物を例示することができる。これ
らの有機化合物の中でも、ペルフルオロ不活性液体に易
溶の脂肪族炭化水素およびハロゲン化炭化水素が好適で
あり、特に脂肪族炭化水素は短時間での酸化分解が可能
であるために、本発明において酸化分解の対象として好
適である。上記の酸化分解の対象となる有機化合物のペ
ルフルオロ不活性液体中での存在量は特に制限されない
が、通常は、ペルフルオロ不活性液体への溶解量の範囲
内とすればよい。In the present invention, as the organic compound to be oxidatively decomposed, known organic compounds other than the above-mentioned perfluoro-inert liquid can be used without any limitation. For example, methane, ethane, propane, ethylene, propylene, etc., aliphatic hydrocarbons: benzene, toluene, xylene, etc., aromatic hydrocarbons: methanol, ethanol, propanol, etc., alcohol: formaldehyde, acetaldehyde, propioaldehyde, etc. aldehydes: Ethers such as dimethyl ether, methyl ethyl ether, methyl butyl ether: methyl chloride, methylene chloride, chloroform, carbon tetrachloride, trichloroethylene, trichloroethane, perchlorethylene, chlorobenzene, bromobenzene, trichlorofluoromethane, dichlorodifluoromethane, trichlorotrifluoro Halogenated hydrocarbons such as ethane, tetrachlorodifluoroethane, polychlorinated biphenyls: dimethylamine, trimethylamine, aniline, pyridine Such amine organic compound: may be further exemplified organic compounds such as dioxin. Among these organic compounds, aliphatic hydrocarbons and halogenated hydrocarbons which are easily soluble in a perfluoroinert liquid are preferable, and in particular, since aliphatic hydrocarbons can be oxidized and decomposed in a short time, the present invention It is suitable as a target of oxidative decomposition. The amount of the organic compound to be subjected to the above-mentioned oxidative decomposition in the perfluoro-inert liquid is not particularly limited, but is usually within the range of the amount dissolved in the perfluoro-inert liquid.
【００１０】本発明の方法における酸化分解反応は、光
を照射することによって進行する。光としては、通常、
波長２００ないし４２０ｎｍの紫外線を好適に使用する
ことができる。光の照度は、分解反応を充分に行うため
には、１００ないし１０００Ｗ／ｍ2 の範囲であること
が好ましい。分解反応の温度は、ペルフルオロ不活性液
体の沸点以下であれば特に制限されないが、一般には０
ないし１５０℃の範囲で、圧力は、減圧、常圧、加圧の
いずれでもよく、また、反応時間は分解の対象となる有
機化合物の種類にもよるが、通常、５ないし３０時間の
範囲であれば充分である。The oxidative decomposition reaction in the method of the present invention proceeds by irradiation with light. As light usually
Ultraviolet rays having a wavelength of 200 to 420 nm can be preferably used. The illuminance of light is preferably in the range of 100 to 1000 W / m 2 in order to sufficiently carry out the decomposition reaction. The temperature of the decomposition reaction is not particularly limited as long as it is not higher than the boiling point of the perfluoroinert liquid, but is generally 0.
To 150 ° C., the pressure may be any of reduced pressure, normal pressure and increased pressure, and the reaction time is usually in the range of 5 to 30 hours, though it depends on the kind of the organic compound to be decomposed. It is enough.
【００１１】[0011]
【発明の効果】本発明によれば、反応媒体としてペルフ
ルオロ不活性液体を使用した液相で酸化分解を行うため
に、酸化分解の対象となる有機化合物が酸化分解温度に
おいて気体または液体のいずれであっても容易に酸化分
解を行うことができる。しかも、酸化による中間生成物
や一酸化炭素の生成がほとんどなく、有機化合物に含ま
れる炭素原子を二酸化炭素に変換することができる。し
たがって、本発明は、環境汚染等の原因となる有害な有
機化合物の処理方法として好適に使用することができ
る。特に本発明の方法によってポリ塩化ビフェニルの分
解を行ったとき、ダイオキシン等の有害物質の生成が全
くなく、環境衛生上からも優れていることが理解される
であろう。According to the present invention, in order to carry out oxidative decomposition in a liquid phase using a perfluoroinert liquid as a reaction medium, the organic compound to be oxidatively decomposed is either gas or liquid at the oxidative decomposition temperature. Even if there is, oxidative decomposition can be easily performed. Moreover, there is almost no generation of intermediate products or carbon monoxide due to oxidation, and the carbon atoms contained in the organic compound can be converted into carbon dioxide. Therefore, the present invention can be suitably used as a method for treating harmful organic compounds that cause environmental pollution and the like. It will be understood that when polychlorinated biphenyls are decomposed by the method of the present invention, no harmful substances such as dioxins are generated at all, which is excellent in environmental hygiene.
【００１２】[0012]
【実施例】以下に、本発明を実施例によって説明する
が、本発明はこれら実施例に限定されるものではない。The present invention will be described below with reference to examples, but the present invention is not limited to these examples.
【００１３】＜実施例１＞ペルフルオロトリブチルアミ
ン１ｍＬに平均粒径２１ｎｍの酸化チタン（商品名Ｐ−
２５、日本エアロジル製）１０ｍｇを分散させ、その中
にエタンと酸素ガスを吹き込んで飽和させた。ペルフル
オロトリブチルアミン１ｍＬ中に溶解したエタンおよび
酸素の量は、２５℃、１気圧における容積でそれぞれ
１．５８ｍＬ、および０．３５ｍＬであった。その後、
２９０ｎｍの紫外線を５００Ｗ／ｍ2の照度で酸素ガス
を吹き込みながら２０時間照射し、エタンを酸化分解し
た。反応の進行に伴う二酸化炭素の生成量を表１に示し
た。なお、酸化分解による中間生成物は検出されず、ま
た、一酸化炭素も検出されなかった。Example 1 Titanium oxide having a mean particle size of 21 nm (trade name P-
25, manufactured by Nippon Aerosil Co., Ltd.) was dispersed, and ethane and oxygen gas were blown into the mixture to saturate it. The amounts of ethane and oxygen dissolved in 1 mL of perfluorotributylamine were 1.58 mL and 0.35 mL at 25 ° C. and 1 atmosphere volume, respectively. afterwards,
The ethane was oxidatively decomposed by irradiating it with ultraviolet rays of 290 nm at an illuminance of 500 W / m 2 for 20 hours while blowing oxygen gas. Table 1 shows the amount of carbon dioxide produced as the reaction proceeded. In addition, an intermediate product due to oxidative decomposition was not detected, and neither carbon monoxide was detected.
【００１４】 [0014]
【００１５】＜実施例２＞表２に示した有機化合物を使
用したこと以外は、実施例１と同様にして有機化合物の
酸化分解を行った。実施例１と同様に酸化分解による中
間生成物は検出されず、また、一酸化炭素も検出されな
かった。反応前にペルフルオロトリブチルアミン中に溶
解させた有機化合物の量、表２に示した反応時間後の二
酸化炭素の生成量を表２に示した。<Example 2> Oxidative decomposition of an organic compound was carried out in the same manner as in Example 1 except that the organic compounds shown in Table 2 were used. As in Example 1, no intermediate product due to oxidative decomposition was detected, nor was carbon monoxide detected. Table 2 shows the amount of the organic compound dissolved in perfluorotributylamine before the reaction and the amount of carbon dioxide produced after the reaction time shown in Table 2.
【００１６】 [0016]
【００１７】＜実施例３＞表３に示したペルフルオロ不
活性液体を使用したこと以外は、実施例１と同様にして
有機化合物の酸化分解を行った。実施例１と同様に酸化
分解による中間生成物は検出されず、また、一酸化炭素
も検出されなかった。反応前にペルフルオロ不活性液体
中に溶解させたエタンの量、表３に示した反応時間後の
二酸化炭素の生成量を表３に示した。Example 3 The organic compound was oxidatively decomposed in the same manner as in Example 1 except that the perfluoroinert liquid shown in Table 3 was used. As in Example 1, no intermediate product due to oxidative decomposition was detected, nor was carbon monoxide detected. Table 3 shows the amount of ethane dissolved in the perfluoroinert liquid before the reaction and the amount of carbon dioxide produced after the reaction time shown in Table 3.
【００１８】 [0018]
【００１９】＜実施例４＞酸化チタンに代えて平均粒径
４．５ｎｍの含水酸化チタン（商品名ＣＳ−Ｃ石原産業
社製）１０ｍｇを使用したこと以外は実施例１とまった
く同様にしてエタンの分解を行った。その結果、２０時
間後の二酸化炭素の生成量は１１０μｍｏｌであり、酸
化分解による中間生成物は検出されず、また、一酸化炭
素も検出されなかった。<Example 4> Except for using 10 mg of hydrous titanium oxide (trade name: CS-C Ishihara Sangyo Co., Ltd.) having an average particle size of 4.5 nm instead of titanium oxide, ethane was carried out in the same manner as in Example 1. Was disassembled. As a result, the amount of carbon dioxide produced after 20 hours was 110 μmol, no intermediate product due to oxidative decomposition was detected, and neither carbon monoxide was detected.
Claims (1)
チタンおよび／または含水酸化チタンと、酸素の存在下
に有機化合物に光を照射することを特徴とする有機化合
物の分解方法。1. A method of decomposing an organic compound, which comprises irradiating an organic compound with light in the presence of titanium oxide and / or titanium oxide hydrate and oxygen in a perfluoro-inert liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22245592A JP3202801B2 (en) | 1992-08-21 | 1992-08-21 | Organic compound decomposition method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22245592A JP3202801B2 (en) | 1992-08-21 | 1992-08-21 | Organic compound decomposition method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0663178A true JPH0663178A (en) | 1994-03-08 |
| JP3202801B2 JP3202801B2 (en) | 2001-08-27 |
Family
ID=16782686
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22245592A Expired - Fee Related JP3202801B2 (en) | 1992-08-21 | 1992-08-21 | Organic compound decomposition method |
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| Country | Link |
|---|---|
| JP (1) | JP3202801B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4020313A1 (en) * | 1989-06-26 | 1991-01-17 | Hitachi Ltd | THERMAL PRINTER |
-
1992
- 1992-08-21 JP JP22245592A patent/JP3202801B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4020313A1 (en) * | 1989-06-26 | 1991-01-17 | Hitachi Ltd | THERMAL PRINTER |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3202801B2 (en) | 2001-08-27 |
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