CN1332891C - Hydrogen peroxide catalytic decomposing method of phenol compound - Google Patents
Hydrogen peroxide catalytic decomposing method of phenol compound Download PDFInfo
- Publication number
- CN1332891C CN1332891C CNB2004100693711A CN200410069371A CN1332891C CN 1332891 C CN1332891 C CN 1332891C CN B2004100693711 A CNB2004100693711 A CN B2004100693711A CN 200410069371 A CN200410069371 A CN 200410069371A CN 1332891 C CN1332891 C CN 1332891C
- Authority
- CN
- China
- Prior art keywords
- hydrogen peroxide
- acetonitrile
- nitrophenol
- reaction
- catalyst
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 238000000034 method Methods 0.000 title claims abstract description 14
- 230000003197 catalytic effect Effects 0.000 title description 22
- -1 phenol compound Chemical class 0.000 title description 2
- 239000003054 catalyst Substances 0.000 claims abstract description 30
- 150000002989 phenols Chemical class 0.000 claims abstract description 22
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 18
- LYGJENNIWJXYER-UHFFFAOYSA-N nitromethane Chemical compound C[N+]([O-])=O LYGJENNIWJXYER-UHFFFAOYSA-N 0.000 claims abstract description 16
- PBCJIPOGFJYBJE-UHFFFAOYSA-N acetonitrile;hydrate Chemical compound O.CC#N PBCJIPOGFJYBJE-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000003421 catalytic decomposition reaction Methods 0.000 claims abstract description 11
- 238000003756 stirring Methods 0.000 claims abstract description 8
- 150000001449 anionic compounds Chemical class 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 229910001412 inorganic anion Inorganic materials 0.000 claims abstract description 6
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 69
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- 239000000243 solution Substances 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 43
- 238000000354 decomposition reaction Methods 0.000 abstract description 21
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 abstract description 7
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 230000007935 neutral effect Effects 0.000 abstract description 3
- 239000007800 oxidant agent Substances 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 239000012456 homogeneous solution Substances 0.000 description 39
- BTJIUGUIPKRLHP-UHFFFAOYSA-N 4-nitrophenol Chemical compound OC1=CC=C([N+]([O-])=O)C=C1 BTJIUGUIPKRLHP-UHFFFAOYSA-N 0.000 description 33
- 238000006731 degradation reaction Methods 0.000 description 23
- 230000035484 reaction time Effects 0.000 description 20
- 238000010992 reflux Methods 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 6
- IQUPABOKLQSFBK-UHFFFAOYSA-N 2-nitrophenol Chemical compound OC1=CC=CC=C1[N+]([O-])=O IQUPABOKLQSFBK-UHFFFAOYSA-N 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 3
- HORNXRXVQWOLPJ-UHFFFAOYSA-N 3-chlorophenol Chemical compound OC1=CC=CC(Cl)=C1 HORNXRXVQWOLPJ-UHFFFAOYSA-N 0.000 description 3
- RTZZCYNQPHTPPL-UHFFFAOYSA-N 3-nitrophenol Chemical compound OC1=CC=CC([N+]([O-])=O)=C1 RTZZCYNQPHTPPL-UHFFFAOYSA-N 0.000 description 3
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- NWVVVBRKAWDGAB-UHFFFAOYSA-N p-methoxyphenol Chemical compound COC1=CC=C(O)C=C1 NWVVVBRKAWDGAB-UHFFFAOYSA-N 0.000 description 3
- VGVRPFIJEJYOFN-UHFFFAOYSA-N 2,3,4,6-tetrachlorophenol Chemical class OC1=C(Cl)C=C(Cl)C(Cl)=C1Cl VGVRPFIJEJYOFN-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000002917 insecticide Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- YZCKVEUIGOORGS-OUBTZVSYSA-N Deuterium Chemical compound [2H] YZCKVEUIGOORGS-OUBTZVSYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 1
- RBXVOQPAMPBADW-UHFFFAOYSA-N nitrous acid;phenol Chemical class ON=O.OC1=CC=CC=C1 RBXVOQPAMPBADW-UHFFFAOYSA-N 0.000 description 1
- IYDGMDWEHDFVQI-UHFFFAOYSA-N phosphoric acid;trioxotungsten Chemical compound O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.OP(O)(O)=O IYDGMDWEHDFVQI-UHFFFAOYSA-N 0.000 description 1
- 230000000886 photobiology Effects 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 238000013032 photocatalytic reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
本发明公开了属于环境环境治理技术领域的一种酚类化合物的过氧化氢催化分解方法。以钒酸盐或杂多钒酸盐为催化剂,以过氧化氢为氧化剂,和酚类化合物一起加入水-乙腈(4∶1 v/v)溶液中,在加热搅拌条件下进行催化分解反应,使酚类化合物的分解转化率达到97%以上。本发明可使难降解的酚类化合物在中性水-乙腈溶液中,高效快速催化分解为CO2和相应的无机阴离子和硝基甲烷或乙酸。The invention discloses a hydrogen peroxide catalytic decomposition method for phenolic compounds, which belongs to the technical field of environmental treatment. Using vanadate or heteropolyvanadate as a catalyst, hydrogen peroxide as an oxidant, and phenolic compounds are added to a water-acetonitrile (4:1 v/v) solution, and the catalytic decomposition reaction is carried out under heating and stirring conditions. Make the decomposition conversion rate of phenolic compounds reach more than 97%. The invention can decompose the refractory phenolic compound into CO 2 and corresponding inorganic anion and nitromethane or acetic acid with high efficiency and rapid catalysis in neutral water-acetonitrile solution.
Description
技术领域technical field
本发明属于环境治理技术领域,特别涉及一种酚类化合物的过氧化氢催化分解方法。The invention belongs to the technical field of environmental treatment, and in particular relates to a hydrogen peroxide catalytic decomposition method of phenolic compounds.
背景技术Background technique
化学工业的快速发展而导致的环境问题已成为当今世界密切关注的焦点之一。工业废水中的酚类化合物是主要污染物,例如作为杀虫剂、消毒剂、木材防腐剂而被广泛使用的氯酚;作为杀虫剂、染料、炸药、在纺织品和纸的制备等工业过程中广泛使用的硝基酚等。这些被排放的工业废水中的酚类化合物即使在很低的浓度下对环境仍有极大的污染,而这些化合物由于它们的稳定性,很难用生物降解的方法进行处理。目前使用的化学方法主要有:化学氧化法和光催化分解法。Miguel L.Rodriguez,Vitaliy I.Timokhin,等在文献“Advances inEnvironmental Research 7(2003)583-595”中报导,化学氧化法并不能使酚完全分解。而C.-H.Yoon,S.-H.Cho,S.-H.Kim and S.-R.Ha,等在文献“WaterScience and Technology Vol43,No.2,pp.229-236”中报导,湿空气氧化法必须在高温高压下进行,催化剂易失活,处理费用高。P.V.Kamat,在“Chem.Rev.3(1993)267”中报导,光催化分解法主要是在紫外可见光照射下,在双氧水或臭氧或二氧化钛存在下,使酚类化合物分解成可生物降解的有机小分子、CO2和相应的被矿化的无机阴离子。在文献“A.Mylonas,E.Papaconstantinou,J.Photochemistry and Photobiology A:Chemistry 94(1996)77-82”、“A.Hiskia,E.Androulaki et al.Res.Chem.Intermed.Vol.26,No.3,pp.235-251(2000)”和“P.Kormali,D.Dimoticali,E.Papaconstantinou,et al.AppliedCatalysis B:Enviromental 48(2004)175-183)”中报导,Keggin型磷钨酸被发现是一种与二氧化钛同样有效的光催化剂,可使氯酚分解为二氧化碳和盐酸。然而,这种光催化反应是在酸性条件下进行的(pH~2),对于更难分解的硝基酚的催化降解未见报导。The environmental problems caused by the rapid development of the chemical industry have become one of the focuses that the world pays close attention to. Phenolic compounds in industrial wastewater are the main pollutants, such as chlorophenols, which are widely used as insecticides, disinfectants, wood preservatives; industrial processes such as insecticides, dyes, explosives, in the preparation of textiles and paper Nitrophenols are widely used in The phenolic compounds in these discharged industrial wastewaters still pollute the environment greatly even at very low concentrations, and these compounds are difficult to treat with biodegradable methods due to their stability. The chemical methods currently used mainly include chemical oxidation and photocatalytic decomposition. Miguel L. Rodriguez, Vitaliy I. Timokhin, etc. reported in the literature "Advances in Environmental Research 7 (2003) 583-595" that the chemical oxidation method cannot completely decompose phenol. And C.-H.Yoon, S.-H.Cho, S.-H.Kim and S.-R.Ha, etc. reported in the literature "WaterScience and Technology Vol43, No.2, pp.229-236" , The wet air oxidation method must be carried out under high temperature and high pressure, the catalyst is easily deactivated, and the treatment cost is high. PVKamat, reported in "Chem.Rev.3 (1993) 267", the photocatalytic decomposition method is mainly to decompose phenolic compounds into biodegradable organic small compounds under the irradiation of ultraviolet and visible light in the presence of hydrogen peroxide or ozone or titanium dioxide. molecules, CO 2 and the corresponding mineralized inorganic anions. In the literature "A. Mylonas, E. Papaconstantinou, J. Photochemistry and Photobiology A: Chemistry 94 (1996) 77-82", "A. Hiskia, E. Androulaki et al. Res. Chem. Intermed. Vol.26, No. .3, pp.235-251(2000)" and "P.Kormali, D.Dimoticali, E.Papaconstantinou, et al.AppliedCatalysis B:Enviromental 48(2004) 175-183)", Keggin-type phosphotungstic acid Found to be a photocatalyst as effective as titanium dioxide for decomposing chlorophenols into carbon dioxide and hydrochloric acid. However, this photocatalytic reaction is carried out under acidic conditions (pH ~ 2), and the catalytic degradation of the more recalcitrant nitrophenol has not been reported.
发明内容Contents of the invention
本发明的目的是提供一种酚类化合物的过氧化氢催化分解方法,其特征在于以钒酸盐或杂多钒酸盐为催化剂,过氧化氢水溶液为氧化剂,在水-乙腈混合溶液中,加热、搅拌,进行酚类化合物的催化分解反应,该体系催化降解反应包括以下步骤:The object of this invention is to provide a kind of hydrogen peroxide catalytic decomposition method of phenolic compound, it is characterized in that with vanadate or heteropolyvanadate as catalyst, hydrogen peroxide aqueous solution is oxygenant, in water-acetonitrile mixed solution, Heating, stirring, carrying out the catalytic decomposition reaction of phenolic compound, this system catalytic degradation reaction comprises the following steps:
1)将(20-70)μmol的钒酸盐或(2-6)μmol杂多钒酸盐催化剂溶于(1-8)ml,30%(v/v)双氧水中,按水-乙腈(4∶1 v/v)与乙腈配成10ml均一水溶液;1) (20-70) μ mol vanadate or (2-6) μ mol heteropolyvanadate catalyst is dissolved in (1-8) ml, 30% (v/v) hydrogen peroxide, press water-acetonitrile ( 4:1 v/v) and acetonitrile to make 10ml homogeneous aqueous solution;
2)将酚类化合物溶于步骤(1)中含有催化剂和过氧化氢的水-乙腈溶液中(4∶1v/v),加热30-70℃,在搅拌下反应10-120分钟,酚类化合物分解为CO2、H2O和相应的无机阴离子和硝基甲烷或乙酸。2) Dissolving the phenolic compound in the water-acetonitrile solution (4:1v/v) containing the catalyst and hydrogen peroxide in step (1), heating at 30-70°C, and reacting for 10-120 minutes under stirring, the phenolic compound The compounds decompose into CO 2 , H 2 O and the corresponding inorganic anions and nitromethane or acetic acid.
所述钒酸盐为KVO3,、NaVO3,或NH4VO3。The vanadate is KVO 3 , NaVO 3 , or NH 4 VO 3 .
所述杂多钒酸盐为K7NiV13O38和K7MnV13O38。The heteropolyvanadate is K 7 NiV 13 O 38 and K 7 MnV 13 O 38 .
本发明的有益效果是:本发明与现有技术比,使硝基酚等难降解的酚类化合物在中性条件下,快速高效分解为CO2和相应的无机阴离子和硝基甲烷或乙酸。使各类酚的分解转化率达到97%以上。The beneficial effects of the present invention are: compared with the prior art, the present invention enables the refractory phenolic compounds such as nitrophenol to be rapidly and efficiently decomposed into CO2 and corresponding inorganic anions and nitromethane or acetic acid under neutral conditions. The decomposition conversion rate of various phenols can reach more than 97%.
具体实施方式Detailed ways
本发明为新的一种酚类化合物的过氧化氢催化降解方法。是以钒酸盐或杂多钒酸盐为催化剂,以过氧化氢为氧化剂,在水-乙腈(4∶1v/v)混合溶剂加热搅拌条件下进行酚类芳烃化合物的催化分解反应,该体系催化分解反应包括以下步骤:The invention is a new hydrogen peroxide catalytic degradation method for phenolic compounds. Using vanadate or heteropolyvanadate as a catalyst, hydrogen peroxide as an oxidant, the catalytic decomposition reaction of phenolic aromatic compounds is carried out under the condition of heating and stirring in a water-acetonitrile (4:1v/v) mixed solvent. The catalytic decomposition reaction includes the following steps:
1)将优选40μmol的钒酸盐或3μmol杂多钒酸盐催化剂溶于(1-8)ml,30%(v/v)双氧水中,按水-乙腈(4∶1v/v)与乙腈配成10ml均一水溶液;1) Dissolve the preferred 40 μmol of vanadate or 3 μmol of heteropolyvanadate catalyst in (1-8) ml, 30% (v/v) hydrogen peroxide, and mix with acetonitrile according to water-acetonitrile (4: 1v/v) into 10ml homogeneous aqueous solution;
2)将酚类化合物溶于(1)中含有催化剂和过氧化氢的水-乙腈溶液中,加热30-70℃,在搅拌下反应10-120分钟,酚类化合物降解为CO2、H2O和相应的无机盐和少量的酚类有机降解小分子(如硝基甲烷或乙酸)。2) Dissolving the phenolic compound in the water-acetonitrile solution containing the catalyst and hydrogen peroxide in (1), heating at 30-70°C, and reacting for 10-120 minutes under stirring, the phenolic compound is degraded into CO 2 , H 2 O and corresponding inorganic salts and a small amount of phenolic organic degradation small molecules (such as nitromethane or acetic acid).
上述钒酸盐为KVO3,、NaVO3,或NH4VO3;杂多钒酸盐为K7NiV13O38或K7MnV13O38。The aforementioned vanadate is KVO 3 , NaVO 3 , or NH 4 VO 3 ; the heteropolyvanadate is K 7 NiV 13 O 38 or K 7 MnV 13 O 38 .
下面再举实施例对本发明予以进一步说明。The following examples are given to further illustrate the present invention.
实施例1:Example 1:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到99.2%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve in 8 ml of 30% hydrogen peroxide and 2 ml of acetonitrile to prepare a homogeneous solution. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 99.2%.
实施例2:Example 2:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至50℃进行催化降解反应。反应时间为40分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到98.7%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 50°C for catalytic degradation reaction. The reaction time is 40 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 98.7%.
实施例3:Example 3:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至30℃进行催化降解反应。反应时间为10小时,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到99.5%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 30°C for catalytic degradation reaction. The reaction time is 10 hours, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 99.5%.
实施例4:Example 4:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于1ml30%(v/v)双氧水中,与2ml乙腈和7ml水配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为60分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到53%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 1 ml of 30% (v/v) hydrogen peroxide, and prepare a homogeneous solution with 2 ml of acetonitrile and 7 ml of water. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 60 minutes, and the result of the reaction is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 53%.
实施例5:Example 5:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于2ml30%(v/v)双氧水中,与2ml乙腈和6ml水配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为60分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到66.5%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 2 ml of 30% (v/v) hydrogen peroxide, and prepare a homogeneous solution with 2 ml of acetonitrile and 6 ml of water. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 60 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 66.5%.
实施例6:Embodiment 6:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于3ml30%(v/v)双氧水中,与2ml乙腈和5ml水配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为30分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到88%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 3 ml of 30% (v/v) hydrogen peroxide, and prepare a homogeneous solution with 2 ml of acetonitrile and 5 ml of water. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 30 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 88%.
实施例7:Embodiment 7:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于4ml30%(v/v)双氧水中,与2ml乙腈和4ml水配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为30分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到91%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 4 ml of 30% (v/v) hydrogen peroxide, and prepare a homogeneous solution with 2 ml of acetonitrile and 4 ml of water. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 30 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 91%.
实施例8:Embodiment 8:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于6ml30%(v/v)双氧水中,与2ml乙腈和2ml水配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为30分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到94%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 6 ml of 30% (v/v) hydrogen peroxide, and prepare a homogeneous solution with 2 ml of acetonitrile and 2 ml of water. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 30 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 94%.
实施例9:Embodiment 9:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)邻硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:邻硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,邻硝基苯酚的分解转化率达到97.5%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-necked round bottom flask, 0.57g (4mmol) of o-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is that o-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of o-nitrophenol reaches 97.5%.
实施例10:Example 10:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)间硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:间硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,间硝基苯酚的分解转化率达到99%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.57g (4mmol) m-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the result of the reaction is that m-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of m-nitrophenol reaches 99%.
实施例11:Example 11:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.38g(4mmol)对苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为60分钟,反应结果是:苯酚分解为CO2和水和少量的丙酮,苯酚的分解转化率达到97.5%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.38g (4mmol) of p-phenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 60 minutes, and the reaction result is: phenol is decomposed into CO 2 and water and a small amount of acetone, and the decomposition conversion rate of phenol reaches 97.5%.
实施例12:Example 12:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.51g(4mmol)对氯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:对氯酚分解为CO2和Cl-,对氯酚的分解转化率达到98.5%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.51g (4mmol) of p-chlorophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is that p-chlorophenol is decomposed into CO 2 and Cl - , and the conversion rate of p-chlorophenol reaches 98.5%.
实施例13:Example 13:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.51g(4mmol)邻氯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:邻氯酚分解为CO2和Cl-,邻氯酚的分解转化率达到98%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-necked round bottom flask, 0.51g (4mmol) o-chlorophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is that o-chlorophenol is decomposed into CO 2 and Cl - , and the decomposition conversion rate of o-chlorophenol reaches 98%.
实施例14:Example 14:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.51g(4mmol)间氯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:间氯酚分解为CO2和Cl-,间氯酚的分解转化率达到99%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.51g (4mmol) m-chlorophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is that m-chlorophenol is decomposed into CO 2 and Cl - , and the conversion rate of m-chlorophenol reaches 99%.
实施例15:Example 15:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.43g(4mmol)对甲基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为120分钟,反应结果是:对甲基苯酚分解为CO2和水,对甲基苯酚的分解转化率达到99.1%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.43g (4mmol) p-cresol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 120 minutes, and the reaction result is: p-cresol is decomposed into CO and water, and the decomposition conversion rate of p-cresol reaches 99.1%.
实施例16:Example 16:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.5g(4mmol)对羟基苯甲醚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为60分钟,反应结果是:对羟基苯甲醚分解为CO2和水,对羟基苯甲醚的分解转化率达到99.2%。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-neck round bottom flask, 0.5g (4mmol) p-hydroxyanisole was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 60 minutes, and the reaction result is that p-hydroxyanisole is decomposed into CO and water, and the decomposition conversion rate of p-hydroxyanisole reaches 99.2%.
实施例17:Example 17:
称取5.3mg(3μmol)KVO3催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和乙酸,对硝基苯酚的分解转化率达到99.5%。Weigh 5.3 mg (3 μmol) of KVO 3 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and mix with 2 ml of acetonitrile to form a homogeneous solution. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is: p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and acetic acid, and the decomposition conversion rate of p-nitrophenol reaches 99.5%.
实施例18:Example 18:
称取5.7mg(3μmol)K7MnV13O38催化剂,溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行催化降解反应。反应时间为15分钟,反应结果是:对硝基苯酚分解为CO2,NO3 -和少量的NO2 -和硝基甲烷,对硝基苯酚的分解转化率达到99%。Weigh 5.7 mg (3 μmol) of K 7 MnV 13 O 38 catalyst, dissolve it in 8 ml of 30% (v/v) hydrogen peroxide and prepare a homogeneous solution with 2 ml of acetonitrile. In a 50ml two-necked round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for catalytic degradation reaction. The reaction time is 15 minutes, and the reaction result is that p-nitrophenol is decomposed into CO 2 , NO 3 - and a small amount of NO 2 - and nitromethane, and the decomposition conversion rate of p-nitrophenol reaches 99%.
对比例1:Comparative example 1:
在无催化剂条件下,将0.57g(4mmol)对硝基苯溶于8ml30%(v/v)双氧水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,搅拌,加热回流至70℃进行反应。反应时间为120分钟,反应结果是:对硝基苯酚分解转化率只有15%。Under the condition of no catalyst, 0.57g (4mmol) of p-nitrobenzene was dissolved in 8ml of 30% (v/v) hydrogen peroxide and 2ml of acetonitrile to form a homogeneous solution. In a 50ml two-neck round bottom flask, stir, and heat to reflux to 70°C for reaction. The reaction time is 120 minutes, and the result of the reaction is that the decomposition conversion rate of p-nitrophenol is only 15%.
对比例2:Comparative example 2:
称取5.7mg(3μmol)K7NiV13O38催化剂,溶于8ml水中与2ml乙腈配成均一溶液。在50ml二颈圆底烧瓶中,将0.57g(4mmol)对硝基苯酚溶于上述均一溶液中,搅拌,加热回流至70℃进行反应。反应时间为120分钟,反应结果是:对硝基苯酚几乎不分解。Weigh 5.7 mg (3 μmol) of K 7 NiV 13 O 38 catalyst, dissolve in 8 ml of water and 2 ml of acetonitrile to prepare a homogeneous solution. In a 50ml two-neck round bottom flask, 0.57g (4mmol) p-nitrophenol was dissolved in the above homogeneous solution, stirred, and heated to reflux to 70°C for reaction. The reaction time was 120 minutes, and the reaction result was that p-nitrophenol hardly decomposed.
通过上面实施例的对比,可以得出本发明使酚类化合物在中性条件下,高效快速的催化分解为CO2和相应的无机阴离子和少量的酚类有机降解小分子。Through the comparison of the above examples, it can be concluded that the present invention can efficiently and rapidly decompose phenolic compounds into CO2 and corresponding inorganic anions and a small amount of phenolic organic degradation small molecules under neutral conditions.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2004100693711A CN1332891C (en) | 2004-07-21 | 2004-07-21 | Hydrogen peroxide catalytic decomposing method of phenol compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2004100693711A CN1332891C (en) | 2004-07-21 | 2004-07-21 | Hydrogen peroxide catalytic decomposing method of phenol compound |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1587095A CN1587095A (en) | 2005-03-02 |
CN1332891C true CN1332891C (en) | 2007-08-22 |
Family
ID=34604347
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2004100693711A Expired - Fee Related CN1332891C (en) | 2004-07-21 | 2004-07-21 | Hydrogen peroxide catalytic decomposing method of phenol compound |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1332891C (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1056893A (en) * | 1991-07-04 | 1991-12-11 | 东北煤气化设计研究所 | Gas sewage extracting and dephenolizing, ammonia still process treatment process |
CN1133600A (en) * | 1993-07-29 | 1996-10-16 | 普罗格特-甘布尔公司 | Oxidation process |
CN1150128A (en) * | 1995-11-15 | 1997-05-21 | 陶荣达 | paper mill sewage treatment process |
-
2004
- 2004-07-21 CN CNB2004100693711A patent/CN1332891C/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1056893A (en) * | 1991-07-04 | 1991-12-11 | 东北煤气化设计研究所 | Gas sewage extracting and dephenolizing, ammonia still process treatment process |
CN1133600A (en) * | 1993-07-29 | 1996-10-16 | 普罗格特-甘布尔公司 | Oxidation process |
CN1150128A (en) * | 1995-11-15 | 1997-05-21 | 陶荣达 | paper mill sewage treatment process |
Non-Patent Citations (1)
Title |
---|
光催化氧化处理污水的研究 河北化工,第1期 2002 * |
Also Published As
Publication number | Publication date |
---|---|
CN1587095A (en) | 2005-03-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Torres-Pinto et al. | Metal-free carbon nitride photocatalysis with in situ hydrogen peroxide generation for the degradation of aromatic compounds | |
Singh et al. | Role of electrocatalysis in the remediation of water pollutants | |
Lee et al. | Photosensitized oxidation of emerging organic pollutants by tetrakis C60 aminofullerene-derivatized silica under visible light irradiation | |
Kadam et al. | Advancement in methodologies for reduction of nitroarenes | |
Fan et al. | Review on the treatment of organic wastewater by discharge plasma combined with oxidants and catalysts | |
Shiraishi et al. | One-pot synthesis of imines from alcohols and amines with TiO 2 loading Pt nanoparticles under UV irradiation | |
Barakat et al. | Hydrogen peroxide-assisted photocatalytic oxidation of phenolic compounds | |
Wang et al. | Selective oxidation of various phenolic contaminants by activated persulfate via the hydrogen abstraction pathway | |
CN102491450B (en) | Method for treating dye waste water by using ultraviolet-acetylacetone oxidation treatment process | |
Huang et al. | Photocatalytic destruction of air pollutants with vacuum ultraviolet (VUV) irradiation | |
Munir et al. | Development of photocatalysts for selective and efficient organic transformations | |
Porcar-Santos et al. | Photocatalytic degradation of sulfamethoxazole using TiO2 in simulated seawater: Evidence for direct formation of reactive halogen species and halogenated by-products | |
Ghali et al. | New hybrid polyoxometalate/polymer composites for photodegradation of eosin dye | |
CN103990494A (en) | Heterogeneous cage-form metal complex catalyst as well as preparation method and application thereof | |
CN102874914A (en) | Method for removing pollutants from drinking water by using supported ruthenium catalyst | |
Das et al. | Reusable floating polymer nanocomposite photocatalyst for the efficient treatment of dye wastewaters under scaled‐up conditions in batch and recirculation modes | |
CN101518742B (en) | Iron composition visible light photocatalyst composed of double-coordination functional group ligands and iron ions and preparation method and purpose thereof | |
CN100388979C (en) | Method for degrading organic pollutant by light catalyst and its special solid-phase light catalyst | |
Lara-Ramos et al. | Evaluation of caffeine degradation by sequential coupling of TiO 2/O 3/H 2 O 2/UV processes | |
CN103691464B (en) | A kind of catalyst for the low-temperature catalyzed hydrogenation elimination of chlorophenol compounds in water and preparation and application thereof | |
Mancuso et al. | Photoreactive polymer composite for selective oxidation of benzene to phenol | |
CN102921143A (en) | Method for efficiently degrading chlorinated phenolic compound | |
CN1332891C (en) | Hydrogen peroxide catalytic decomposing method of phenol compound | |
Vibbert et al. | On-demand photochemical synthesis of hydrogen peroxide from alkylated anthraquinones | |
CN106831284A (en) | It is a kind of to be catalyzed the method that carbon-carbon double bond oxidation scission prepares aldehyde ketone |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Hebei Hongyuan Chemical Co., Ltd. Assignor: Tsinghua University Contract fulfillment period: 2008.12.26 to 2013.12.25 contract change Contract record no.: 2009130000001 Denomination of invention: Hydrogen peroxide catalytic decomposing method of phenol compound Granted publication date: 20070822 License type: Exclusive license Record date: 2009.1.12 |
|
LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.12.26 TO 2013.12.25; CHANGE OF CONTRACT Name of requester: HEBEI HONGYUAN CHEMICAL CO., LTD. Effective date: 20090112 |
|
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070822 Termination date: 20130721 |