Cell penetrating agents were designed and synthesized that introduce cationic and hydrophobic moieties along the backbone of a polyproline helix (PPII) in an amphiphilic manner. The CD profile has the features that are expected for a PPII helix, demonstrating that the addition of these groups had little effect on the backbone structure. Dramatic increases in uptake were found with MCF-7 cells when up to six guanidinium groups were positioned on the polyproline helix, whereas only modest increases in cellular uptake were observed with the amine-containing polyproline compounds as compared to their flexible counterparts. Amphiphilicity played a key role in the enhanced cell translocation, as scrambled versions of the designed agents, with hydrophobic and cationic groups on all faces of the helix, were only as effective as their flexible peptide counterparts. Interestingly, the most potent agent, P11LRR, demonstrated almost an order of magnitude more efficient cellular uptake as compared to that of the well-studied Tat peptide, with minimal cytotoxicity.

Oligonucleotide drugs show promise to treat diseases afflicting millions of people. To address the need to manufacture large quantities of oligonucleotide therapeutics, the novel convergent liquid-phase synthesis has been developed for an 18-mer oligonucleotide drug candidate. Fragments containing tetra- and pentamers were synthesized and assembled into the 18-mer without column chromatography, which had a similar impurity profile to material made by standard solid-phase oligonucleotide synthesis. Two of the fragments have been synthesized at ∼3 kg/batch sizes and four additional tetra- and pentamer fragments were synthesized at >300-g scale, and a 34-mer was assembled from the fragments. Critical impurities are controlled in the fragment syntheses to provide oligonucleotides of purities suitable for clinical use after applying standard full-length product purification process. Impurity control in the assembly steps demonstrated the potential to eliminate chromatography of full-length oligonucleotides, which should enhance scalability and reduce the environmental impact of the process. The convergent assembly and telescoping of reactions made the long synthesis (>60 reactions) practical by reducing production time, material loss, and chances for impurity generation.

Trimethylammonium functionalized gold nanoparticles are demonstrated as templates for the assembly of peptide fragments and their subsequently promoted ligation. This system displays the use of organically tailored nanoparticles as effective supramolecular reagents for catalyzing bond-forming reactions and may also serve as a model for prebiotic conditions where charged surfaces may have promoted the polymerization of the early biopolymers.

Oligonucleotides containing phosphorothioate (PS) linkages have recently demonstrated significant clinical utility. PS oligonucleotides are manufactured via a solid-phase chain elongation process in which a four-reaction cycle consisting of detritylation, coupling, sulfurization, and failure sequence capping with AcO is repeated. In the capping step, uncoupled sequences are acetylated at the 5'-OH to stop the chain growth and control the levels of deletion, or ( n-1), impurities. Herein, we report that the byproducts of commonly used sulfurization reagents react with the 5'-OH and cap the failure sequences. The standard AcO capping step can therefore be eliminated, and this 3-reaction cycle process affords a higher yield and higher or comparable overall purity compared to the conventional 4-reaction synthesis. This improvement results in reducing the number of reactions from ∼80 to ∼60 for the synthesis of a typical length 20-mer oligonucleotide. For every kilogram of an oligonucleotide intermediate synthesized, > 500 L of reagents and organic solvents is saved, and the E-factor is decreased to <1500 from ∼2000.

The understanding, control, and removal of nonoligonucleotide process-related impurities (PRI) are of key importance for the manufacturing of therapeutic oligonucleotides as their presence in the final product is both a quality and safety concern. Regulatory agencies require manufacturers to demonstrate that PRI are under control or adequately purged during the manufacturing process. Purging depends on the physicochemical properties of the impurities and the unit operations of the manufacturing process but should be independent of oligonucleotide size or type. The purging power of unit operations relevant to oligonucleotide manufacturing (synthesis, cleavage and deprotection, chromatography, ultrafiltration/diafiltration) was measured using representative solvents and other small molecules typical for oligonucleotide synthesis. The results show that each unit operation has significant purging capability (synthesis >1000; cleavage and deprotection >100 (reactivity, when applicable); chromatography >1000; ultrafiltration/diafiltration >10) and that large overall purge factors can be obtained (≥1 × 107). Experimentally determined purge values are aligned with theoretical purge values; thus, the use of purge arguments in oligonucleotide control strategies is a sound scientific approach. Guidance on reasonable purge values for oligonucleotide unit operations is presented. Additionally, the data demonstrate that solvents and reagents typically used in oligonucleotide synthesis are robustly cleared by the process and should not require testing in the final product.