CN102603618A - Biphenyl compound, synthetic method and application thereof - Google Patents
Biphenyl compound, synthetic method and application thereof Download PDFInfo
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- 239000004305 biphenyl Substances 0.000 title claims abstract description 14
- -1 Biphenyl compound Chemical class 0.000 title claims abstract description 12
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 title claims abstract description 10
- 235000010290 biphenyl Nutrition 0.000 title claims abstract description 9
- 238000010189 synthetic method Methods 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000003054 catalyst Substances 0.000 claims abstract description 29
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 239000002904 solvent Substances 0.000 claims abstract description 6
- 238000006266 etherification reaction Methods 0.000 claims abstract 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 15
- 230000003647 oxidation Effects 0.000 claims description 14
- 238000007254 oxidation reaction Methods 0.000 claims description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 9
- UZGLOGCJCWBBIV-UHFFFAOYSA-N 3-(chloromethyl)pyridin-1-ium;chloride Chemical compound Cl.ClCC1=CC=CN=C1 UZGLOGCJCWBBIV-UHFFFAOYSA-N 0.000 claims description 8
- 239000011230 binding agent Substances 0.000 claims description 8
- 238000010898 silica gel chromatography Methods 0.000 claims description 8
- 239000011521 glass Substances 0.000 claims description 7
- 238000010992 reflux Methods 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 229910020366 ClO 4 Inorganic materials 0.000 claims description 4
- 239000003480 eluent Substances 0.000 claims description 4
- 239000012074 organic phase Substances 0.000 claims description 4
- 239000000376 reactant Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 239000012065 filter cake Substances 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 claims 6
- 239000004327 boric acid Substances 0.000 claims 3
- 150000002978 peroxides Chemical class 0.000 claims 3
- 238000002156 mixing Methods 0.000 claims 1
- 238000000967 suction filtration Methods 0.000 claims 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 68
- 150000001879 copper Chemical class 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000006069 Suzuki reaction reaction Methods 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 238000001308 synthesis method Methods 0.000 abstract description 3
- 238000003786 synthesis reaction Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 abstract description 2
- 239000013067 intermediate product Substances 0.000 abstract description 2
- 239000003960 organic solvent Substances 0.000 abstract description 2
- 239000010891 toxic waste Substances 0.000 abstract description 2
- QRFMXBKGNQEADL-UHFFFAOYSA-N 1,1'-biphenyl;phenol Chemical compound OC1=CC=CC=C1.OC1=CC=CC=C1.C1=CC=CC=C1C1=CC=CC=C1 QRFMXBKGNQEADL-UHFFFAOYSA-N 0.000 abstract 1
- 238000004458 analytical method Methods 0.000 abstract 1
- 230000031709 bromination Effects 0.000 abstract 1
- 238000005893 bromination reaction Methods 0.000 abstract 1
- 238000004440 column chromatography Methods 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 19
- 239000010949 copper Substances 0.000 description 16
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 8
- VCUVETGKTILCLC-UHFFFAOYSA-N 5,5-dimethyl-1-pyrroline N-oxide Chemical compound CC1(C)CCC=[N+]1[O-] VCUVETGKTILCLC-UHFFFAOYSA-N 0.000 description 6
- 239000002516 radical scavenger Substances 0.000 description 6
- QLULGIRFKAWHOJ-UHFFFAOYSA-N pyridin-4-ylboronic acid Chemical compound OB(O)C1=CC=NC=C1 QLULGIRFKAWHOJ-UHFFFAOYSA-N 0.000 description 5
- FCTQSFVLYRQKTR-UHFFFAOYSA-N 4-bromo-2-(5-bromo-2-hydroxyphenyl)phenol Chemical compound OC1=CC=C(Br)C=C1C1=CC(Br)=CC=C1O FCTQSFVLYRQKTR-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 239000002957 persistent organic pollutant Substances 0.000 description 4
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- 239000006227 byproduct Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003446 ligand Substances 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 description 2
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- IMHDGJOMLMDPJN-UHFFFAOYSA-N biphenyl-2,2'-diol Chemical compound OC1=CC=CC=C1C1=CC=CC=C1O IMHDGJOMLMDPJN-UHFFFAOYSA-N 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 150000004056 anthraquinones Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 1
- YRNNKGFMTBWUGL-UHFFFAOYSA-L copper(ii) perchlorate Chemical compound [Cu+2].[O-]Cl(=O)(=O)=O.[O-]Cl(=O)(=O)=O YRNNKGFMTBWUGL-UHFFFAOYSA-L 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
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- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
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Abstract
本发明公开了一种联苯类化合物及其合成方法和应用,化合物(其结构式如下)的具体合成路线是从原料2,2’-联苯二酚出发,经过溴代、醚化、柱层析得到中间体B,再经suzuki偶联反应、柱层析得到催化剂。该催化剂在水热条件下与金属铜盐可以催化氧化水产生双氧水。本发明采用水热清洁生产工艺,溶剂只用到了纯水,无有机溶剂添加,不会产生有毒废气,不需要分离中间产物,缩短了工艺流程。 The invention discloses a biphenyl compound and its synthesis method and application. The specific synthesis route of the compound (its structural formula is as follows) starts from the raw material 2,2'-biphenyl diphenol, and undergoes bromination, etherification, column layer The intermediate B was obtained by analysis, and then the catalyst was obtained by suzuki coupling reaction and column chromatography. The catalyst can catalyze and oxidize water to produce hydrogen peroxide under hydrothermal condition with metal copper salt. The invention adopts a hydrothermal cleaning production process, only pure water is used as a solvent, no organic solvent is added, no toxic waste gas is produced, no intermediate product needs to be separated, and the process flow is shortened.
Description
技术领域 technical field
本发明涉及一种联苯类化合物及其合成方法和应用。The invention relates to a biphenyl compound and its synthesis method and application.
背景技术 Background technique
双氧水在医学、军工及工业上都有广泛的应用,且随着城市化规模的不断扩大,含有高浓度有机废水的污染源日益增多,对有机污染物的降解技术成为有效解决污水处理难题的首要选择,以双氧水处理有机污染物成为目前废水处理方面的有效手段,其原因是由于双氧水分解得到的羟基自由基(·OH)具有极高的氧化电位(2.8V),其氧化能力极强,与大部分有机污染物都可以发生快速的链式反应,把有害物质氧化成CO2、H2O或矿物盐,无二次污染。目前各国生产双氧水的技术基本上都是采用1958年杜邦公司的蒽醌法制备,该方法是以烷基蒽醌为媒介物,循环氧化还原制得双氧水,但该技术成本较高,且在生产双氧水过程中,排出含有大量三甲苯和二甲苯的废气以及含大量有机污染物的废水。Hydrogen peroxide is widely used in medicine, military industry and industry, and with the continuous expansion of urbanization scale, pollution sources containing high-concentration organic wastewater are increasing, and the degradation technology of organic pollutants has become the first choice to effectively solve the problem of sewage treatment At present, the treatment of organic pollutants with hydrogen peroxide has become an effective means of wastewater treatment. The reason is that the hydroxyl radical (OH) obtained by the decomposition of hydrogen peroxide has a very high oxidation potential (2.8V), and its oxidation ability is extremely strong. Some organic pollutants can undergo a rapid chain reaction to oxidize harmful substances into CO 2 , H 2 O or mineral salts without secondary pollution. At present, the technologies for producing hydrogen peroxide in various countries are basically prepared by the anthraquinone method of DuPont Company in 1958. This method uses alkyl anthraquinone as a medium to produce hydrogen peroxide through cyclic oxidation and reduction, but the cost of this technology is relatively high. During the hydrogen peroxide process, waste gas containing a large amount of trimethylbenzene and xylene and waste water containing a large amount of organic pollutants are discharged.
发明内容 Contents of the invention
本发明的目的是为克服上述现有技术的不足,提供一种联苯类化合物,其能够在水热条件下与铜盐(硝酸铜,高氯酸铜,三氟磺酸铜)共同催化氧化水产生双氧水的新型催化剂,该项发明在清洁生产双氧水方面有望得到广泛的应用前景,实现双氧水的绿色生产。The purpose of the present invention is to overcome above-mentioned deficiencies in the prior art, and a kind of biphenyl compound is provided, and it can co-catalyze oxidation with copper salt (copper nitrate, copper perchlorate, copper trifluorosulfonate) under hydrothermal condition A new type of catalyst for producing hydrogen peroxide from water. This invention is expected to have wide application prospects in the clean production of hydrogen peroxide and realize the green production of hydrogen peroxide.
本发明还提供了该联苯类化合物的合成方法。The invention also provides a synthesis method of the biphenyl compound.
本发明还提供了使用联苯类化合物催化氧化水产生双氧水的方法。The invention also provides a method for producing hydrogen peroxide by using biphenyl compounds to catalyze and oxidize water.
为实现上述目的,本发明采用下述技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种联苯类化合物,其化学命名为5,5’-二(4-吡啶基)-2,2’-联苯二酚二-3-吡啶甲醚,其结构式如下:A kind of biphenyl compound, its chemical designation is 5,5'-bis(4-pyridyl)-2,2'-biphenyldiol bis-3-pyridine methyl ether, and its structural formula is as follows:
上述联苯类化合物的合成方法,包括以下步骤:The synthetic method of above-mentioned biphenyl compound, comprises the following steps:
(1)以5,5’-二溴-2,2’-联苯二酚为原料,与3-氯甲基吡啶盐酸盐发生醚化反应制得中间体B,中间体B结构如下:(1) Use 5,5'-dibromo-2,2'-biphenyldiol as raw material, and react with 3-chloromethylpyridine hydrochloride to produce intermediate B. The structure of intermediate B is as follows:
(2)将中间体B与吡啶-4-硼酸发生suzuki偶联反应制成目标化合物。(2) Suzuki coupling reaction between intermediate B and pyridine-4-boronic acid to prepare the target compound.
步骤(1)具体为:以5,5’-二溴-2,2’-联苯二酚为原料,与3-氯甲基吡啶盐酸盐、缚酸剂K2CO3、催化剂KI在DMF中常温搅拌24-36h,将反应物倒入水中,抽滤,滤饼硅胶柱层析,洗脱剂为CH2Cl2∶CH3OH=25∶1v/v,制得中间体B;其中5,5’-二溴-2,2’-联苯二酚与3-氯甲基吡啶盐酸盐投料摩尔比为1∶(2-2.5)。Step (1) is specifically: using 5,5'-dibromo-2,2'-diphenol as raw material, and 3-chloromethylpyridine hydrochloride, acid-binding agent K 2 CO 3 , and catalyst KI in the Stir in DMF at room temperature for 24-36 hours, pour the reactant into water, filter with suction, and perform silica gel column chromatography on the filter cake, the eluent is CH 2 Cl 2 : CH 3 OH=25:1 v/v to obtain intermediate B; The molar ratio of 5,5'-dibromo-2,2'-biphenyldiol to 3-chloromethylpyridine hydrochloride is 1:(2-2.5).
步骤(1)中缚酸剂K2CO3、催化剂KI与5,5’-二溴-2,2’-联苯二酚的投料摩尔比(15-20)∶(0.3-0.5)∶1。In step (1), the molar ratio of acid-binding agent K 2 CO 3 , catalyst KI and 5,5'-dibromo-2,2'-biphenyldiol (15-20):(0.3-0.5):1 .
步骤(1)中DMF的与5,5’-二溴-2,2’-联苯二酚的摩尔比为1∶30-34。In the step (1), the molar ratio of DMF to 5,5'-dibromo-2,2'-diphenol is 1:30-34.
步骤(2)具体为:N2保护下,将中间体B、吡啶-4-硼酸、缚酸剂K2CO3置于反应容器中,以甲苯、乙醇和水按体积比为1∶1∶1配制的混合溶液作溶剂,加入催化剂Pd(PPh3)4,加热回流,控制温度在90℃-110℃,控制回流时间在24-36h,TLC跟踪,反应结束后静置,冷却,分液,有机相旋干,硅胶柱层析,洗脱剂为CH2Cl2∶CH3OH=20∶1v/v,得催化剂;其中中间体B与吡啶-4-硼酸的摩尔比为1∶(2-2.5)。Step (2) is specifically: under the protection of N 2 , intermediate B, pyridine-4-boronic acid, and acid-binding agent K 2 CO 3 are placed in a reaction vessel, and the volume ratio of toluene, ethanol and water is 1:1: 1 Prepare the mixed solution as a solvent, add catalyst Pd(PPh 3 ) 4 , heat to reflux, control the temperature at 90°C-110°C, control the reflux time at 24-36h, TLC tracking, let stand after the reaction, cool, and separate the liquid , the organic phase was spin-dried, silica gel column chromatography, the eluent was CH 2 Cl 2 :CH 3 OH=20:1v/v, and the catalyst was obtained; wherein the molar ratio of intermediate B to pyridine-4-boronic acid was 1:( 2-2.5).
步骤(2)缚酸剂K2CO3、催化剂Pd(PPh3)4与中间体B的投料摩尔比为(12-15)∶0.1∶1。Step (2) The molar ratio of acid-binding agent K 2 CO 3 , catalyst Pd(PPh 3 ) 4 and intermediate B is (12-15):0.1:1.
步骤(2)中所述以甲苯、乙醇和水配制的混合溶液与中间体B的摩尔比为450-500∶1。The molar ratio of the mixed solution prepared with toluene, ethanol and water to the intermediate B in step (2) is 450-500:1.
上述的化合物在催化氧化水的反应中的应用。The application of the above-mentioned compound in the reaction of catalyzing the oxidation of water.
应用的具体方法是:将催化剂、铜盐和水按摩尔比为1∶(4-6)∶(100-120)密封在玻璃管中,在145-150℃,恒温3800-4320min,然后经过2800-3000min降至25-30℃,得到含双氧水的溶液。The specific method of application is: the molar ratio of catalyst, copper salt and water is 1: (4-6): (100-120) sealed in a glass tube, at 145-150 ° C, constant temperature 3800-4320min, and then through 2800 -3000min to 25-30°C to obtain a solution containing hydrogen peroxide.
将催化剂、铜盐和水在玻璃管中,在150℃恒温4320min,然后经过3000min降至30℃,得到含双氧水的溶液。Put the catalyst, copper salt and water in a glass tube at a constant temperature of 150°C for 4320min, and then drop it to 30°C after 3000min to obtain a solution containing hydrogen peroxide.
所述铜盐为Cu(NO3)2·6H2O、Cu(ClO4)2·6H2O或Cu(SO3CF3)2。The copper salt is Cu(NO 3 ) 2 ·6H 2 O, Cu(ClO 4 ) 2 ·6H 2 O or Cu(SO 3 CF 3 ) 2 .
本发明合成的催化剂的合成路线如下所示:The synthesis route of the catalyst synthesized by the present invention is as follows:
a:以2,2’-Biphenol为原料合成中间体Ba: Synthesis of intermediate B using 2,2'-Biphenol as raw material
b:通过Suzuki反应合成催化剂Lb: Catalyst L synthesized by Suzuki reaction
与以往得到双氧水经典方法相比,本发明具有以下有益效果:Compared with the classic method of obtaining hydrogen peroxide in the past, the present invention has the following beneficial effects:
1、采用水热清洁生产工艺,溶剂只用到了纯水,无有机溶剂添加,不会产生有毒废气,不需要分离中间产物,缩短了工艺流程。1. The hydrothermal cleaning production process is adopted. The solvent only uses pure water, no organic solvent is added, no toxic waste gas is produced, no intermediate products need to be separated, and the process flow is shortened.
2、作为副产物的黄色一价铜盐的聚合物,可以直接从溶液中析出,使双氧水溶液与副产物通过简单的过滤就可以分离,不会产生对环境造成污染的有机废液,相对于经典方法,本发明的生产工艺更为绿色清洁。2. The yellow monovalent copper salt polymer as a by-product can be directly precipitated from the solution, so that the hydrogen peroxide solution and the by-product can be separated by simple filtration, and no organic waste that pollutes the environment will be produced. Compared with Classical method, the production process of the present invention is more green and clean.
3、本发明中的水溶液PH值反应后降低,可以直接作为过氧化氢的酸性稳定剂,无需另加,节约了成本。3. The pH value of the aqueous solution in the present invention decreases after the reaction, and can be directly used as an acid stabilizer for hydrogen peroxide without additional addition, which saves costs.
4、由于一价铜离子很容易被空气中的氧气氧化,所以副产物可以在被氧化后再次套用。4. Since monovalent copper ions are easily oxidized by oxygen in the air, the by-products can be applied again after being oxidized.
附图说明 Description of drawings
图1是本发明的催化剂的单晶结构图。Figure 1 is a single crystal structure diagram of the catalyst of the present invention.
图2是本发明实施例3的催化剂与Cu(NO3)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,表明得到的溶液中双氧水部分产生了羟基自由基。Fig. 2 is the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalytic oxidation of water with the catalyst of Example 3 of the present invention and Cu(NO 3 ) 2 , indicating that hydroxyl radicals are generated in the hydrogen peroxide part of the obtained solution.
图3是本发明实施例4的催化剂与Cu(ClO4)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,表明得到的溶液中双氧水部分产生了羟基自由。Fig. 3 is the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalytic oxidation of water with the catalyst of Example 4 of the present invention and Cu(ClO 4 ) 2 , indicating that the hydrogen peroxide in the obtained solution partially generates free hydroxyl groups.
图4是本发明实施例5的催化剂与Cu(SO3CF3)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,表明得到的溶液中双氧水部分产生了羟基自由。Fig. 4 is the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalytic oxidation of water with the catalyst of Example 5 of the present invention and Cu(SO 3 CF 3 ) 2 , indicating that the hydrogen peroxide in the obtained solution partially generates free hydroxyl groups.
图5是氧化水产生双氧水用比色管测得的颜色变化的照片,表明产生的溶液中含有双氧水。Figure 5 is a photograph of the color change measured with a colorimetric tube for oxidizing water to produce hydrogen peroxide, indicating that the resulting solution contains hydrogen peroxide.
具体实施方式 Detailed ways
下面通过实施例对本发明进行具体描述,有必要在此指出的是:本实施例只用于对本发明进行进一步说明,但不局限其范围。本领域专业人员在阅读本发明之后在不违背本发明实质所作出的各种改进都是显而易见的,都属于本发明要求保护范围。The present invention is specifically described below through the examples, and it is necessary to point out that: the present examples are only used to further illustrate the present invention, but do not limit its scope. Various improvements made by those skilled in the art without departing from the essence of the present invention after reading the present invention are all obvious, and all belong to the protection scope of the present invention.
实施例1:催化剂的制备Embodiment 1: the preparation of catalyst
1.5,5’-二溴-2,2’-联苯二酚(3.44g,10mmol),3-氯甲基吡啶盐酸盐(3.80g,25mmol),K2CO3(27.6g,200mmol),KI(0.60g,3.6mmol),DMF 25mL,常温搅拌36h,将反应物倒入水中,抽滤,滤饼硅胶柱层析(CH2Cl2∶CH3OH=25∶1),得白色固体中间体B 4.27g,产率812%。1.5,5'-dibromo-2,2'-diphenol (3.44g, 10mmol), 3-chloromethylpyridine hydrochloride (3.80g, 25mmol), K 2 CO 3 (27.6g, 200mmol) , KI (0.60g, 3.6mmol), DMF 25mL, stirred at room temperature for 36h, poured the reactant into water, filtered with suction, and filtered the cake through silica gel column chromatography (CH 2 Cl 2 :CH 3 OH=25:1) to obtain a white Solid intermediate B 4.27g, yield 812%.
2.N2保护下,中间体B(5.26g,10mmol),吡啶-4-硼酸(3.08g,25mmol),K2CO3(17.25g,125mmol),置于250mL三口烧瓶中,甲苯,乙醇和水作溶剂,加入催化剂Pd(PPh3)4(1.2g,1mmol),加热回流,控制温度在90℃-110℃,控制回流时间在24h。TLC跟踪,反应结束后静置,冷却,分液,有机相旋干,硅胶柱层析(CH2Cl2∶CH3OH=20∶1),得淡黄色固体4.16g,产率79.6%。将实施例1所制得的产品在乙醇和水的混合溶液中得到化合物的无色片状晶体,经x-射线单晶衍射确定化合物的结构(如图1所示),由图可知,所制得化合物即为目标化合物。2. Under N 2 protection, intermediate B (5.26g, 10mmol), pyridine-4-boronic acid (3.08g, 25mmol), K 2 CO 3 (17.25g, 125mmol), placed in a 250mL three-necked flask, toluene, ethanol Use water as a solvent, add catalyst Pd(PPh 3 ) 4 (1.2g, 1mmol), heat to reflux, control the temperature at 90°C-110°C, and control the reflux time at 24h. TLC tracking, after the reaction was completed, let stand, cooled, separated, the organic phase was spin-dried, and silica gel column chromatography (CH 2 Cl 2 : CH 3 OH=20:1) gave 4.16 g of a light yellow solid, with a yield of 79.6%. The product obtained in embodiment 1 is obtained the colorless flaky crystal of compound in the mixed solution of ethanol and water, determines the structure of compound (as shown in Figure 1) through x-ray single crystal diffraction, as can be seen from the figure, the The obtained compound is the target compound.
实施例2:催化剂的制备Embodiment 2: the preparation of catalyst
1.5,5’-二溴-2,2’-联苯二酚(3.44g,10mmol),3-氯甲基吡啶盐酸盐(3.04g,20mmol),K2CO3(20.7g,150mmol),KI(0.80g,4.8mmol),DMF 25mL,常温搅拌24h,将反应物倒入水中,抽滤,滤饼硅胶柱层析(CH2Cl2∶CH3OH=25∶1),得白色固体中间体B4.12g,产率78.3%。1.5,5'-dibromo-2,2'-diphenol (3.44g, 10mmol), 3-chloromethylpyridine hydrochloride (3.04g, 20mmol), K 2 CO 3 (20.7g, 150mmol) , KI (0.80g, 4.8mmol), DMF 25mL, stirred at room temperature for 24h, poured the reactant into water, filtered with suction, and filtered the cake through silica gel column chromatography (CH 2 Cl 2 :CH 3 OH=25:1) to obtain a white Solid intermediate B4.12g, yield 78.3%.
2.N2保护下,中间体B(5.26g,10mmol),吡啶-4-硼酸(2.46g,20mmol),K2CO3(20.7g,150mmol),置于250mL三口烧瓶中,甲苯,乙醇和水作溶剂,加入催化剂Pd(PPh3)4(1.2g,1mmol),加热回流,控制温度在90℃-110℃,控制回流时间在36h。TLC跟踪,反应结束后静置,冷却,分液,有机相旋干,硅胶柱层析(CH2Cl2∶CH3OH=20∶1),得淡黄色固体4.02g,产率76.9%。2. Under N 2 protection, intermediate B (5.26g, 10mmol), pyridine-4-boronic acid (2.46g, 20mmol), K 2 CO 3 (20.7g, 150mmol), placed in a 250mL three-necked flask, toluene, ethanol Use water as a solvent, add catalyst Pd(PPh 3 ) 4 (1.2g, 1mmol), heat to reflux, control the temperature at 90°C-110°C, and control the reflux time at 36h. TLC tracking, standing still after the reaction, cooling, liquid separation, spin-dried organic phase, silica gel column chromatography (CH 2 Cl 2 : CH 3 OH=20:1), yielded 4.02 g of light yellow solid with a yield of 76.9%.
实施例3:Cu(NO3)2水热下氧化水产生双氧水Embodiment 3: Cu(NO 3 ) Hydrogen peroxide is produced by oxidizing water under hydrothermal conditions
将由于实施例1制备的催化剂配体L 5.22mg(0.01mmol),Cu(NO3)2·6H2O 12.0mg(0.04mmol),水2mL,密封在10cm的玻璃管中,程序设定经过300min升温至150℃,恒温4320min,然后经过3000min降至30℃,得到黄色一价铜盐的聚合物及含双氧水的溶液。5.22 mg (0.01 mmol) of the catalyst ligand L prepared in Example 1, 12.0 mg (0.04 mmol) of Cu(NO 3 ) 2 6H 2 O, and 2 mL of water were sealed in a 10 cm glass tube, and the program was set through The temperature was raised to 150°C in 300 minutes, kept at a constant temperature for 4320 minutes, and then lowered to 30°C after 3000 minutes to obtain a yellow monovalent copper salt polymer and a solution containing hydrogen peroxide.
图3为催化剂与Cu(NO3)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,由此得出水被氧化为双氧水且部分产生羟基自由基。Figure 3 shows the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalyst and Cu(NO 3 ) 2 catalyzed oxidation of water, from which it can be concluded that the water is oxidized to hydrogen peroxide and partially generates hydroxyl radicals.
实施例4:Cu(Cl04)2水热下氧化水产生双氧水Embodiment 4: Cu(Cl0 4 ) Hydrogen peroxide is produced by oxidizing water under hydrothermal conditions
将由于实施例1制备的催化剂配体L 5.22mg(0.01mmol),Cu(ClO4)2·6H2O 12.4mg(0.03mmol),水2mL,密封在10cm的玻璃管中,程序设定经过300min升温至150℃,恒温4320min,然后经过3000min降至30℃,得到黄色一价铜盐的聚合物及含双氧水的溶液。5.22 mg (0.01 mmol) of catalyst ligand L prepared in Example 1, 12.4 mg (0.03 mmol) of Cu(ClO 4 ) 2 6H 2 O, and 2 mL of water were sealed in a 10 cm glass tube, and the program was set through The temperature was raised to 150°C in 300 minutes, kept at a constant temperature for 4320 minutes, and then lowered to 30°C after 3000 minutes to obtain a yellow monovalent copper salt polymer and a solution containing hydrogen peroxide.
图4为催化剂与Cu(NO3)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,由此得出水被氧化为双氧水且部分产生羟基自由基。Figure 4 shows the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalyst and Cu(NO 3 ) 2 catalyzed oxidation of water, from which it can be concluded that the water is oxidized to hydrogen peroxide and partially generates hydroxyl radicals.
实施例5:Cu(SO3CF3)2水热下氧化水产生双氧水Example 5: Cu(SO 3 CF 3 ) 2 hydrothermally oxidizes water to produce hydrogen peroxide
将由于实施例2制备的催化剂配体L 5.22mg(0.01mmol),Cu(SO3CF3)2 15.1mg(0.04mmol),水2mL,密封在10cm的玻璃管中,程序设定经过300min升温至150℃,恒温4320min,然后经过3000min降至30℃,得到黄色一价铜盐的聚合物及含双氧水的溶液。Put 5.22mg (0.01mmol) of the catalyst ligand L prepared in Example 2, 15.1mg (0.04mmol) of Cu(SO 3 CF 3 ) 2 , and 2mL of water into a 10cm glass tube, and set the temperature to rise after 300min To 150°C, keep the temperature constant for 4320min, then drop to 30°C after 3000min, to obtain a yellow monovalent copper salt polymer and a solution containing hydrogen peroxide.
图5为催化剂与Cu(NO3)2催化氧化水得到的溶液加入羟基自由基捕捉剂DMPO测得的EPR信号,由此得出水被氧化为双氧水且部分产生羟基自由基。Figure 5 shows the EPR signal measured by adding the hydroxyl radical scavenger DMPO to the solution obtained by catalyst and Cu(NO 3 ) 2 to catalyze the oxidation of water, so it can be concluded that the water is oxidized to hydrogen peroxide and partially generates hydroxyl radicals.
实施例6:氧化水产生双氧水用比色管测得的颜色变化Embodiment 6: oxidized water produces the color change that hydrogen peroxide measures with colorimetric tube
将双氧水比色管中的白色试剂迅速加入到经催化剂(由实施例3制备)和铜盐催化氧化水得到的无色溶液中,如图5所示,左边小瓶是本发明的氧化水得到的溶液加入H2O2比色管试剂后的颜色变化,右边的小瓶为30%H2O2加入H2O2比色管试剂后的颜色变化。经30秒后与过氧化氢浓度比色卡比较可得,所得到的双氧水浓度约为1mg/L,在150℃的反应条件下,双氧水有相当的部分产生了氧气。The white reagent in the hydrogen peroxide colorimetric tube is quickly added to the colorless solution obtained by catalyst (prepared by Example 3) and copper salt catalyzed oxidation water, as shown in Figure 5, the left vial is obtained by the oxidation water of the present invention The color change of the solution after adding the H 2 O 2 colorimetric tube reagent, the vial on the right is the color change after adding 30% H 2 O 2 to the H 2 O 2 colorimetric tube reagent. After 30 seconds, it can be compared with the hydrogen peroxide concentration color chart, and the obtained hydrogen peroxide concentration is about 1mg/L. Under the reaction conditions of 150°C, a considerable part of the hydrogen peroxide produces oxygen.
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