Identification of Fmoc-beta-Ala-OH and Fmoc-beta-Ala-amino acid-OH as new impurities in Fmoc-protected amino acid derivatives.

During the manufacture of a proprietary peptide drug substance a new impurity appeared unexpectedly. Investigation of its chemical structure established the impurity as a beta-Ala insertion mutant of the mother peptide. The source of the beta-Ala was identified as contamination of the Fmoc-Ala-OH raw material with Fmoc-beta-Ala-Ala-OH. Further studies also demonstrated the presence of beta-Ala in other Fmoc-amino acids, particularly in Fmoc-Arg(Pbf)-OH. In this case, it was due to the presence of both Fmoc-beta-Ala-OH and Fmoc-beta-Ala-Arg(Pbf)-OH. It is concluded that beta-Ala contamination of Fmoc-amino acid derivatives is a general and hitherto unrecognized problem to suppliers of Fmoc-amino acid derivatives. The beta-Ala is often present as Fmoc-beta-Ala-OH and/or as a dipeptide, Fmoc-beta-Ala-amino acid-OH. In collaboration with the suppliers, new specifications were introduced, recognizing the presence of beta-Ala-related impurities in the raw materials and limiting them to acceptable levels. The implementation of these measures has essentially eliminated beta-Ala contamination as a problem in the manufacture of the drug substance.     

Removal of the fermentation by-product succinyl L-tyrosine from the beta-lactamase inhibitor clavulanic acid using a molecularly imprinted polymer

Clavulanic acid is a beta-lactamase inhibitor used in therapeutic combinations with the penicillin-type antibiotics. During the fermentation leading to clavulanic acid, a succinyl L-tyrosine by-product is unavoidably formed. Occasionally, the amount of this by-product is found to be as high as 2% of the product even after standard purification operations. To further remove this impurity, we prepared a highly specific adsorbent for succinyl L-tyrosine with the molecular imprinting technique. This was performed by simultaneously using vinylbenzyl trimethylammonium chloride and methacrylic acid as the functional monomers. The imprinted polymer selectively bound succinyl L-tyrosine, and could be successfully used to remove this impurity at concentrations of less than 2% in the presence of clavulanic acid.     

A Feasible Approach to Evaluate the Relative Reactivity of NHS-Ester Activated Group with Primary Amine-Derivatized DNA Analogue and Non-Derivatized Impurity

Synthetic DNA analogues with improved stability are widely used in life science. The 3′and/or 5′ equivalent terminuses are often derivatized by attaching an active group for further modification, but a certain amount of non-derivatized impurity often remains. It is important to know to what extent the impurity would influence further modification. The reaction of an NHS ester with primary amine is one of the most widely used options to modify DNA analogues. In this short communication, a 3′-(NH₂-biotin)-derivatized morpholino DNA analogue (MORF) was utilized as the model derivatized DNA analogue. Inclusion of a biotin concomitant with the primary amine at the 3′-terminus allows for the use of streptavidin to discriminate between the products from the derivatized MORF and non-derivatized MORF impurity. To detect the MORF reaction with NHS ester, S-acetyl NHS-MAG₃ was conjugated to the DNA analogue for labeling with ^99mTc, a widely used nuclide in the clinic. It was found that the non-derivatized MORF also reacted with the S-acetyl NHS-MAG₃. Radiolabeling of the product yielded an equally high labeling efficiency. Nevertheless, streptavidin binding indicated that under the conditions of this investigation, the non-derivatized MORF was five times less reactive than the amine-derivatized MORF.     

Kinetic analysis and modeling of the liquid-liquid conversion of emulsified di-rhamnolipids by Naringinase from Penicillium decumbens

The enzymatic conversion of an aggregate-forming substrate was kinetically analyzed and a model was applied for the prediction of reaction-time courses. An L-rhamnose molecule from a di-rhamnolipid is cleaved by Naringinase from Penicillium decumbens leading to a mono-rhamnolipid. Optimal reaction rates were found when both, substrate and product build large co-aggregates in a slightly acidic aqueous phase. On the other hand, reaction rates were independent of initial di-rhamnolipid concentration and this was interpreted by assuming that the reaction occurs in the aqueous phase according to Michaelis-Menten kinetics in combination with competitive L-rhamnose inhibition. Rhamnolipids were therefore assumed to be highly concentrated in aggregates, a second liquid phase, whereas diffusive rhamnolipid transport from and to the aqueous phase occurs due to the enzymatic reaction. Furthermore, ideal surfactant mixing between di- and mono-rhamnolipid was assumed for interpretation of the negative effect of the last on the reaction rate. A model was created that describes the system accordingly. The comparison of the experimental data, were in excellent agreement with the predicted values. The findings of this study may beneficially be adapted for any bioconversion involving aggregate-forming substrate and/or product being catalyzed by hydrophilic enzymes.     

An important side reaction using the thiol, 3,6‐dioxa‐1,8‐octanedithiol (DODT), in 9‐fluorenylmethoxycarbonyl‐based solid phase peptide synthesis

A considerable quantity of an alkylation by‐product is observed when using 3,6‐dioxa‐1,8‐octanedithiol as a scavenger during acidic release of peptides containing the thioether amino acid methionine from the solid support. Adjustment of the cleavage conditions by replacement of 3,6‐dioxa‐1,8‐octanedithiol with ethane dithiol or by using methionine sulfoxide as an alternative to methionine resulted in no such impurity. The by‐product was detectable by liquid chromatography and mass spectrometry and characterised by NMR spectroscopy of an isolated model peptide. It could be effectively removed in a separate post cleavage step by treatment with dilute aqueous acid at 37 °C. Copyright © 2013 European Peptide Society and John Wiley & Sons, Ltd.     

Oxidative decarboxylation of retinoic acid in microsomes of rat liver and kidney

Liver and kidney microsomes have been found to catalyze a rapid decarboxylation of retinoic acid in vitro. The reaction requires NADPH and Fe(2+), and is further stimulated by the presence of pyrophosphate. Thiamine pyrophosphate contained sufficient iron as an impurity to provide strong enhancement of the reaction in the absence of added iron. The decarboxylation could also be shown to occur nonenzymatically in the presence of ascorbate, Fe(2+), and boiled microsomes, but there was little autoxidation resulting in decarboxylation. The reaction was strongly inhibited by chelating agents, N,N'-diphenyl-p-phenylene diamine, phenazine methosulfate, and ferricyanide, and resembled lipid peroxidation in both its cofactor requirements and response to inhibitors. The product of the reaction appeared to lack only the C-15 of the original retinoic acid molecule. It was not retained by diethylaminoethyl cellulose, was more polar than retinoic acid upon silicic acid chromatography, had a lower UV absorption maximum (295 m micro ) than the starting product, and seemed to have an aldehyde group at C-14. The physiological significance of the decarboxylation remains to be assessed, but its rapidity makes it important to in vitro work on retinoic acid.     

Optimization of ultrafiltration/diafiltration processes for partially bound impurities

Ultrafiltration and diafiltration processes are used extensively for removal of a variety of small impurities from biological products. There has, however, been no experimental or theoretical analysis of the effects of impurity- product binding on the rate of impurity removal during these processes. Model calculations were performed to account for the effects of equilibrium binding between a small impurity and a large (retained) product on impurity clearance. Experiments were performed using D-tryptophan and bovine serum albumin as a model system. The results clearly demonstrate that binding interactions can dramatically reduce the rate of small impurity removal, leading to large increases in the required number of diavolumes. The optimal product concentration for performing the diafiltration shifts to lower product concentrations in the presence of strong binding interactions. Approximate analytical expressions for the impurity removal were developed which can provide a guide for the design and optimization of industrial ultrafiltration/diafiltration processes.     

Microbial deracemisation of aromatic β-hydroxy acid esters

Aromatic β-hydroxy acid esters were found to undergo deracemisation using whole cells of Candida parapsilosis. The conditions for the deracemisation reaction were optimised where 75% isolated yield and >95% enantiomeric excess of the product was achieved. The effect of electron donating as well as electron withdrawing groups present in the standard substrate, ethyl 3-hydroxy 3-phenyl propionate was studied to establish the generality of the reaction. The enantiomeric excess of the product remains high (>95%) irrespective of the different substituents in the para position but substitution at the ortho position obstructs the process. Similarly, ethyl and methyl esters of the standard substrate undergo deracemisation reaction giving high ee of the product, but the benzyl ester of the standard substrate did not undergo deracemisation.     

Affinity ultrafiltration: effects of ligand binding on selectivity and process optimization.

The effective design of affinity ultrafiltration processes using a selective macroligand requires a detailed understanding of the effects of ligand-binding interactions on product yield and purification. Theoretical calculations were performed to evaluate the performance of affinity diafiltration separations with both competitive and independent binding interactions for the product and impurity. The intrinsic selectivity for independent binding decreased during the diafiltration due to the increase in fractional impurity binding as the impurity is selectively removed. The opposite behavior was seen for competitive binding because the strongly bound product displaces the impurity from the binding sites. Purification-yield diagrams were used to examine the effects of affinity-ligand concentration and binding constants on the separation. Model calculations were in excellent agreement with experimental data for the separation of tryptophan isomers using bovine serum albumin as the steroselective macroligand. Simulations with a fixed number of diavolumes show a clear optimum in product yield and purification factor at an intermediate ligand concentration due to the competing effects of the intrinsic selectivity and the rate of impurity removal. These results provide an appropriate framework for the design and optimization of affinity ultrafiltration systems.     

Integrated reactor concepts for the enzymatic kinetic synthesis of cephalexin

Integrated process concepts for enzymatic cephalexin synthesis were investigated by our group, and this article focuses on the integration of reactions and product removal during the reactions. The last step in cephalexin production is the enzymatic kinetic coupling of activated phenylglycine (phenylglycine amide or phenylglycine methyl ester) and 7-aminodeacetoxycephalosporanic acid (7-ADCA). The traditional production of 7-ADCA takes place via a chemical ring expansion step and an enzymatic hydrolysis step starting from penicillin G. However, 7-ADCA can also be produced by the enzymatic hydrolysis of adipyl-7-ADCA. In this work, this reaction was combined with the enzymatic synthesis reaction and performed simultaneously (i.e., one-pot synthesis). Furthermore, in situ product removal by adsorption and complexation were investigated as means of preventing enzymatic hydrolysis of cephalexin. We found that adipyl-7-ADCA hydrolysis and cephalexin synthesis could be performed simultaneously. The maximum yield on conversion (reaction) of the combined process was very similar to the yield of the separate processes performed under the same reaction conditions with the enzyme concentrations adjusted correctly. This implied that the number of reaction steps in the cephalexin process could be reduced significantly. The removal of cephalexin by adsorption was not specific enough to be applied in situ. The adsorbents also bound the substrates and therewith caused lower yields. Complexation with beta-naphthol proved to be an effective removal technique; however, it also showed a drawback in that the activity of the cephalexin-synthesizing enzyme was influenced negatively. Complexation with beta-naphthol rendered a 50% higher cephalexin yield and considerably less byproduct formation (reduction of 40%) as compared to cephalexin synthesis only. If adipyl-7-ADCA hydrolysis and cephalexin synthesis were performed simultaneously and in combination with complexation with beta-naphthol, higher cephalexin concentrations also were found. In conclusion, a highly integrated process (two reactions simultaneously combined with in situ product removal) was shown possible, although further optimization is necessary.     

Reactivity of old yellow enzyme with alpha-NADPH and other pyridine nucleotide derivatives

The reaction of Old Yellow Enzyme (OYE) with pyridine nucleotides has been examined using steady state kinetics, rapid reaction kinetics, and equilibrium binding. alpha-NADPH, beta-NADPH, and the acid breakdown products of NADPH all bind to oxidized OYE with dissociation constants below 1 microM. These complexes produce characteristic red shifts in the absorption spectrum of OYE. A similar red shift which occurs after multiple turnovers of OYE with NADPH has been found to be due to an impurity in the NADPH preparation, possibly an acid breakdown product. Anions such as chloride, acetate, azide, and phenolates compete with the pyridine nucleotides for binding to a common site in oxidized OYE. Anaerobic reduction of OYE by NADPH proceeds via two intermediates to establish a readily reversible equilibrium. In contrast to most other NADPH-dependent enzymes, both alpha- and beta-NADPH are capable of reducing OYE, and alpha-NADPH is more effective. Using beta-[4(R)-2H]NADPH, a primary deuterium isotope effect was observed in the reduction reaction. Results from rapid reaction and steady state studies showed that reduction of OYE was rate limiting in turnover. Consistent with this, the turnover number with alpha-NADPH was significantly higher than that with beta-NADPH.     

Improving Product Specificity of Whole‐Cell Alkane Oxidation in Nonconventional Media: A Multivariate Analysis Approach

Two‐liquid‐phase reaction media have long been used in bioconversions to supply or remove hydrophobic organic reaction substrates and products to reduce inhibitory and toxic effects on biocatalysts. In case of the terminal oxyfunctionalization of linear alkanes by the AlkBGT monooxygenase the excess alkane substrate is often used as a second phase to extract the alcohol, aldehyde, and acid products. However, the selection of other carrier phases or surfactants is complex due to a large number of parameters that are involved, such as biocompatibility, substrate bioavailability, and product extraction selectivity. This study combines systematic high‐throughput screening with chemometrics to correlate physicochemical parameters of a range of cosolvents to product specificity and yield using a multivariate regression model. Partial least‐squares regression shows that the defining factor for product specificity is the solubility properties of the reaction substrate and product in the cosolvent, as measured by Hansen solubility parameters. Thus the polarity of cosolvents determines the accumulation of either alcohol or acid products. Whereas usually the acid product accumulates during the reaction, by choosing a more polar cosolvent the 1‐alcohol product can be accumulated. Especially with Tergitol as a cosolvent, a 3.2‐fold improvement in the 1‐octanol yield to 18.3 mmol L^?1 is achieved relative to the control reaction without cosolvents.     

An impurity characterization based approach for the rapid development of integrated downstream purification processes

In this study, we describe a new approach for the characterization of process‐related impurities along with an in silico tool to generate orthogonal, integrated downstream purification processes for biological products. A one‐time characterization of process‐related impurities from product expression in Pichia pastoris was first carried out using linear salt and pH gradients on a library of multimodal, salt‐tolerant, and hydrophobic charge induction chromatographic resins. The Reversed‐phase ultra‐performance liquid chromatography (UPLC) analysis of the fractions from these gradients was then used to generate large data sets of impurity profiles. A retention database of the biological product was also generated using the same linear salt and pH gradients on these resins, without fraction collection. The resulting two data sets were then analyzed using an in silico tool, which incorporated integrated manufacturing constraints to generate and rank potential three‐step purification sequences based on their predicted purification performance as well as whole‐process “orthogonality” for impurity removal. Highly ranked sequences were further examined to identify templates for process development. The efficacy of this approach was successfully demonstrated for the rapid development of robust integrated processes for human growth hormone and granulocyte‐colony stimulating factor.     

Studies on the reaction of D-amino acid oxidase with beta-cyano-D-alanine. Observation of an intermediary stable charge transfer complex

The reaction of D-amino acid oxidase [EC 1.4.3.3] (DAO) from porcine kidney with beta-cyano-D-alanine (D-BCNA) was studied. DAO was found to catalyze elimination of the cyano group as well as oxidation of D-BCNA. During the course of the reaction in the presence of excess oxygen, an intermediate was observed which exhibited a characteristic absorption spectrum with a broad charge transfer band in the longer wavelength region. The CD spectrum of this intermediate resembles that of DAO-anthranilate complex. The rate of oxygen consumption in the aerobic reaction decreased with time, suggesting product inhibition due to complex formation between the enzyme and the product. Anaerobic addition of D-BCNA reduced the enzyme to its fully reduced state, the CD spectrum of which closely resembles that of the enzyme reduced by excess D-alanine. When an appropriate amount of D-BCNA was added to the enzyme under air, the charge transfer complex was observed immediately, and underwent a change to the reduced state as the oxygen was consumed. The binding strength in the charge transfer complex was found to be comparable to that in DAO-benzoate complex. The accumulating product in the oxidation of D-BCNA had a strong absorption at 285 nm. The aerobic reaction of beta-cyano-L-alanine (L-BCNA) with snake venom L-amino acid oxidase (LAO) produced the same product with an absorption at 285 nm as the reaction of DAO with D-BCNA. The product obtained in the reaction with LAO was found to form the same charge transfer complex with DAO. We tentatively identified this product as alpha-amino-beta-cyanoacrylate and the charge transfer complex as the complex of alpha-amino-alpha-cyanoacrylate with the oxidized enzyme. A hypothetical reaction pathway based on the present finding is proposed. Addition of L-BCNA to the enzyme produced an absorption spectrum very similar to that of the DAO-benzoate complex without oxidation or elimination. L-BCNA was found to be a competitive inhibitor of the oxidation of D-alanine.     

A mass spectrometric technique for detecting and identifying by-products in the synthesis of peptides

The utility of a new mass spectrometric technique for detecting and identifying peptide by-products produced in the synthesis of peptides is demonstrated. The technique involves three sequential steps: (1) practically nondestructive 252Cf plasma desorption mass spectrometric analysis of monolayer amounts of the peptide(s) of interest bound to a thin layer of nitrocellulose; (2) enzyme-catalyzed microscale chemical reaction of the surface-bound peptide(s) to produce structurally informative hydrolysis products; (3) plasma desorption mass spectrometric analysis of these hydrolysis products. The first step determines the presence and the molecular weights of unwanted by-products resulting from errors or incomplete reactions during synthesis. The subsequent two steps provide information on the precise location in the peptides where errors have occurred. In the present paper, the technique is applied to an investigation of unwanted peptide by-products associated with the use of tryptophan during stepwise solid-phase peptide synthesis. Synthetic preparations of melittin and [Bpa-8]dynorphin A (1-17) were each found to contain a major impurity with molecular weight 28 Da higher than that of the desired product. The impurity in the melittin preparation, in which the final deprotection step involved the high-low HF procedure, was shown to result from incomplete removal of the formyl group from Trp-19. On the other hand, the impurity in the [Bpa-8]dynorphin A (1-17) preparation, where the removal of the formyl group from Trp-14 was carried out using piperidine, was shown to result from migration of the formyl group to Lys-11 or Lys-13.(ABSTRACT TRUNCATED AT 250 WORDS)     

Fmoc-2-mercaptobenzothiazole, for the introduction of the Fmoc moiety free of side-reactions

A double side-reaction, consisting in the formation of Fmoc-beta-Ala-OH and Fmoc-beta-Ala-AA-OH, during the preparation of Fmoc protected amino acids (Fmoc-AA-OH) with Fmoc-OSu is discussed. Furthermore, the new Fmoc-2-MBT reagent is proposed for avoiding these side-reactions as well as the formation of the Fmoc-dipeptides (Fmoc-AA-AA-OH) and even tripeptides, which is another important side-reaction when chloroformates such as Fmoc-Cl is used for the protection of the alpha-amino function of the amino acids.     

Modeling and kinetic analysis of the reaction system using whole cells with separately and co-expressed D-hydantoinase and N-carbamoylase

We developed a kinetic model that describes a heterogeneous reaction system for the production of D-p-hydroxyphenylglycine from D,L-p-hydroxyphenyl-hydantoin using D-hydantoinase of Bacillus stearothermophilus SD1 and N-carbamoylase of Agrobacterium tumefaciens NRRL B11291. As a biocatalyst, whole cells with separately or co-expressed enzymes were used. The reaction system involves dissolution of substrate particles, enzymatic conversion, racemization of the L-form substrate, and transfer of the dissolved substrate, intermediate, and product through the cell membrane. Because the two enzymes have different pH optimum, kinetic parameters were evaluated at different pH for the reaction systems. The model was simulated using the kinetic parameters and compared with experimental data, and it was found that the kinetic model well describes the behavior of the reaction systems using whole cells with separately and co-expressed enzymes. Factors affecting the kinetics of the reaction systems were analyzed on the basis of the kinetic model. In the reaction system with separately expressed enzymes, racemization rate and transport of the reaction intermediate (N-carbamoyl-D-p-hydroxyphenylglycine) were revealed to be the limiting factors at neutral pH, resulting in accumulation of intermediate in the reaction medium. At alkaline condition, on the other hand, inhibition of N-carbamoylase by ammonia was severe, and thereby the reaction rate significantly reduced. In the co-expressed enzyme system, accumulation of intermediate was negligible in the reaction medium, and the improved performance was observed compared to that with separately expressed enzymes. The present model might be applied for the optimization and development of the reaction system using two sequential enzymes.     

Discovery,characterization, and remediation of a C-terminal Fc-extension in proteins expressed in CHO cells

ABSTRACT

Protein-based biotherapeutics are produced in engineered cells through complex processes and may contain a wide variety of variants and post-translational modifications that must be monitored or controlled to ensure product quality. Recently, a low level (~1–5%) impurity was observed in a number of proteins derived from stably transfected Chinese hamster ovary (CHO) cells using mass spectrometry. These molecules include antibodies and Fc fusion proteins where Fc is on the C-terminus of the construct. By liquid chromatography-mass spectrometry (LC-MS), the impurity was found to be ~1177 Da larger than the expected mass. After tryptic digestion and analysis by LC-MS/MS, the impurity was localized to the C-terminus of Fc in the form of an Fc sequence extension. Targeted higher-energy collision dissociation was performed using various normalized collision energies (NCE) on two charge states of the extended peptide, resulting in nearly complete fragment ion coverage. The amino acid sequence, SLSLSPEAEAASASELFQ, obtained by the de novo sequencing effort matches a portion of the vector sequence used in the transfection of the CHO cells, specifically in the promoter region of the selection cassette downstream of the protein coding sequence. The modification was the result of an unexpected splicing event, caused by the resemblance of the commonly used GGU codon of the C-terminal glycine to a consensus splicing donor. Three alternative codons for glycine were tested to alleviate the modification, and all were found to completely eliminate the undesirable C-terminal extension, thus improving product quality.     

Interaction of anticancer drug cisplatin with guanine: density functional theory and surface-enhanced Raman spectroscopy study

Surface-enhanced Raman spectroscopy (SERS) in a silver sol assisted by density functional theory (DFT) calculations is shown to be a promising tool in the characterization of platinum complexes and their interaction with nucleic acid bases. This is demonstrated using cisplatin and guanine as a model. The energies and geometric parameters of cisplatin, guanine, and their reaction products are calculated at Becke's nonlocal three parameter exchange and correlation functional and the Lee-Yang-Parr correlation functional level using the 6-31++G(d,p) basis set on the light elements and the effective core potential by Hay and Wadt on platinum. Available X-ray crystallography data are mostly in agreement with predictions within the experimental precision level, although Pt-N bond lengths tend to be systematically overestimated. The normal Raman spectrum of cisplatin is assigned. The SERS spectra of cisplatin and its reaction product with guanine are measured from 10(-6) M aqueous solution. The observed spectral changes in the SERS spectrum of guanine upon cisplatin binding are modeled by DFT calculations. The best agreement between theory and experiment is achieved when the adsorbed reaction product is assumed to be the 1:1 adduct cis-Pt(NH3)2ClG in which Pt is bound to N7 and guanine is deprotonated at N9.     

Kinetic modeling of lipase‐catalyzed esterification reaction between oleic acid and trimethylolpropane: A simplified model for multi‐substrate multi‐product ping–pong mechanisms

Kinetic models are among the tools that can be used for optimization of biocatalytic reactions as well as for facilitating process design and upscaling in order to improve productivity and economy of these processes. Mechanism pathways for multi‐substrate multi‐product enzyme‐catalyzed reactions can become very complex and lead to kinetic models comprising several tens of terms. Hence the models comprise too many parameters, which are in general highly correlated and their estimations are often prone to huge errors. In this study, Novozym^®435 catalyzed esterification reaction between oleic acid (OA) and trimethylolpropane (TMP) with continuous removal of side‐product (water) was carried out as an example for reactions that follow multi‐substrate multi‐product ping‐pong mechanisms. A kinetic model was developed based on a simplified ping‐pong mechanism proposed for the reaction. The model considered both enzymatic and spontaneous reactions involved and also the effect of product removal during the reaction. The kinetic model parameters were estimated using nonlinear curve fitting through unconstrained optimization methodology and the model was verified by using empirical data from different experiments and showed good predictability of the reaction under different conditions. This approach can be applied to similar biocatalytic processes to facilitate their optimization and design. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1422–1429, 2013