CN112076788A - Method for oxidizing cycloalkane under concerted catalysis of metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt - Google Patents
Method for oxidizing cycloalkane under concerted catalysis of metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt Download PDFInfo
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- 239000013097 PCN-222 Substances 0.000 title claims abstract description 82
- 239000012621 metal-organic framework Substances 0.000 title claims abstract description 77
- 150000001924 cycloalkanes Chemical class 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 30
- 150000003839 salts Chemical class 0.000 title claims abstract description 26
- 230000001590 oxidative effect Effects 0.000 title claims abstract description 13
- 230000002153 concerted effect Effects 0.000 title claims description 11
- 238000006555 catalytic reaction Methods 0.000 title abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 223
- 238000003756 stirring Methods 0.000 claims abstract description 109
- 230000003647 oxidation Effects 0.000 claims abstract description 30
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 30
- 230000003197 catalytic effect Effects 0.000 claims abstract description 22
- -1 cycloalkyl alcohol Chemical compound 0.000 claims abstract description 19
- 239000000047 product Substances 0.000 claims abstract description 11
- 239000007800 oxidant agent Substances 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 238000007789 sealing Methods 0.000 claims abstract 2
- RIOQSEWOXXDEQQ-UHFFFAOYSA-N triphenylphosphine Chemical compound C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 RIOQSEWOXXDEQQ-UHFFFAOYSA-N 0.000 claims description 125
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 103
- 239000001301 oxygen Substances 0.000 claims description 103
- 229910052760 oxygen Inorganic materials 0.000 claims description 103
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 92
- 150000002978 peroxides Chemical class 0.000 claims description 55
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 9
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 7
- 239000012043 crude product Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- DDTBPAQBQHZRDW-UHFFFAOYSA-N cyclododecane Chemical compound C1CCCCCCCCCCC1 DDTBPAQBQHZRDW-UHFFFAOYSA-N 0.000 claims description 4
- WJTCGQSWYFHTAC-UHFFFAOYSA-N cyclooctane Chemical compound C1CCCCCCC1 WJTCGQSWYFHTAC-UHFFFAOYSA-N 0.000 claims description 4
- 239000004914 cyclooctane Substances 0.000 claims description 4
- 150000004677 hydrates Chemical class 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 229910021592 Copper(II) chloride Inorganic materials 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims description 2
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 2
- 229910000366 copper(II) sulfate Inorganic materials 0.000 claims description 2
- LMGZGXSXHCMSAA-UHFFFAOYSA-N cyclodecane Chemical compound C1CCCCCCCCC1 LMGZGXSXHCMSAA-UHFFFAOYSA-N 0.000 claims description 2
- GPTJTTCOVDDHER-UHFFFAOYSA-N cyclononane Chemical compound C1CCCCCCCC1 GPTJTTCOVDDHER-UHFFFAOYSA-N 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 11
- 150000002576 ketones Chemical class 0.000 abstract description 10
- 239000004215 Carbon black (E152) Substances 0.000 abstract description 9
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 9
- 229930195733 hydrocarbon Natural products 0.000 abstract description 9
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 8
- 230000002194 synthesizing effect Effects 0.000 abstract description 7
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- 230000002195 synergetic effect Effects 0.000 abstract 1
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- 239000011541 reaction mixture Substances 0.000 description 145
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 114
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 108
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 90
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 86
- 239000005711 Benzoic acid Substances 0.000 description 54
- 235000010233 benzoic acid Nutrition 0.000 description 54
- 238000004811 liquid chromatography Methods 0.000 description 51
- 239000002904 solvent Substances 0.000 description 51
- 229910001220 stainless steel Inorganic materials 0.000 description 50
- 239000010935 stainless steel Substances 0.000 description 50
- 238000004817 gas chromatography Methods 0.000 description 49
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- 239000004809 Teflon Substances 0.000 description 48
- 229920006362 Teflon® Polymers 0.000 description 48
- 238000004458 analytical method Methods 0.000 description 48
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 45
- FGGJBCRKSVGDPO-UHFFFAOYSA-N hydroperoxycyclohexane Chemical compound OOC1CCCCC1 FGGJBCRKSVGDPO-UHFFFAOYSA-N 0.000 description 45
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 description 43
- 239000001361 adipic acid Substances 0.000 description 43
- 235000011037 adipic acid Nutrition 0.000 description 43
- JFCQEDHGNNZCLN-UHFFFAOYSA-N anhydrous glutaric acid Natural products OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 description 43
- 230000015572 biosynthetic process Effects 0.000 description 20
- 101100030361 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) pph-3 gene Proteins 0.000 description 9
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- 238000003786 synthesis reaction Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 150000003254 radicals Chemical class 0.000 description 5
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- 239000013067 intermediate product Substances 0.000 description 4
- WLJVNTCWHIRURA-UHFFFAOYSA-N pimelic acid Chemical compound OC(=O)CCCCCC(O)=O WLJVNTCWHIRURA-UHFFFAOYSA-N 0.000 description 4
- 125000001931 aliphatic group Chemical group 0.000 description 3
- 230000003321 amplification Effects 0.000 description 3
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
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- 238000005485 electric heating Methods 0.000 description 3
- 238000003199 nucleic acid amplification method Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
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- SXVPOSFURRDKBO-UHFFFAOYSA-N Cyclododecanone Chemical compound O=C1CCCCCCCCCCC1 SXVPOSFURRDKBO-UHFFFAOYSA-N 0.000 description 2
- 229910007926 ZrCl Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 2
- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 description 2
- 239000012847 fine chemical Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- TYFQFVWCELRYAO-UHFFFAOYSA-N suberic acid Chemical compound OC(=O)CCCCCCC(O)=O TYFQFVWCELRYAO-UHFFFAOYSA-N 0.000 description 2
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 229910007932 ZrCl4 Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- SFVWPXMPRCIVOK-UHFFFAOYSA-N cyclododecanol Chemical compound OC1CCCCCCCCCCC1 SFVWPXMPRCIVOK-UHFFFAOYSA-N 0.000 description 1
- QCRFMSUKWRQZEM-UHFFFAOYSA-N cycloheptanol Chemical compound OC1CCCCCC1 QCRFMSUKWRQZEM-UHFFFAOYSA-N 0.000 description 1
- CGZZMOTZOONQIA-UHFFFAOYSA-N cycloheptanone Chemical compound O=C1CCCCCC1 CGZZMOTZOONQIA-UHFFFAOYSA-N 0.000 description 1
- FHADSMKORVFYOS-UHFFFAOYSA-N cyclooctanol Chemical compound OC1CCCCCCC1 FHADSMKORVFYOS-UHFFFAOYSA-N 0.000 description 1
- IIRFCWANHMSDCG-UHFFFAOYSA-N cyclooctanone Chemical compound O=C1CCCCCCC1 IIRFCWANHMSDCG-UHFFFAOYSA-N 0.000 description 1
- XCIXKGXIYUWCLL-UHFFFAOYSA-N cyclopentanol Chemical compound OC1CCCC1 XCIXKGXIYUWCLL-UHFFFAOYSA-N 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- GPHZOCJETVZYTP-UHFFFAOYSA-N hydroperoxycyclododecane Chemical compound OOC1CCCCCCCCCCC1 GPHZOCJETVZYTP-UHFFFAOYSA-N 0.000 description 1
- GRLDKEKHXHSXQW-UHFFFAOYSA-N hydroperoxycycloheptane Chemical compound OOC1CCCCCC1 GRLDKEKHXHSXQW-UHFFFAOYSA-N 0.000 description 1
- DTMZBUVZQPKYDT-UHFFFAOYSA-N hydroperoxycyclooctane Chemical compound OOC1CCCCCCC1 DTMZBUVZQPKYDT-UHFFFAOYSA-N 0.000 description 1
- VGGFAUSJLGBJRZ-UHFFFAOYSA-N hydroperoxycyclopentane Chemical compound OOC1CCCC1 VGGFAUSJLGBJRZ-UHFFFAOYSA-N 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000001384 succinic acid Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1691—Coordination polymers, e.g. metal-organic frameworks [MOF]
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/04—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing carboxylic acids or their salts
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/48—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by oxidation reactions with formation of hydroxy groups
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
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- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/70—Oxidation reactions, e.g. epoxidation, (di)hydroxylation, dehydrogenation and analogues
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0238—Complexes comprising multidentate ligands, i.e. more than 2 ionic or coordinative bonds from the central metal to the ligand, the latter having at least two donor atoms, e.g. N, O, S, P
- B01J2531/0241—Rigid ligands, e.g. extended sp2-carbon frameworks or geminal di- or trisubstitution
- B01J2531/025—Ligands with a porphyrin ring system or analogues thereof, e.g. phthalocyanines, corroles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/84—Metals of the iron group
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Abstract
A method for oxidizing cycloalkane under synergetic catalysis of metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt comprises the steps of dispersing 1% -10% of PCN-222(Co) and 0.01% -10% of Cu (II) salt (mol/mol) in cycloalkane, sealing a reaction system, heating to 90-150 ℃ under stirring, introducing an oxidant (0.10-2.0 MPa), keeping the set temperature and pressure, stirring for reaction for 2.0-24.0 hours, and carrying out aftertreatment on reaction liquid to obtain a product, namely cycloalkyl alcohol and cycloalkyl ketone. The method has the advantages of high selectivity of the naphthenic alcohol and the naphthenic ketone, low reaction temperature, few byproducts, small environmental influence and the like. In addition, the content of naphthenic hydroperoxide is low, and the safety coefficient is high. The invention provides a high-efficiency, feasible and safe method for synthesizing naphthenic alcohol and naphthenic ketone by selective catalytic oxidation of naphthenic hydrocarbon.
Description
Technical Field
The invention relates to a method for synthesizing cycloalkanol and cycloalkanone by synergistically catalyzing and oxidizing cycloalkane with metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt, belonging to the field of industrial catalysis and fine organic synthesis.
Background
Catalytic oxidation of cycloalkane is an important conversion process in chemical industry, and oxidation products of cycloalkanol and cycloalkanone are not only important organic solvents, but also important fine chemical intermediates, and are widely applied to synthesis of fine chemical products such as pesticides, medicines, dyes, surfactants, resins and the like, especially production of polyamide fiber nylon-6 and nylon-66. At present, the catalytic oxidation of cycloalkanes is industrially carried out mainly by homogeneous Co2+Or Mn2+As catalyst, oxygen (O)2) As an oxidizing agent, at 150 ℃ to 170 ℃, there are major problems of high reaction temperature, low substrate conversion, poor selectivity of the target product, and in particular, difficulty in inhibiting the formation of aliphatic diacids (Applied Catalysis a, General 2019,575: 120-; catalysis Communications 2019,132: 105809). The main sources of the above problems are: (1) at present, O is industrially used2Oxidized cycloalkanes undergo mainly a disordered radical diffusion history; (2) the intermediate product of oxidation, the naphthenic base hydrogen peroxide, is converted to the target oxidation product of naphthenic alcohol and cycloalkanone by a free radical thermal decomposition path, thereby increasing the uncontrollable property of a reaction system and reducing the selectivity of the naphthenic alcohol and the naphthenic ketone. Thus, O is effectively controlled2The free radical diffusion in the process of catalytically oxidizing the cycloalkane and the catalytic conversion of the intermediate product of the oxidation, namely the cycloalkyl hydrogen peroxide, are beneficial to the improvement of the catalytic oxidation selectivity of the cycloalkane, and are novel process improvements in the field of industrial cycloalkane catalytic oxidation and have great application significance.
The metal-organic framework material PCN-222 is a series of porous materials with better chemical stability and thermal stability, is applied to the field of organic catalysis, can realize the high-efficiency dispersion of catalytic active centers, can provide a certain micro-domain environment for chemical reaction, effectively limits the disordered diffusion of free radicals, and improves the reaction selectivity (Angewandte Chemistry International Edition 2012,51, 10307-. In addition, Cu (II) can catalyze the decomposition and conversion of naphthenic base hydrogen peroxide which is an intermediate product of naphthenic hydrocarbon oxidation, limit the non-selective thermal decomposition and conversion of the naphthenic hydrocarbon, and improve the selectivity of catalytic oxidation of the naphthenic hydrocarbon (Catalysis Communications 2019,132: 105809).
Disclosure of Invention
In order to overcome the defects of the prior art, the invention aims to provide a method for synthesizing cycloalkyl alcohol and cycloalkyl ketone by synergistically catalyzing and oxidizing cycloalkane with metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt2The method for selectively synthesizing the naphthenic alcohol and the naphthenic ketone by oxidizing the naphthenic hydrocarbon has the advantages of high selectivity of the naphthenic alcohol and the naphthenic ketone, low reaction temperature, less by-products, small environmental influence and the like, and the method provided by the invention has low content of naphthenic hydroperoxide and high safety coefficient, and is an efficient, feasible and safe method for selectively catalytically oxidizing the naphthenic hydrocarbon to synthesize the naphthenic alcohol and the naphthenic ketone.
The technical scheme of the invention is as follows:
a method for the concerted catalytic oxidation of cycloalkanes by a metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt, said method comprising the following steps:
dispersing metalloporphyrin MOFs PCN-222(Co) and Cu (II) salt into cycloalkane, wherein the mass of the metalloporphyrin MOFs PCN-222(Co) is 1% -10% of the content of the cycloalkane material, and g/mol; the amount of Cu (II) salt is 0.01-10% of that of naphthenic hydrocarbon, mol/mol of the salt is sealed in a reaction system, the temperature is raised to 90-150 ℃ under stirring, an oxidant (0.10-2.0 MPa) is introduced, the set temperature and pressure are kept, the stirring reaction is carried out for 2.0-24.0 h, and then the reaction solution is subjected to post-treatment to obtain the product of naphthenic alcohol and naphthenic ketone;
the metalloporphyrin MOFs PCN-222(Co) contains at least one metalloporphyrin unit of compounds shown in a formula (I), a formula (II) and a formula (III):
the Cu (II) salt is Cu (CH)3COO)2,Cu(NO2)2,CuSO4,CuCl2And hydrates thereof, or a mixture of at least two of the hydrates in any proportion;
the cycloalkane is one of cyclopentane, cyclohexane, cycloheptane, cyclooctane, cyclononane, cyclodecane and cyclododecane or a mixture of at least two of the above materials in any proportion.
Further, the ratio of the mass of the metalloporphyrin MOFs PCN-222(Co) to the mass of the naphthenic hydrocarbon substances is 1: 100-1: 10, preferably 1: 25-2: 25.
The mass ratio of the Cu (II) salt to the cycloalkane is 1: 10000-1: 10, preferably 1: 1000-1: 100.
The reaction temperature is 90-150 ℃, and preferably 100-130 ℃; the reaction pressure is 0.10-2.0 MPa, preferably 0.60-1.20 MPa; the stirring speed is 600-1200 rpm, preferably 800-1000 rpm.
The oxidant is oxygen, air or a mixture of oxygen and air in any proportion;
the post-treatment method comprises the following steps: after the reaction is finished, adding triphenylphosphine PPh into the reaction solution3And the using amount of the peroxide is 3 percent of the amount of the cyclane, the peroxide generated by reduction is stirred for 40min at room temperature (20-30 ℃), and the crude product is distilled, rectified under reduced pressure and recrystallized to obtain an oxidation product.
The method for analyzing the reaction result comprises the following steps: after the reaction is finished, peroxide generated by the reduction of the reaction liquid by triphenylphosphine is sampled and analyzed. Diluting with acetone as solvent, performing gas chromatography with toluene as internal standard, and calculating conversion rate of cycloalkane and selectivity of cycloalkyl alcohol, cycloalkyl ketone and peroxide; performing liquid chromatography analysis by taking benzoic acid as an internal standard, and calculating the selectivity of the aliphatic diacid;
in the invention, the metalloporphyrin unit contained in the metalloporphyrin MOFs PCN-222(Co) is at least one of compounds shown in a formula (I), a formula (II) and a formula (III):
the invention constructs a binary catalytic system by using metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt to synergistically catalyze O2The oxidation of the cycloalkane to synthesize the cycloalkyl alcohol and the cycloalkyl ketone not only effectively inhibits the disordered diffusion of free radicals in the oxidation process, but also realizes the catalytic conversion of the oxidation intermediate product, namely the cycloalkyl hydrogen peroxide, greatly improves the selectivity of the target product, namely the cycloalkyl alcohol and the cycloalkyl ketone, reduces the generation of byproducts, reduces the emission of environmental pollutants, and meets the practical requirements of the chemical industry on energy conservation and emission reduction at present. The invention not only provides a method for synthesizing naphthenic alcohol and naphthenic ketone by high-efficiency and selective oxidation of naphthenic C-H bonds, but also has certain reference value for preparing alcohols and ketone compounds by selective catalytic oxidation of other hydrocarbon C-H bonds.
The invention has the following beneficial effects: the method for synthesizing the naphthenic alcohol and the naphthenic ketone by the concerted catalytic oxidation of the cycloparaffin by the metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt has the advantages of high selectivity of the naphthenic alcohol and the naphthenic ketone, low reaction temperature, less byproducts, small environmental influence and the like. In addition, the content of the naphthenic base hydroperoxide is low, and the safety coefficient is high. The invention provides a high-efficiency, feasible and safe method for synthesizing cycloalkyl alcohol and cycloalkyl ketone by selective catalytic oxidation of cycloalkane.
Detailed Description
The invention will be further illustrated with reference to specific examples, without however being limited thereto.
The metalloporphyrins MOFs PCN-222(Co) used in the invention refer to Angewandte Chemie International Edition 2012,51, 10307-10310; inorganic Chemistry 2018,57,6, 3339-3347; inorganic Chemistry 2019,58: 5145-. All reagents used were commercially available analytical grade.
Examples 1 to 3 are syntheses of the metalloporphyrins MOFs PCN-222 (Co).
Examples 4 to 46 are examples of catalytic oxidation of cycloalkanes.
Examples 47 to 50 are comparative experimental cases.
Examples 51 to 53 are scale-up experimental cases.
Example 1
Synthesis of PCN-222(Co) -m: t (3-COOH) PPCo (II) (0.0847g, 0.1mmol), ZrCl were placed in a 35mL pressure-resistant reaction tube4(0.1400g,0.6mmol), benzoic acid (5.4000g,44.3mmol) was dissolved in 16.0mL DMF and sonicated for 30min until all dissolved. The mixture is put into an electric heating constant temperature air blast drying oven to be kept still for reaction for 48.0h at the temperature of 120 ℃. After the reaction is finished, the heating is closed, the reaction product is naturally cooled to room temperature, the crude product is filtered, rinsed with DMF and acetone sequentially and transferred to a 10.0mL centrifuge tube, a low-speed centrifuge is used for centrifuging for 5min (3000rpm), the upper layer liquid is poured out, dry DMF is statically extracted (3 × 8.0mL) until the upper layer liquid is clear, dry acetone is extracted (3 × 8.0mL) until the upper layer liquid is clear, the lower layer solid is taken off, and the drying is carried out for 8.0h at 90 ℃ to obtain brick red powder (0.0680g, 44.7% yield).
Example 2
Synthesis of PCN-222(Co) -p: t (4-COOH) PPCo (II) (0.0847g, 0.1mmol), ZrCl were placed in a 35mL pressure-resistant reaction tube4(0.1400g,0.6mmol), benzoic acid (5.4000g,44.3mmol) was dissolved in 16.0mL DMF and sonicated for 30min until all dissolved. The mixture is put into an electric heating constant temperature air blast drying oven to be kept still for reaction for 48.0h at the temperature of 120 ℃. After the reaction is finished, the heating is closed, the reaction product is naturally cooled to room temperature, the crude product is filtered, rinsed with DMF and acetone sequentially and then transferred to a 10.0mL centrifuge tube, a low-speed centrifuge is used for centrifuging for 5min (3000rpm), the upper layer liquid is poured out, and DMF is dried and is statically extracted (3 × 8.0mL) to the upper layerThe supernatant was clarified, dry acetone leached (3X 8.0mL) to a clear supernatant, the solid from the lower layer was dried at 90 ℃ for 8.0h to give a brick-red powder (0.0690g, 45.3% yield).
Example 3
Synthesis of PCN-222(Co) -d: in a 35mL pressure-resistant reaction tube, [ T (4- (4-COOH) P) PPCo (II) ]] (0.1152g,0.1mmol),ZrCl4(0.1400g,0.6mmol), benzoic acid (5.4000g,44.3mmol) was dissolved in 16.0mL DMF and sonicated for 30min until all dissolved. The mixture is put into an electric heating constant temperature air blast drying oven to be stood still for reaction for 48.0h at the temperature of 120 ℃. After the reaction is finished, the heating is closed, the reaction product is naturally cooled to room temperature, the crude product is filtered, rinsed with DMF and acetone sequentially and transferred to a 10.0mL centrifuge tube, a low-speed centrifuge is used for centrifuging for 5min (3000rpm), the upper layer liquid is poured out, dry DMF is statically extracted (3 × 8.0mL) until the upper layer liquid is clear, dry acetone is extracted (3 × 8.0mL) until the upper layer liquid is clear, the lower layer solid is taken off, and the dry DMF is dried for 8.0h at 90 ℃ to obtain brick red powder (0.0660g, 43.4% yield).
Example 4
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (2 mg,0.01mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 4.96%, cyclohexanol selectivity 50.4%, cyclohexanone selectivity 36.1%, cyclohexyl hydroperoxide selectivity 9.8%, adipic acid selectivity 3.7%, and no formation of glutaric acid was detected.
Example 5
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (8 mg,0.04mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion was 5.24%, the cyclohexanol selectivity was 49.2%, the cyclohexanone selectivity was 37.7%, the cyclohexyl hydroperoxide selectivity was 10.1%, the adipic acid selectivity was 3.0%, and the formation of glutaric acid was not detected.
Example 6
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 6.79%, the cyclohexanol selectivity is 48.5%, the cyclohexanone selectivity is 37.8%, the cyclohexyl hydroperoxide selectivity is 5.5%, the adipic acid selectivity is 7.2%, and the glutaric acid selectivity is 1%.
Example 7
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (16mg,0.08mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. At 120 deg.CStirring and reacting at 800rpm for 8.0h under the oxygen pressure of 1.0 MPa. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 5.71%, cyclohexanol selectivity 46.7%, cyclohexanone selectivity 36.4%, cyclohexyl hydroperoxide selectivity 10.5%, adipic acid selectivity 6.4%, and no formation of glutaric acid was detected.
Example 8
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (20mg,0.10mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion was 5.68%, the cyclohexanol selectivity was 50.7%, the cyclohexanone selectivity was 36.2%, the cyclohexyl hydroperoxide selectivity was 8.5%, the adipic acid selectivity was 4.6%, and the formation of glutaric acid was not detected.
Example 9
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(3.6mg,0.018mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ while stirring, and oxygen was introduced thereinto to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 4.65%, cyclohexanol selectivity 51.4%, cyclohexanone selectivity 33.6%, cyclohexyl hydroperoxide selectivity 8.4%, adipic acid selectivity 6.6%, and no formation of glutaric acid was detected.
Example 10
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(50mg,0.250mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 4.86%, cyclohexanol selectivity 48.2%, cyclohexanone selectivity 37.4%, cyclohexyl hydroperoxide selectivity 7.7%, adipic acid selectivity 6.7%, and no formation of glutaric acid was detected.
Example 11
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(100mg,0.500mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. Remove 10mLCarrying out gas phase chromatographic analysis on the obtained solution by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 5.51%, cyclohexanol selectivity 49.6%, cyclohexanone selectivity 38.3%, cyclohexyl hydroperoxide selectivity 5.8%, adipic acid selectivity 6.3%, and no formation of glutaric acid was detected.
Example 12
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(200mg,1.000mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 5.85 percent, the cyclohexanol selectivity is 48.8 percent, the cyclohexanone selectivity is 37.8 percent, the cyclohexyl hydroperoxide selectivity is 6.8 percent, the adipic acid selectivity is 6.6 percent, and the glutaric acid is not generated.
Example 13
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(300mg,1.500mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Conversion of cyclohexane6.23 percent, 49.6 percent of cyclohexanol selectivity, 36.3 percent of cyclohexanone selectivity, 7.8 percent of cyclohexyl hydroperoxide selectivity and 6.3 percent of adipic acid selectivity, and the generation of glutaric acid is not detected.
Example 14
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(600mg,2.000mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is removed, toluene is taken as an internal standard, and gas chromatography analysis is carried out; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 6.43%, cyclohexanol selectivity 49.9%, cyclohexanone selectivity 37.1%, cyclohexyl hydroperoxide selectivity 6.8%, adipic acid selectivity 6.2%, glutaric acid selectivity.
Example 15
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(800mg,4.000mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 6.21%, cyclohexanol selectivity 48.2%, cyclohexanone selectivity 39.1%, cyclohexyl hydroperoxide selectivity 6.3%, adipic acid selectivity 6.4%, no glutaric acid formation detectedAnd (4) obtaining.
Example 16
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(3669mg,18.345mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion was 6.12%, cyclohexanol selectivity was 47.6%, cyclohexanone selectivity was 40.4%, cyclohexyl hydroperoxide selectivity was 5.4%, adipic acid selectivity was 6.6%, and glutaric acid formation was not detected.
Example 17
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 90 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 90 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 2.52%, cyclohexanol selectivity 25.6%, cyclohexanone selectivity 26.2%, cyclohexyl hydroperoxide selectivity 48.2%, no diacid formation was detected.
Example 18
In a 100mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -m (14mg, 0).07mg/mmol),Cu(OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 100 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 100 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, ice water was cooled to room temperature, and 1.3115g (5.00mmol) of triphenylphosphine (PPh3) was added to the reaction mixture, and the reaction mixture was stirred at room temperature for 30min to reduce the formed peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 3.58%, cyclohexanol selectivity 47.2%, cyclohexanone selectivity 34.5%, cyclohexyl hydroperoxide selectivity 18.3%, no diacid formation was detected.
Example 19
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 125 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 125 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 7.58%, cyclohexanol selectivity 39.4%, cyclohexanone selectivity 46.7%, cyclohexyl hydroperoxide selectivity 6.9%, adipic acid selectivity 6.0%, glutaric acid selectivity 1.0%.
Example 20
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. At 130 ℃ and 1.0MPa oxygen pressure,the reaction was stirred at 800rpm for 8.0 h. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.58%, cyclohexanol selectivity 36.8%, cyclohexanone selectivity 53.4%, cyclohexyl hydroperoxide selectivity 1.0%, adipic acid selectivity 7.4%, glutaric acid selectivity 1.4%.
Example 21
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 135 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 135 ℃ under 1.0MPa of oxygen pressure at 800rpm for 8.0 h. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 10.72%, the cyclohexanol selectivity is 29.2%, the cyclohexanone selectivity is 56.8%, the cyclohexyl hydroperoxide selectivity is 1.0%, the adipic acid selectivity is 10.4%, and the glutaric acid selectivity is 2.6%.
Example 22
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 140 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 140 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) Stirring at room temperatureThe generated peroxide was reduced for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion rate 12.88%, cyclohexanol selectivity 25.3%, cyclohexanone selectivity 56.6%, cyclohexyl hydroperoxide selectivity 0.8%, adipic acid selectivity 12.3%, glutaric acid selectivity 5.0%.
Example 23
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 145 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 145 ℃ under 1.0MPa of oxygen pressure at 800rpm for 8.0 h. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 15.64%, cyclohexanol selectivity 23.2%, cyclohexanone selectivity 49.4%, cyclohexyl hydroperoxide selectivity 0.6%, adipic acid selectivity 18.8%, glutaric acid selectivity 8.0%.
Example 24
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 150 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 150 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the resulting solution was removed and subjected to gas chromatography with toluene as an internal standardPerforming phase chromatographic analysis; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 17.78%, the cyclohexanol selectivity is 16.8%, the cyclohexanone selectivity is 46.5%, the cyclohexyl hydroperoxide selectivity is 0.2%, the adipic acid selectivity is 28.1%, and the glutaric acid selectivity is 8.4%.
Example 25
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 0.1 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 0.1MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. No significant product was detected.
Example 26
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 0.4 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 0.4MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 3.63%, cyclohexanol selectivity 36.4%, cyclohexanone selectivity 36.3%, cyclohexyl hydroperoxide selectivity 20.2%, adipic acid selectivity 6.1%, glutaric acid selectivity 1.0%.
Example 27
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 0.6 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 0.6MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion was 6.64%, cyclohexanol selectivity was 28.4%, cyclohexanone selectivity was 49.3%, cyclohexyl hydroperoxide selectivity was 18.4%, adipic acid selectivity was 3.9%, and glutaric acid formation was not detected.
Example 28
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 0.8 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 0.8MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 8.28%, the cyclohexanol selectivity is 43.7%, the cyclohexanone selectivity is 49.3%, the cyclohexyl hydroperoxide selectivity is 0.8%, the adipic acid selectivity is 5.2%, and the glutaric acid selectivity is 1.0%.
Example 29
In a 100mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -m (14 mg),0.07mg/mmol),Cu(OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.2 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.2MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.42%, cyclohexanol selectivity 36.5%, cyclohexanone selectivity 54.5%, cyclohexyl hydroperoxide selectivity 0.4%, adipic acid selectivity 6.9%, glutaric acid selectivity 1.7%.
Example 30
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.6 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.6MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.49%, cyclohexanol selectivity 37.6%, cyclohexanone selectivity 53.4%, cyclohexyl hydroperoxide selectivity 0.3%, adipic acid selectivity 7.4%, glutaric acid selectivity 1.3%.
Example 31
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.8 MPa.The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.8MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.40%, cyclohexanol selectivity 36.7%, cyclohexanone selectivity 54.3%, cyclohexyl hydroperoxide selectivity 0.5%, adipic acid selectivity 7.5%, glutaric acid selectivity 1.0%.
Example 32
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 2.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 2.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.38%, cyclohexanol selectivity 35.9%, cyclohexanone selectivity 55.1%, cyclohexyl hydroperoxide selectivity 0.6%, adipic acid selectivity 7.1%, glutaric acid selectivity 1.3%.
Example 33
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 600rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PP) was added to the reaction mixtureh3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 8.62%, cyclohexanol selectivity 39.7%, cyclohexanone selectivity 54.8%, cyclohexyl hydroperoxide selectivity 0.6%, adipic acid selectivity 4.3%, glutaric acid selectivity 0.6%.
Example 34
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 130 ℃ under 1.0MPa oxygen pressure at 1000rpm for 8.0 h. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.45%, cyclohexanol selectivity 37.0%, cyclohexanone selectivity 54.6%, cyclohexyl hydroperoxide selectivity 0.4%, adipic acid selectivity 7.1%, glutaric acid selectivity 0.9%.
Example 35
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 1200rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the resulting solution was removed,taking methylbenzene as an internal standard, and carrying out gas-phase chromatographic analysis; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.40%, cyclohexanol selectivity 36.2%, cyclohexanone selectivity 56.4%, cyclohexyl hydroperoxide selectivity 0.2%, adipic acid selectivity 6.3%, glutaric acid selectivity 0.9%.
Example 36
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 2.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 4.32%, cyclohexanol selectivity 36.6%, cyclohexanone selectivity 24.4%, cyclohexyl hydroperoxide selectivity 38.4%, adipic acid selectivity 0.6%, no formation of glutaric acid was detected.
Example 37
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 6.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The conversion rate of the cyclohexane is 6.85 percent,the selectivity of cyclohexanol was 41.9%, the selectivity of cyclohexanone was 43.4%, the selectivity of cyclohexyl hydroperoxide was 7.4%, the selectivity of adipic acid was 6.6%, and the selectivity of glutaric acid was 0.7%.
Example 38
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 12.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 11.85%, the cyclohexanol selectivity is 36.9%, the cyclohexanone selectivity is 41.4%, the cyclohexyl hydroperoxide selectivity is 0.2%, the adipic acid selectivity is 17.2%, and the glutaric acid selectivity is 4.3%.
Example 39
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 16.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion rate 12.64%, cyclohexanol selectivity 24.8%, cyclohexanone selectivity 42.4%, cyclohexyl hydroperoxide selectivity 0.2%, adipic acid selectivity 26.4%, glutaric acid selectivity 6.2%.
Example 40
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 24.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 14.84%, cyclohexanol selectivity 22.3%, cyclohexanone selectivity 32.5%, cyclohexyl hydroperoxide selectivity 0.2%, adipic acid selectivity 33.1%, glutaric acid selectivity 11.9%.
EXAMPLE 41
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -p (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 130 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The cyclohexane conversion rate is 9.68%, the cyclohexanol selectivity is 34.5%, the cyclohexanone selectivity is 56.3%, the cyclohexyl hydroperoxide selectivity is 0.4%, the adipic acid selectivity is 8.2%, and the glutaric acid selectivity is 0.6%.
Example 42
In a 100mL stainless steel high-pressure reaction kettle with a polytetrafluoroethylene inner containerA MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.92%, cyclohexanol selectivity 37.6%, cyclohexanone selectivity 53.8%, cyclohexyl hydroperoxide selectivity 0.4%, adipic acid selectivity 7.4%, glutaric acid selectivity 0.8%.
Example 43
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 14.0280g (200mmol) of cyclopentane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The conversion rate of cyclopentane was 4.13%, the selectivity for cyclopentanol was 16.5%, the selectivity for cyclopentanone was 70.2%, the selectivity for cyclopentyl hydroperoxide was 10.3%, the selectivity for glutaric acid was 2.6%, and the selectivity for succinic acid was 0.4%.
Example 44
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 19.6540g (200mmol) of cycloheptane, the reaction vessel was sealed, and the temperature was raised by stirringOxygen was introduced at 120 ℃ to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The conversion rate of cycloheptane is 19.9 percent, the selectivity of cycloheptanol is 18.1 percent, the selectivity of cycloheptanone is 62.4 percent, the selectivity of cycloheptyl hydroperoxide is 11.5 percent, the selectivity of pimelic acid is 6.8 percent, and the selectivity of adipic acid is 1.2 percent.
Example 45
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 22.4400g (200mmol) of cyclooctane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 120 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. 22.8 percent of cyclooctane conversion rate, 32.6 percent of cyclooctanol selectivity, 53.5 percent of cyclooctanone selectivity, 10.7 percent of cyclooctyl hydrogen peroxide selectivity, 3.0 percent of octanedioic acid selectivity and 0.2 percent of pimelic acid selectivity.
Example 46
In a 100mL stainless steel autoclave having a Teflon liner, MOF PCN-222(Co) -m (14mg,0.07mg/mmol), Cu (OAc)2(400mg,2mg/mmol) was dispersed in 19.6540g (200mmol) cyclododecane, the reaction vessel was sealed, the temperature was raised to 120 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 120 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water1.3115g (5.00mmol) of triphenylphosphine (PPh) were added3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. The conversion of cyclododecane was 25.9%, the selectivity for cyclododecanol was 20.1%, the selectivity for cyclododecanone was 58.5%, and the selectivity for cyclododecyl hydroperoxide was 21.4%, and no formation of aliphatic diacid was detected.
Example 47 (comparative experiment)
In a 100mL stainless steel autoclave with a Teflon liner, the MOF PCN-222(Co) -m (14mg,0.07mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the autoclave was sealed, stirred and heated to 130 deg.C, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 5.58%, cyclohexanol selectivity 36.3%, cyclohexanone selectivity 48.4%, cyclohexyl hydroperoxide selectivity 3.3%, adipic acid selectivity 10.1%, glutaric acid selectivity 1.9%.
Example 48 (comparative experiment)
In a 100mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -p (14mg,0.07mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the autoclave was sealed, stirred and heated to 130 deg.C, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the resulting solution was removed,taking methylbenzene as an internal standard, and carrying out gas chromatography analysis; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 5.46%, cyclohexanol selectivity 37.4%, cyclohexanone selectivity 47.3%, cyclohexyl hydroperoxide selectivity 3.1%, adipic acid selectivity 10.3%, glutaric acid selectivity 1.9%.
Example 49 (comparative experiment)
In a 100mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -d (14mg,0.07mg/mmol) was dispersed in 16.8320g (200mmol) cyclohexane, the autoclave was sealed, stirred and heated to 130 deg.C, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 5.86%, cyclohexanol selectivity 38.3%, cyclohexanone selectivity 45.3%, cyclohexyl hydroperoxide selectivity 2.1%, adipic acid selectivity 12.3%, glutaric acid selectivity 2.0%.
Example 50 (comparative experiment)
In a 100mL stainless steel autoclave having a polytetrafluoroethylene inner bladder, Cu (OAc)2(400mg,2mg/mmol) was dispersed in 16.8320g (200mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. The reaction was stirred at 800rpm for 8.0h at 130 ℃ under 1.0MPa of oxygen pressure. After completion of the reaction, the reaction mixture was cooled to room temperature with ice water, and 1.3115g (5.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) Stirring at room temperature for 30min to reduce the generated peroxide. The resulting reaction mixture was made to 100mL with acetone as the solvent. 10mL of the obtained solution is removed, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 2.45%, cyclohexanol selectivity 29.6%, cyclohexanone selectionThe performance was 24.8%, the cyclohexyl hydroperoxide selectivity was 45.6%, and no diacid formation was detected.
Example 51 (amplification experiment)
In a 1000mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -m (140mg,0.07mg/mmol), Cu (OAc)2(4000mg,2mg/mmol) was dispersed in 168.320g (2000mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 130 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 13.115 g (50.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The reaction mixture was made to 1000mL using acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.48%, cyclohexanol selectivity 35.1%, cyclohexanone selectivity 56.4%, cyclohexyl hydroperoxide selectivity 1.6%, adipic acid selectivity 6.3%, glutaric acid selectivity 0.6%.
Example 52 (amplification experiment)
In a 1000mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -p (140mg,0.07mg/mmol), Cu (OAc)2(4000mg,2mg/mmol) was dispersed in 168.320g (2000mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 130 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 13.115 g (50.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The reaction mixture was made to 1000mL using acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.61%, cyclohexanol selectivity 34.2%, cyclohexanone selectivity 58.4%, cyclohexyl hydroperoxide selectivity 1.1%, adipic acid selectivity 5.9%, glutaric acid selectivity 0.4%.
Example 53 (amplification experiment)
In a 1000mL stainless steel autoclave with a Teflon liner, MOF PCN-222(Co) -d (140mg,0.07mg/mmol), Cu (OAc)2(4000mg,2mg/mmol) was dispersed in 168.320g (2000mmol) of cyclohexane, the reaction vessel was sealed, the temperature was raised to 130 ℃ with stirring, and oxygen was introduced to 1.0 MPa. Stirring and reacting at 130 ℃ and 1.0MPa oxygen pressure for 8.0h at 800 rpm. After completion of the reaction, ice water was cooled to room temperature, and 13.115 g (50.00mmol) of triphenylphosphine (PPh) was added to the reaction mixture3) The resulting peroxide was reduced by stirring at room temperature for 30 min. The reaction mixture was made to 1000mL using acetone as the solvent. 10mL of the obtained solution is transferred, and gas chromatography analysis is carried out by taking toluene as an internal standard; 10mL of the resulting solution was removed and analyzed by liquid chromatography using benzoic acid as an internal standard. Cyclohexane conversion 9.84%, cyclohexanol selectivity 38.3%, cyclohexanone selectivity 54.4%, cyclohexyl hydroperoxide selectivity 0.3%, adipic acid selectivity 6.3%, glutaric acid selectivity 0.7%.
Claims (8)
1. A method for the concerted catalytic oxidation of cycloalkanes by a metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt, characterized in that it comprises the following steps:
dispersing metalloporphyrin MOFs PCN-222(Co) and Cu (II) salt into cycloalkane, wherein the mass of the metalloporphyrin MOFs PCN-222(Co) is 1% -10% of the content of the cycloalkane material, and g/mol; the amount of Cu (II) salt substance is 0.01-10% of the amount of cycloalkane substance, mol/mol; sealing the reaction system, heating to 90-150 ℃ under stirring, introducing an oxidant, keeping the set temperature and pressure, stirring for reaction for 2.0-24.0 h, and performing aftertreatment on the reaction solution to obtain a product, namely cycloalkyl alcohol and cycloalkyl ketone;
the metalloporphyrin MOFs PCN-222(Co) contains at least one metalloporphyrin unit of compounds shown in a formula (I), a formula (II) and a formula (III):
the above-mentionedThe Cu (II) salt is Cu (CH)3COO)2,Cu(NO2)2,CuSO4,CuCl2And hydrates thereof, or a mixture of at least two of the hydrates in any proportion;
the cycloalkane is one of cyclopentane, cyclohexane, cycloheptane, cyclooctane, cyclononane, cyclodecane and cyclododecane or a mixture of at least two of the above materials in any proportion.
2. The method for the concerted catalytic oxidation of cycloalkanes with metalloporphyrin MOFs PCN-222(Co)/cu (ii) salts according to claim 1, wherein the catalyst is a binary combination of metalloporphyrin MOFs PCN-222(Co) and cu (ii) salts.
3. The method for the concerted catalytic oxidation of cycloalkanes by metalloporphyrin MOFs PCN-222(Co)/cu (ii) salts according to claim 1 or 2, wherein the ratio of the mass of metalloporphyrin MOFs PCN-222(Co) to the amount of cycloalkanes is 1: 100 to 1: 10.
4. The method for the concerted catalytic oxidation of cycloalkanes with metalloporphyrin MOFs PCN-222(Co)/Cu (II) salt according to claim 1 or 2, wherein the mass ratio of Cu (II) salt to cycloalkanes is 1: 10000 to 1: 10.
5. The method for the concerted catalytic oxidation of cycloalkanes with metalloporphyrin MOFs PCN-222(Co)/Cu (II) salts according to claim 1 or 2, wherein the reaction pressure is 0.10-2.0 MPa.
6. The method for the concerted catalytic oxidation of cycloalkanes with metalloporphyrin MOFs PCN-222(Co)/Cu (II) salts according to claim 1 or 2, wherein the stirring speed is 600-1200 rpm.
7. The process for the concerted catalytic oxidation of cycloalkanes with metalloporphyrin salts, MOFs PCN-222(Co)/cu (ii), according to claim 1 or 2, wherein said oxidant is oxygen, air or a mixture thereof in any proportion.
8. The metalloporphyrin PCN-222(Co)/Cu (II) salt Co-catalyzed oxidation method of cycloalkanes according to claim 1, wherein said post-treatment method is: after the reaction is finished, adding triphenylphosphine PPh into the reaction solution3And the using amount is 3 percent of the amount of the cyclane substance, the peroxide generated by reduction is stirred for 40min at room temperature, and the crude product is distilled, rectified under reduced pressure and recrystallized to obtain an oxidation product.
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