| Literature DB >> 35036792 |
Artyom E Paromov1, Sergey V Sysolyatin1.
Abstract
Here, we explored in detail an acid-catalyzed condensation of glyoxylic acid or its ethyl ester with several carboxamides of different basicity, or with mesyl amide, to furnish diaminoacetic acid derivatives. The most suitable synthesis conditions and the reaction catalysts were identified. Properties such as structure and basicity of the starting amides were demonstrated to influence the condensation process. Elemental iodine was used for the first time herein as an acid catalyst for the condensation of glyoxylic acid or its ester, which gave access to diaminoacetic acid derivatives in higher yields in most cases, as opposed to p-toluenesulfonic acid (PTSA). An abnormally high activity of mesyl amide when condensed with ethyl glyoxylate was noticed, which may evidence a special impact of the sulfonyl moiety in the amide molecule on the condensation.Entities:
Year: 2021 PMID: 35036792 PMCID: PMC8757442 DOI: 10.1021/acsomega.1c05916
Source DB: PubMed Journal: ACS Omega ISSN: 2470-1343
Figure 1Structural formulas of RDX, HMX, and CL-20.
Scheme 1Synthesis of Polyheterocyclic Cage Molecules from Diaminoacetic Acid Derivatives
Scheme 2Synthesis of 1,3-Bis(1,3-dinitroimidazol-idin-2-yl)urea (1)
Scheme 3Synthesis of Derivatives 2a–i
Synthesis of Compounds 2a–i in Toluene at Reflux without Catalyst
| entry | condensation product | yield, % |
|---|---|---|
| 1 | 60.9 | |
| 2 | 62.5 | |
| 3 | 67.9 | |
| 4 | 61.2 | |
| 5 | no reaction | |
| 6 | 72.9 | |
| 7 | 73.9 | |
| 8 | below 30 | |
| 9 | 74.4 |
Most Favorable Conditions in Which Compounds 2a–i Are Formed in Toluene at Reflux over the PTSA Catalyst
| entry | condensation product | ω (PTSA), % | t, h | yield, % |
|---|---|---|---|---|
| 1 | 0.03 | 3 | 57.4 | |
| 2 | 0.06 | 5 | 71.2 | |
| 3 | 0.06 | 3 | 71.5 | |
| 4 | 0.06 | 4 | 64.5 | |
| 5 | 0.13 | 4 | 78.4 | |
| 6 | 0.19 | 3 | 73.6 | |
| 7 | 0.25 | 4 | 76.2 | |
| 8 | 0.12 | 3 | 77.1 | |
| 9 | 0.06 | 4 | 76.0 |
Content by weight in the mixture (including toluene).
Most Favorable Conditions in Which Compound 1 Is Formed in Toluene at Reflux over the I2 Catalyst
| entry | condensation product | ω (I2), % | t, h | yield, % |
|---|---|---|---|---|
| 1 | 0,33 | 4 | 62.9 | |
| 2 | 0,11 | 4 | 68.4 | |
| 3 | 0,11 | 4 | 63.5 | |
| 4 | 0,21 | 3 | 68.5 | |
| 5 | 0,40 | 5 | 78.4 | |
| 6 | 0,77 | 4 | 77.5 | |
| 7 | 0,33 | 4 | 79.5 | |
| 8 | 0,33 | 3 | 77.9 | |
| 9 | 0,54 | 5 | 72.8 |
Content by weight in the mixture (including toluene).
The presence of I2 decreases the yield.
Comparative Data on Yields of Compounds 2a–i at Constant Synthesis Times and Acid Catalyst Quantities
| entry | condensation product | ω (PTSA/I2), % | t, h | yield (PTSA/I2), % |
|---|---|---|---|---|
| 1 | 0,06/0,11 | 4 | 49,9/50,1 | |
| 2 | 0,06/0,11 | 4 | 65,7/68.4 | |
| 3 | 0,06/0,11 | 4 | 66,9/63.5 | |
| 4 | 0,06/0,11 | 4 | 64,5/59,0 | |
| 5 | 0,13/0,33 | 3 | 78,2/77,8 | |
| 6 | 0,13/0,33 | 3 | 73,3/69,3 | |
| 7 | 0,13/0,33 | 3 | 73,7/76,3 | |
| 8 | 0,13/0,33 | 3 | 77.1/77.9 | |
| 9 | 0,13/0,33 | 3 | 53,3/71,0 |
Content by weight in the mixture (including toluene).
The presence of I2 decreases the yield.
Most Favorable Conditions in Which Compound 1 Is Formed in Toluene at Reflux over the I2 Catalyst
| entry | condensation product | ω (PTSA/I2), % | t (PTSA/I2), h | yield (PTSA/I2), % |
|---|---|---|---|---|
| 1 | no catalyst | 4 | 50.4 | |
| 2 | 0.016/0.11 | 4 | 51.1/50.5 | |
| 3 | 0.03/0.22 | 4 | 54,5/59.7 | |
| 4 | 0.047/0.33 | 4 | 52.4/62.9 | |
| 5 | 0,06/0.44 | 4 | 49.9/59.3 | |
| 6 | no catalyst | 4 | no formation | |
| 7 | 0.05/0.22 | 3/4 | 71.4/29.8 | |
| 8 | 0.08/0.34 | 3/4 | 77.5/77.0 | |
| 9 | 0.11/0.45 | 3/4 | 78.2/76.7 | |
| 10 | 0.13/0.67 | 3/4 | 77.7/4.1 |
Content by weight in the mixture.