| Literature DB >> 33662183 |
Fabián Amaya-García1,2, Michael Caldera3,4, Anna Koren3, Stefan Kubicek3, Jörg Menche3,4, Miriam M Unterlass1,2,3.
Abstract
Here, the hydrothermal synthesis (HTS) of 2,3-diarylquinoxalines from 1,2-diketones and o-phenylendiamines (o-PDAs) was achieved. The synthesis is simple, fast, and generates high yields, without requiring any organic solvents, strong acids or toxic catalysts. Reaction times down to <10 min without decrease in yield could be achieved through adding acetic acid as promoter, even for highly apolar biquinoxalines (yield >90 % in all cases). Moreover, it was shown that HTS has high compatibility: (i) hydrochlorides, a standard commercial form of amines, could be used directly as combined amine source and acidic catalyst, and (ii) Boc-diprotected o-PDA could be directly employed as substrate that underwent HT deprotection. A systematic large-scale computational comparison of all reported syntheses of the presented quinoxalines from the same starting compounds showed that this method is more environmentally friendly and less toxic than all existing methods and revealed generic synthetic routes for improving reaction yields. Finally, the application of the synthesized compounds as fluorescent dyes for cell staining was explored.Entities:
Keywords: computational analysis; fluorescence; green chemistry; hydrothermal synthesis; quinoxalines
Year: 2021 PMID: 33662183 PMCID: PMC8252754 DOI: 10.1002/cssc.202100433
Source DB: PubMed Journal: ChemSusChem ISSN: 1864-5631 Impact factor: 8.928
Scheme 1(A) Synthetic approach of this work. (B) Classical synthesis towards 2,3‐diarylquinoxalines. (C) Schematic of the physicochemical properties of water (ϵ=static dielectric constant, η=viscosity, ρ=density, K w=self‐ionization of water) as a function of temperature (adapted from references [29, 30]) and examples of heteroaromatics obtained between 150–250 °C (in the HT regime).
c
). These regimes vary substantially in physicochemical properties, and consequently also in the necessary equipment. First, the autogenous pressure of water is still moderate until 250 °C, but relatively high at >250 °C, that is, in proximity to the critical point. Hence, synthesis in sub‐ and supercritical water places more stringent demands on reaction vessel engineering than HTS. Second, through structural changes in H2O(l) with T, properties that are very relevant for synthesis, such as density, viscosity, polarity, and acidity/basicity, also change drastically and with different signatures.[ , , ] The density and viscosity of H2O(l) decrease with T, which is beneficial for mass transfer in all regimes, often resulting in astonishingly short t r. Polarity‐wise, the lower HT regime is still quite polar, while the HT regime at 150 °C≤T r≤250 °C spans relative permittivities of approximately 41 (corresponding to glycerol at RT) to approximately 25 (corresponding to ethanol at RT), while the subcritical regime is already fairly apolar, and the supercritical regime fully apolar (Scheme 1C). Moreover, the maximal acidity and basicity of water through its autoprotolysis are found at approximately 250 °C but are lower at both lower and higher T. Thus, around T r≈250 °C Brønsted acid/base catalysis is provided by the medium itself, which is convenient for many reactions, including condensations. As indicated by prior work,[ , , , , , ] and further substantiated through this contribution, the HT range of approximately 250 °C seems privileged for generating heteroaromatics through condensations, possibly enabled through an optimal combination and interplay of the relevant physicochemical characteristics of the medium.Screening of reaction conditions for synthesizing quinoxaline 1.
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|---|---|---|---|---|---|
|
Entry |
|
|
|
Additive |
Yield[b] [%] |
|
1 |
0.02 |
110 |
10 |
– |
4 |
|
2 |
0.02 |
150 |
10 |
– |
29 |
|
3 |
0.02 |
200 |
10 |
– |
56 |
|
4 |
0.02 |
230 |
10 |
– |
61 |
|
5 |
0.01 |
230 |
5 |
– |
38 |
|
6 |
0.02 |
230 |
5 |
– |
51 |
|
7 |
0.04 |
230 |
5 |
– |
65 |
|
8 |
0.20 |
230 |
5 |
– |
82 |
|
9 |
0.50 |
230 |
5 |
– |
83 |
|
10 |
1.00 |
230 |
5 |
– |
86 |
|
11 |
0.20 |
230 |
10 |
– |
88 |
|
12 |
0.20 |
230 |
30 |
– |
94 |
|
13 |
0.20 |
230 |
60 |
– |
|
|
14 |
0.02 |
230 |
10 |
HOAc (10 equiv.) |
89 |
|
15 |
0.02 |
230 |
10 |
DIPEA |
39 |
|
16 |
0.20 |
230 |
10 |
HOAc (4.3 equiv.) |
|
|
17 |
0.20 |
230 |
10 |
HOAc (2.6 equiv.) |
97 |
|
18 |
0.20 |
230 |
10 |
HOAc (1.0 equiv.) |
97 |
|
19 |
0.20 |
230 |
10 |
oxalic acid (4.3 equiv.) |
33 |
|
20 |
0.20 |
230 |
10 |
oxalic acid (2.6 equiv.) |
47 |
|
21 |
0.20 |
230 |
10 |
oxalic acid (1.0 equiv.) |
75 |
|
22 |
0.20 |
230 |
10 |
oxalic acid (0.1 equiv.) |
86 |
|
23 |
0.20 |
230 |
10 |
oxalic acid (0.05 equiv.) |
90 |
|
24 |
0.20 |
230 |
10 |
propionic acid (4.3 equiv.) |
|
|
25 |
0.20 |
230 |
10 |
propionic acid (2.6 equiv.) |
95 |
|
26 |
0.20 |
230 |
10 |
propionic acid (1.0 equiv.) |
97 |
[a] P at 230 °C: 20–22 bar, at 200 °C: 15–20 bar, at 150 °C: 15–20 bar, and at 110 °C: max. 5 bar. [b] Determined by 1H NMR spectroscopy; q=quantitative conversion.
Scheme 2Scope of 1,2‐diketone and o‐PDA in HTS of (A) quinoxalines and (B) biquinoxalines (p r=20–22 bar).
Scheme 3One‐pot Boc‐deprotection–quinoxaline formation sequence under HT conditions (p r=20–22 bar). Yields: 73 % with t r=10 min and 76 % with t r=30 min.
Scheme 4Reaction between o‐PDA dihydrochloride and 1,2‐diketones under HT conditions (p r=20–22 bar).
Figure 1(A) Overview of the reaction parameter extraction pipeline. (B) Differences between HTS of quinoxalines and the reported literature synthesis. The spider plot depicts with dashed borders n=323 reactions that report all of the five parameters (solvent, catalyst, T r, t r and yield) used in the analysis. The black solid line indicates the average of all the 323 considered reactions whereas the blue solid line represents the average of HT conditions. Spider plots for individual compounds are included in the Supporting Information (Figure S36) The different histograms were plotted considering the number of reactions that report the corresponding parameter: solvent (n=452), catalyst (n=484), T r (n=479), t r (n=538), yield (n=513). (C) Reaction space of 2,3‐diarylquinoxalines with overlay of the 5 investigated features. Green depicts a more favourable reaction parameter whereas red indicates less favourable conditions. (D) t‐SNE dimension reduction depicting clusters of favourable reaction conditions. (E) Possible reaction strategies to improve reaction yields.
Figure 2Fluorescence microscopy images of the indicated cell lines after treatment with solutions 1.5 μm in DMSO of quinoxalines 1, 4 and 5 (scale bar 200 μm). Results for all of the compounds are included in the Supporting Information (Figure S41).