| Literature DB >> 35492625 |
Zhenghao Zhai1, Xue Du1, Qingshi Wu2, Lin Zhu1, Zahoor H Farooqi3, Jin Li1, Ruyue Lan1, Yusong Wang4, Weitai Wu1.
Abstract
The catalysis of boronic acids immobilized in polymer microgels can be modulated by bubbling with N2/CO2 gas, and in some cases by adding glucose, making their catalytic activity comparable or even superior to that of the corresponding free boronic acid monomers homogeneously dispersed in solutions and, more importantly, making these boronic-acid-containing polymer microgels able to catalyze alternate reactions that may extend the usefulness. This enhanced catalytic function of these boronic-acid-containing microgels as organoboron acid catalysts is plausibly achieved via in situ reversibly structural variations. Kinetic studies have been carried out on the model boronic-acid-catalyzed aza-Michael addition, aldol, amidation, and [4 + 2] cycloaddition reactions in order to better understand the catalytic process. This journal is © The Royal Society of Chemistry.Entities:
Year: 2020 PMID: 35492625 PMCID: PMC9048991 DOI: 10.1039/c9ra10541g
Source DB: PubMed Journal: RSC Adv ISSN: 2046-2069 Impact factor: 4.036
Scheme 1Synthesis of the proposed PBA@PM.
Fig. 1Typical (a–c) TEM images of the PBA@PM. (d) EELS spectra of the PBA@PM along the line shown in the TEM image in (c).
Fig. 2Typical IR spectrum of the PBA@PM. IR spectra of 1 and 2 are shown for comparison.
Fig. 3Typical 11B NMR spectra of the PBA@PM dispersed in CD2Cl2/D2O (9 : 1 in volume) upon bubbling with N2 or CO2 gas. Results of 1 are shown for comparison.
Fig. 4Glucose-dependent 〈Dh〉 of the PBA@PM dispersed in CH2Cl2/water (9 : 1 in volume) upon bubbling with N2 or CO2 gas, measured at 10.0 °C and at a scattering angle of 45°.
Scheme 2In situ structural variations in the PBA@PM upon bubbling with N2/CO2 gas, in the absence or in the presence of glucose.
Fig. 5(a) The catalytic aza-Michael addition as a model for evaluating the accessibility and the catalytic performance of the PBA@PM. (b–e) Influence of temperature on k, measured in the reaction mixture in the absence (b and c; [Glu] = 0.0 mM) or in the presence (d and e; [Glu] = 1.5 mM) of glucose, upon bubbling with N2 (b and d) or CO2 (c and e) gas, where lines are first-order kinetic fits.
Fig. 6(a) Influence of the [Glu] on the k of aza-Michael addition catalyzed by the PBA@PM at 10.0 °C. (b) The ln k–1000/T plots, where the solid lines are linear fitting of the plots.
Apparent activation parameters for the aza-Michael addition catalyzed by the PBA@PM
| [Glu] (mM) | Bubbling with N2 gas | Bubbling with CO2 gas | ||
|---|---|---|---|---|
|
|
|
|
| |
| 0.0 | 1.3 × 1016 | 101.3 | 1.3 × 1014 | 109.3 |
| 1.5 | 9.1 × 1015 | 85.7 | 1.2 × 1014 | 109.4 |
Fig. 7(a) A model aldol reaction of hydroxyacetone and aldehyde catalyzed by the PBA@PM. (b and c) Time trace of the yield of aldol adduct 7, measured in the reaction mixture in the absence (b; [Glu] = 0.0 mM) or in the presence (c; [Glu] = 1.5 mM) of glucose, upon bubbling with N2 (■,□) or CO2 (●,○) gas, and at 10.0 °C, where CHA,0 is the starting concentration of hydroxyacetone, C7, is the concentration of 7 at the reaction time t, and lines are first-order kinetic fits.
Fig. 8(a) A model amidation reaction of carboxylic acid and amine catalyzed by the PBA@PM. (b and c) Time trace of the yield of amide product 8, measured in the reaction mixture in the absence (b; [Glu] = 0.0 mM) or in the presence (c; [Glu] = 1.5 mM) of glucose, upon bubbling with N2 (■,□) or CO2 (●,○) gas, and at 10.0 °C, where CCA,0 is the starting concentration of carboxylic acid, C8, is the concentration of 8 at the reaction time t, and lines are first-order kinetic fits.
Fig. 9(a) A model [4 + 2] cycloaddition of acrylic acid and diene catalyzed by the PBA@PM. (b and c) Time trace of the yield of cycloadduct 9, measured in the reaction mixture in the absence (b; [Glu] = 0.0 mM) or in the presence (c; [Glu] = 1.5 mM) of glucose, upon bubbling with N2 (■,□) or CO2 (●,○) gas, and at 10.0 °C, where CAA,0 is the starting concentration of acrylic acid, C9, is the concentration of 9 at the reaction time t, and lines are first-order kinetic fits.
Comparison of results for the model boronic-acid-catalyzed reactions
|
| |||||
|---|---|---|---|---|---|
| Product | Catalyst | Temperature | Time | Yield | |
| 6 | PBA@PM | 10.0 °C | 16 h | 36% | This work |
| PBA@PM | 12.5 °C | 16 h | 52% | This work | |
| PBA@PM | 15.0 °C | 16 h | 58% | This work | |
| PBA@PM | 17.5 °C | 16 h | 69% | This work | |
| PBA@PM | 20.0 °C | 16 h | 79% | This work | |
| Cata- | −10 °C | 16 h | 89% |
| |
| 6-a | PBA@PM | 10.0 °C | 16 h | 37% | This work |
| PBA@PM | 20.0 °C | 16 h | 80% | This work | |
| cata- | −10 °C | 16 h | 88% |
| |
| 6-b | PBA@PM | 10.0 °C | 16 h | 39% | This work |
| PBA@PM | 20.0 °C | 16 h | 82% | This work | |
| Cata- | −10 °C | 24 h | 81% |
| |
| 7 | PBA@PM | 10.0 °C | 7 h | 76% | This work |
| PBA@PM | 20.0 °C | 7 h | 95% | This work | |
| Cata- | R.T. | 7 h | 64% |
| |
| 7-a | PBA@PM | 10.0 °C | 7 h | 81% | This work |
| PBA@PM | 20.0 °C | 7 h | 99% | This work | |
| Cata- | R.T. | 7 h | 68% |
| |
| 7-b | PBA@PM | 10.0 °C | 7 h | 79% | This work |
| PBA@PM | 20.0 °C | 7 h | 96% | This work | |
| Cata- | R.T. | 7 h | 62% |
| |
| 8 | PBA@PM | 10.0 °C | 48 h | 8% | This work |
| PBA@PM | 20.0 °C | 48 h | 9% | This work | |
| Cata- | R.T. | 48 h | 99% |
| |
| 8-a | PBA@PM | 10.0 °C | 48 h | 5% | This work |
| PBA@PM | 20.0 °C | 48 h | 6% | This work | |
| Cata- | R.T. | 48 h | 95% |
| |
| 8-b | PBA@PM | 10.0 °C | 48 h | 3% | This work |
| PBA@PM | 20.0 °C | 48 h | 6% | This work | |
| Cata- | R.T. | 48 h | 73% |
| |
Bubbling with N2 gas, [Glu] = 0.0 mM.
Bubbling with CO2 gas, [Glu] = 0.0 mM.
Bubbling with N2 gas, [Glu] = 1.5 mM.
Bubbling with CO2 gas, [Glu] = 1.5 mM.
Performed with hydroxamic acid (2.5 × 10−3 mol L−1) and quinone imine ketal (1.0 × 10−4 mol L−1) in CH2Cl2/water (9 : 1 in volume; 100.0 mL), and the concentration of boronic acids in the reaction system of ca. 1.2 × 10−5 mol L−1.
Performed with hydroxamic acid (1.3 × 10−1 mol L−1) and quinone imine ketal (0.1 mol L−1) in CH2Cl2 (1.0 mL); the concentration of boronic acids in the reaction system was ca. 1.0 × 10−2 mol L−1, and o-nitrobenzoic acid (5.0 × 10−2 mol L−1) as a co-catalyst.
Performed with hydroxyacetone (1.0 × 10−4 mol L−1) and aldehyde (2.5 × 10−3 mol L−1) in CH2Cl2/water (9 : 1 in volume; 100.0 mL), and the concentration of boronic acids in the reaction system of ca. 1.2 × 10−5 mol L−1.
Performed with hydroxyacetone (5.5 mol L−1) and aldehyde (5.5 × 10−1 mol L−1) in water (2.0 mL), and the concentration of boronic acids in the reaction system of ca. 3.6 × 10−2 mol L−1.
Performed with carboxylic acid (1.0 × 10−4 mol L−1) and amine (2.5 × 10−3 mol L−1) in CH2Cl2/water (9 : 1 in volume; 100.0 mL), and the concentration of boronic acids in the reaction system of ca. 1.2 × 10−5 mol L−1.
Performed with carboxylic acid (7.8 × 10−2 mol L−1) and amine (7.1 × 10−2 mol L−1) in CH2Cl2 (7.0 mL), the concentration of boronic acids in the reaction system of ca. 7.1 × 10−3 mol L−1, and adding the activated 4A molecular sieves (1.0 g).