H-Pro-Pro-Asp-NH2
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H-Pro-Pro-Asp-NH2

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H-Pro-Pro-Asp-NH2, adsorbed on modified silica gel, is a highly efficient recyclable chiral catalyst for aldol reactions.

Category
Others
Catalog number
BAT-014673
CAS number
850440-85-6
Molecular Formula
C14H22N4O5
Molecular Weight
326.35
IUPAC Name
(3S)-4-amino-4-oxo-3-[[(2S)-1-[(2S)-pyrrolidine-2-carbonyl]pyrrolidine-2-carbonyl]amino]butanoic acid
Synonyms
H-PPD-NH2; L-prolyl-L-prolyl-L-isoasparagine; L-Prolyl-L-prolyl-L-α-asparagine; (S)-4-amino-4-oxo-3-((S)-1-((S)-pyrrolidine-2-carbonyl)pyrrolidine-2-carboxamido)butanoic acid
Appearance
White Powder
Purity
≥95%
Density
1.375±0.06 g/cm3 (Predicted)
Boiling Point
733.3±60.0°C (Predicted)
Sequence
Pro-Pro-Asp-NH2
Storage
Store at -20°C
Solubility
Soluble in Water
InChI
InChI=1S/C14H22N4O5/c15-12(21)9(7-11(19)20)17-13(22)10-4-2-6-18(10)14(23)8-3-1-5-16-8/h8-10,16H,1-7H2,(H2,15,21)(H,17,22)(H,19,20)/t8-,9-,10-/m0/s1
InChI Key
KPDOVORMRIAAGW-GUBZILKMSA-N
Canonical SMILES
C1CC(NC1)C(=O)N2CCCC2C(=O)NC(CC(=O)O)C(=O)N
1. Asymmetric aldol reactions catalyzed by efficient and recyclable silica-supported proline-based peptides
Jincan Yan, Lei Wang Chirality. 2009 Apr;21(4):413-20. doi: 10.1002/chir.20603.
A series of silica-supported proline-based peptides were synthesized and applied as catalysts for direct asymmetric intermolecular aldol reactions. Among these, a peptide with two L-proline units was found to be the most efficient one for the asymmetric aldol reactions between acetone and aromatic aldehydes. The reactions generated the corresponding products with satisfactory isolated yields (up to 97%) and enantiomeric excesses (up to 96%) in the presence of this catalyst (5 mol %). Furthermore, the silica-supported organocatalyst could be recovered and recycled by a simple filtration of the reaction solution and used for five consecutive trials without loss of its reactivity.
2. Tripeptides of the type H-D-Pro-Pro-Xaa-NH2 as catalysts for asymmetric 1,4-addition reactions: structural requirements for high catalytic efficiency
Markus Wiesner, Markus Neuburger, Helma Wennemers Chemistry. 2009 Oct 5;15(39):10103-9. doi: 10.1002/chem.200901021.
Analysis of the structural and functional requirements within the asymmetric peptidic catalyst H-D-Pro-Pro-Asp-NH(2) led to the development of the closely related peptide H-D-Pro-Pro-Glu-NH(2) as an even more efficient catalyst for asymmetric conjugate addition reactions of aldehydes to nitroolefins. In the presence of as little as 1 mol % of H-D-Pro-Pro-Glu-NH(2), a broad range of aldehydes and nitroolefins react readily with each other. The resulting gamma-nitroaldehydes were obtained in excellent yields and stereoselectivities at room temperature. Within the structure of the peptidic catalysts, the D-Pro-Pro motif is the major contributor to the high stereoselectivities. The C-terminal amide and the spacer to the carboxylic acid in the side-chain of the C-terminal amino acid are responsible for the fine-tuning of the stereoselectivity. The peptidic catalysts not only allow for highly effective asymmetric catalysis under mild conditions, but also function in the absence of additives.
3. A solid-supported organocatalyst for continuous-flow enantioselective aldol reactions
Carles Ayats, Andrea H Henseler, Miquel A Pericàs ChemSusChem. 2012 Feb 13;5(2):320-5. doi: 10.1002/cssc.201100570.
Asymmetric aldol reactions catalyzed by a novel polystyrene-immobilized proline derivative occur in short reaction times with excellent diastereo- and enantioselectivity. The catalyst can be recovered by simple filtration and shows very high reusability. The high activity depicted by the supported catalyst and its chemical and mechanical stability have allowed its application in packed-bed reactors for continuous flow processing. This system can produce enantio- and diastereomerically pure aldol adducts under continuous flow conditions with a residence time of 26 min. Furthermore, the reactor allowed processing of four different aldol products in sequence without any decrease in both catalytic activity and optical purity. The effective catalyst loading could be reduced to 1.6% (six-fold reduction of catalyst loading compared to the corresponding batch process).
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