Submitted:
24 December 2024
Posted:
25 December 2024
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Abstract
The utilization of the homogeneous (S)-2-pyrrolidine-tetrazole organocatalyst (Ley catalyst) in the self-condensation of ethyl pyruvate and cross-aldol reactions of ethyl pyruvate donor with non-enolizable pyruvate acceptors, namely the sterically hindered ethyl 3-methyl-2-oxobutyrate or the highly electrophilic methyl 3,3,3-trifluoropyruvate, is described as the key enantioselective step toward the synthesis of the corresponding biologically relevant isotetronic acids featuring a quaternary carbon functionalized with ester and alkyl groups. The transition from homogeneous to heterogeneous flow conditions is also investigated, detailing the fabrication and operation of packed-bed reactors filled with silica-supported version of the pyrrolidine-tetrazole catalyst (SBA-15 as the matrix).

Keywords:
1. Introduction
2. Results and Discussion
3. Materials and Methods
3.1. Self-Aldol Reaction of Ethyl Pyruvate 1 Promoted by the Ley Catalyst 4 (Table 1, entry 4)
3.2. Cross-Aldol Reaction of Ethyl Pyruvate 1 with Ethyl 3-methyl-2-oxobutyrate 6 Promoted by the Ley Catalyst 4 (Table 2, Entry 4)
3.3. Cross-Aldol Reaction of Ethyl Pyruvate 1 with Methyl Trifluoropyruvate 8 Promoted by the Ley Catalyst 4 (Scheme 2)
3.4. Procedure for the Heterogeneous Synthesis of the Hydroxy-Free QC-Isotetronic Acid 12 (Scheme 3) and Protected Isotetronic Acid 2 Under Batch Conditions
3.5. Fabrication of Mesoreactor R
3.6. Experimental Set-Up for Flow Experiments and Continuous-Flow Synthesis of Isotetronic Acids 2, 7, and 9 (Table 4)
3.7. Long-Term Stability Experiment (Figure 4)
4. Conclusions
Supplementary Materials
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Sample Availability
References
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| Entry1 | Catalyst (mol%) | Solvent | Time | Yield (%)2 | ee (%)3 |
| 1 | 3 (30)4 | i-PrOH | 16h | 59 | 86 |
| 2 | 4 (30) | i-PrOH | 8h | 26 | 61 |
| 3 | 4 (20) | i-PrOH | 12h | 31 | 61 |
| 4 | 4 (10) | i-PrOH | 18h | 46 | 62 |
| 5 | 4 (5) | i-PrOH | 5d | 35 | 61 |
| 6 | 4 (5) | MeCN | 5d | 27 | 49 |
| 7 | 4 (5) | DMSO | 5d | 32 | 54 |
| 8 | 5-TFA (30)5 | i-PrOH | 7d | <5 | / |
| 9 | 5-AcOH (30)5 | i-PrOH | 7d | <5 | / |
| 10 | 5-TFA (30)5 | MeCN | 7d | <5 | / |
| 11 | 5-AcOH (30)5 | MeCN | 7d | <5 | / |
| 12 | 5-TFA (30)5 | DMSO | 7d | <5 | / |
| 13 | 5-AcOH (30)5 | DMSO | 7d | <5 | / |
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| Entry1 | Catalyst (mol%) | 6:1 | time | Yield (%)2/ee (%)3 | |
| 2 | 7 | ||||
| 1 | 3 (30) | 1:1 | 5d | 40 (72) | 10 (71) |
| 2 | 4 (30) | 1:1 | 5d | 32 (61) | 12 (98) |
| 3 | 3 (30) | 10:1 | 7d4 | 15 (23) | 35 (74) |
| 4 | 4 (30) | 10:1 | 7d4 | 34 (55) | 40 (98) |
| 5 | 4 (20) | 10:1 | 7d4 | 8 (26) | 29 (97) |
| 6 | 4 (30) | 10:1 | 3d4 | 22 (51) | 32 (95) |
| 7 | 5-TFA5 (30) | 10:1 | 7d4 | <5 (/) | <5 (/) |
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| SiO2@Ley (mg)1 |
VG (mL)2 |
Vo [μL]3 |
Total Porosity4 |
Time [min]5 |
p [bar]6 |
| 356 | 346 | 249 | 0.72 | 25 | 4 |
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| Entry |
1 (c [M]) |
Acceptor (c [M]) |
Flow Rate (μLmin-1) |
Conversion (%)2 |
Isotetronic Acid (%)3 |
ee (%)4 |
TOF4 |
| 1 | 0.14 | - | 20 | 32 | 2 (25) | 86 | 1.5 |
| 2e | 0.14 | - | 10 | 78 | 2 (70) | 86 | 3.7 |
| 3 | 0.14 | 5 | >95 | 2 (91) | 86 | 4.8 | |
| 4 | 0.14 | 6 (2.67) | 5 | >95 | 7 (76) | 98 | 4.8 |
| 5 | 0.14 | 8 (0.28) | 5 | >95 | 9 (82) | 75 | 4.8 |
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