Determination of linearized pDNA template in mRNA production process using HPLC.

The recent clinical success of messenger RNA (mRNA) technology in managing the Covid pandemic has triggered an unprecedented innovation in production and analytical technologies for this therapeutic modality. mRNA is produced by enzymatic transcription of plasmid DNA (pDNA) using polymerase in a cell-free process of in vitro transcription. After transcription, the pDNA is considered a process-related impurity and is removed from the mRNA product enzymatically, chromatographically, or by precipitation. Regulatory requirements are currently set at 10 ng of template pDNA per single human dose, which typically ranges between 30 and 100 µg. Here, we report the development of a generic procedure based on enzymatic digestion and chromatographic separation for the determination of residual pDNA in mRNA samples, with a limit of quantification of 2.3 ng and a limit of detection of less than 0.1 ng. The procedure is based on enzymatic degradation of mRNA and anion exchange HPLC separation, followed by quantification of residual pDNA with a chromatographic method that is already widely adopted for pDNA quality analytics. The procedure has been successfully applied for in-process monitoring of three model mRNAs and a self-amplifying RNA (saRNA) and can be considered a generic substitution for qPCR in mRNA in-process control analytical strategy, with added benefits that it is more cost-efficient, faster, and sequence agnostic.

Selective hydrophobic interaction chromatography for high purity of supercoiled DNA plasmids.

High purity of plasmid DNA (pDNA), particularly in supercoiled isoform (SC), is used for various biopharmaceutical applications, such as a transfecting agent for production of gene therapy viral vectors, for pDNA vaccines, or as a precursor for linearized form that serves as a template for mRNA synthesis. In clinical manufacturing, pDNA is commonly extracted from Escherichia coli cells with alkaline lysis followed by anion exchange chromatography or tangential flow filtration as a capture step for pDNA. Both methods remove a high degree of host cell contaminants but are unable to generically discriminate between SC and open-circular (OC) pDNA isoforms, as well as other DNA impurities, such as genomic DNA (gDNA). Hydrophobic interaction chromatography (HIC) is commonly used as polishing purification for pDNA. We developed HIC-based polishing purification methodology that is highly selective for enrichment of SC pDNA. It is generic with respect to plasmid size, scalable, and GMP compatible. The technique uses ammonium sulfate, a kosmotropic salt, at a concentration selective for SC pDNA binding to a butyl monolith column, while OC pDNA and gDNA are removed in flow-through. The approach is validated on multiple adeno-associated virus- and mRNA-encoding plasmids ranging from 3 to 12 kbp. We show good scalability to at least 300 mg of >95% SC pDNA, thus paving the way to increase the quality of genomic medicines that utilize pDNA as a key raw material.

Bridging upstream and downstream for improved adenovirus 5 bioprocess.

Adenoviruses are well-known viral vectors that have been previously used in gene therapy and as a vaccine-delivery vehicle for humans and animals. During the COVID-19 pandemic, it gained renewed attention, but at the same time, it raised concerns due to side effects observed with some of the resulting vaccines administered to patients. It has been indicated that these side effects might be attributed to impurities present in the final product. Therefore, constant enhancement of the vaccine purity and further improvement of impurity detection methods are needed. In this work, we showcase an example of industry-relevant adenovirus bioprocess optimization. Our data show the effect of upstream parameters on the bioburden introduced to the downstream process. We provide an example of process optimization using a combination of the PATfix analytical method, ddPCR, infectivity, total DNA, and total protein analyses to optimize cell density, multiplicity of infection, and length of production. Additionally, we provide data illustrating the robustness of the convective interaction media quaternary amine monolithic chromatography step. This anion exchange strategy was shown to remove over 99% of protein and DNA impurities, including those unable to be addressed by tangential flow filtration, while maintaining high adenovirus recoveries.

Scalable multimodal weak anion exchange chromatographic purification for stable mRNA drug substance.

Messenger RNA (mRNA) has emerged as a modality with immense therapeutic potential. Recent innovations in production process of mRNA call for procedures to isolate pure mRNA drug substance (DS) with high yield, high capacity, scalability, and compatibility with GMP production systems. Novel RNA modalities, such as circular RNA (circRNA), have further driven the need for non-affinity capture possibilities which are already widely used in the biopharmaceutical industry, for example, in monoclonal antibody processing. The principle that multimodal ion exchange/hydrogen bonding chromatography can be used to separate mRNA from in vitro transcription components has recently been demonstrated. Here, we apply and refine this approach to be suitable for scalable purification of multiple mRNA constructs with sufficient yields, purity, and stability, for use in mRNA production process. Binding capacity of the PrimaS-modified monolithic chromatographic column for mRNA enabled up to 7 mg/mL product isolation in a single chromatographic run, with 98% recovery and room temperature stability of the eGFP mRNA demonstrated for up to 28 days. This approach is independent of construct size or the presence of polyadenylic acid tail and is applicable for capture of a wide variety of RNAs, including mRNA, self-amplifying RNA, circRNA, and with optimization also smaller RNAs such as transfer RNA and others.

High Recovery Chromatographic Purification of mRNA at Room Temperature and Neutral pH.

Messenger RNA (mRNA) is becoming an increasingly important therapeutic modality due to its potential for fast development and platform production. New emerging RNA modalities, such as circular RNA, drive the need for the development of non-affinity purification approaches. Recently, the highly efficient chromatographic purification of mRNA was demonstrated with multimodal monolithic chromatography media (CIM® PrimaS), where efficient mRNA elution was achieved with an ascending pH gradient approach at pH 10.5. Here, we report that a newly developed chromatographic material enables the elution of mRNA at neutral pH and room temperature. This material demonstrates weak anion-exchanging properties and an isoelectric point of 5.3. It enables the baseline separation of mRNA (at least up to 10,000 nucleotides (nt) in size) from parental plasmid DNA (regardless of isoform composition) with both a NaCl gradient and ascending pH gradient approach, while mRNA elution is achieved in a pH range of 5-7. In addition, the basic structure of the novel material is a chromatographic monolith, enabling convection-assisted mass transfer of large RNA molecules to and from the active surface. This facilitates the elution of mRNA in 3-7 column volumes with more than 80% elution recovery and uncompromised integrity. This is demonstrated by the purification of a model mRNA (size 995 nt) from an in vitro transcription reaction mixture. The purified mRNA is stable for at least 34 days, stored in purified H2O at room temperature.

Preferential exclusion chromatography as a capture step for extracellular AAV harvest from adherent and suspension productions.

Preferential exclusion chromatography (PXC) sometimes described as hydrophobic interaction chromatography is a well-known, but not widely used technique for purification of Adeno-associated viruses. It employs high molarity of preferentially excluded cosolvent (salt in our case). The downside of this method is that high molarity of salt can lead to aggregation and precipitation of different compounds from the sample. In the case of viruses that are excreted to medium, the concentration of impurities is much lower compared to cell lysates, and PXC can be used as a first chromatographic, serotype independent step to concentrate and purify adeno-associated virus (AAV). Here, we explored PXC for adherent and suspension harvests using monolithic chromatographic columns (CIMmultus). Suspension extracellular adeno-associated virus, serotype 9 (AAV9) harvest had more impurities compared to adherent harvest, therefore it required higher input regarding method development. Final conditions for suspension harvest included higher molarity of binding salt and using more open channel format of chromatographic column (6 µm channel size). Vector genome analysis with droplet digital polymerase chain reaction (ddPCR) revealed 84% and 97% recovery for suspension and adherent AAV9 harvest, respectively. After PXC capture step, adherent AAV9 was purified by already described ion exchange techniques. Overall process vector genome recovery, from clarified harvest to anion exchange elution fraction, was 54% measured by ddPCR. Residual host cell DNA was measured at 40 ng per 1E13 vector genome, and empty AAV was below 5% in final anion exchange chromatography fraction.

Optimization of rAAV capture step purification using SO3 monolith chromatography.

Adeno-associated virus (AAV) vectors are crucial tools for gene therapy applications. As AAVs are administered in vivo, stringent purity requirements must be met, necessitating the development of various downstream processing strategies in accordance with regulatory guidelines. In this context, we focus on the non-affinity serotype-independent recombinant AAV (rAAV) capture step, which involves the use of Convective Interaction Media (CIM) cation-exchange SO3 monoliths. We analyzed differentially pretreated viral samples obtained from the Sf9 cell line and applied these samples to the capture SO3 chromatography step. We conducted screening experiments using CIM SO3 0.05 mL monolithic 96-well plates with buffers of varying pH, sodium chloride concentrations, and the inclusion of poloxamer 188, aiming to select the optimal binding mobile phase. Dynamic binding capacity was defined for different pretreatments and the optimal conditions were subsequently retested using the industrial purification CIMmultus line. The results demonstrated a high overall vector recovery (51%) and a significant reduction in impurities (99.98% for protein reduction and 99.25% for DNA reduction) using the selected capture step parameters, thereby confirming the successful optimization of the rAAV capture step in the downstream process using monoliths.

Effect of plasmid DNA isoforms on preparative anion exchange chromatography.

Increased need for plasmid DNA (pDNA) with sizes above 10 kbp (large pDNA) in gene therapy and vaccination brings the need for its large-scale production with high purity. Chromatographic purification of large pDNA is often challenging due to low process yields and column clogging, especially using anion-exchanging columns. The goal of our investigation was to evaluate the mass balance and pDNA isoform composition at column outlet for plasmids of different sizes in combination with weak anion exchange (AEX) monolith columns of varying channel size (2, 3 and 6 µm channel size). We have proven that open circular pDNA (OC pDNA) isoform is an important driver of reduced chromatographic performance in AEX chromatography. The main reason for the behaviour is the entrapment of OC pDNA in chromatographic supports with smaller channel sizes. Entrapment of individual isoforms was characterised for porous beads and convective monolithic columns. Convective entrapment of OC pDNA isoform was confirmed on both types of stationary phases. Porous beads in addition showed a reduced recovery of supercoiled pDNA (on an 11.6 kbp plasmid) caused by diffusional entrapment within the porous structure. Use of convective AEX monoliths or membranes with channel diameter >3.5 µm has been shown to increase yields and prevent irreversible pressure build-up and column clogging during purification of plasmids at least up to 16 kbp in size.

Analytical separation of plasmid DNA isoforms using anion exchanging chromatographic monoliths with 6 µm channels.

High-performance liquid chromatography (HPLC)-based analytical assays are used to effectively monitor purity and quantity of plasmid DNA (pDNA) throughout the purification process. However, the phenomenon of physical entrapment of open circular (OC) isoforms pDNA inside narrow channels of chromatographic support decreases its accuracy and precision and the effect increases with pDNA size. The purpose of the study was to develop a chromatographic method for accurate analytical separation between isoforms of <16 kbp pDNA using weak anion exchanging monolithic column with large (6 µm) convective channels. Purified samples of 4.7 and 15.4 kbp large pDNA with known isoform composition were prepared and their isoforms separated in ascending salt gradient. Both OC and supercoiled (SC) isoforms were baseline separated at a flow rate below 0.5 mL min-1 in a guanidinium chloride (GdnCl) gradient with a ≥95% OC pDNA elution recovery. However, these chromatographic conditions increased 2 times the peak width for linear (LIN) pDNA isoform compared to the results using monoliths with 1.4 µm channel size. If other chaotropic agents, such as urea or thiocyanate (SCN), were added to Gdn ions, the elution volume for LIN isoform decreased. Optimization of combined GdnCl/GdnSCN gradient for pDNA elution resulted in a simple and robust chromatographic method, where OC-LIN and LIN-SC pDNA (up to 15 kbp size) were separated with resolution above 1.0 and above 2.0, respectively. The accessibility and general acceptance of anion exchange chromatography for pDNA analytics give the newly developed method a great potential for in-process control monitoring of pDNA production processes.

Comparative analysis of transferrin and IgG N-glycosylation in two human populations.

Human plasma transferrin (Tf) N-glycosylation has been mostly studied as a marker for congenital disorders of glycosylation, alcohol abuse, and hepatocellular carcinoma. However, inter-individual variability of Tf N-glycosylation is not known, mainly due to technical limitations of Tf isolation in large-scale studies. Here, we present a highly specific robust high-throughput approach for Tf purification from human blood plasma and detailed characterization of Tf N-glycosylation on the level of released glycans by ultra-high-performance liquid chromatography based on hydrophilic interactions and fluorescence detection (HILIC-UHPLC-FLD), exoglycosidase sequencing, and matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOF-MS). We perform a large-scale comparative study of Tf and immunoglobulin G (IgG) N-glycosylation analysis in two human populations and demonstrate that Tf N-glycosylation is associated with age and sex, along with multiple biochemical and physiological traits. Observed association patterns differ compared to the IgG N-glycome corroborating tissue-specific N-glycosylation and specific N-glycans' role in their distinct physiological functions.

CIM monolithic chromatography as a useful tool for endotoxin reduction and purification of bacteriophage particles supported with PAT analytics.

Bacteriophages represent immense potential as therapeutic agents. Many of the most compelling applications of bacteriophages involve human therapy, some pertinent to gene therapy, others involving antibiotic replacement. Phages themselves are considered safe for humans. However, phage lysates may contain many kinds of harmful by-products, especially endotoxins of gram-negative bacteria and protein toxins produced by many pathogenic bacterial species. In bacteriophage research and therapy, most applications ask for highly purified phage suspensions, as such it is crucial to reduce proteins, endotoxins, DNA and other contaminants. In this article we present an efficient two-step chromatographic purification method for P. aeruginosa bacteriophage PP-01, using Convective Interaction Media (CIM®) monoliths, that is cGMP compliant and easy to scale-up for most stringent production of the therapeutic phage. First chromatographic step on CIMmultus OH resulted in 100% bacteriophage recovery with a reduction of 98 % protein and more than 99 % DNA content. Polishing was conducted using three different column options, CIMmultus with QA, H-Bond and PrimaS ligands. For PP-01 bacteriophage all three different options worked, but multimodal ligands H-Bond and PrimaS outperformed traditional QA in endotoxin removal (7 log step reduction). Additionally, an HPLC analytical method was developed to estimate phage concentration and impurity profile in different in-process samples. The HPLC method shows good correlation with drop assay titration, provides useful insights and can be run very fast with just 20 min per sample analysis.

High-throughput immunoaffinity enrichment and N-glycan analysis of human plasma haptoglobin.

Haptoglobin (Hp) is a positive acute phase protein, synthesized in the liver, with four N-glycosylation sites carrying mainly complex type N-glycans. Its glycosylation is altered in different types of diseases but still has not been extensively studied mainly due to analytical challenges, especially the lack of a fast, efficient, and robust high-throughput Hp isolation procedure. Here, we describe the development of a high-throughput method for Hp enrichment from human plasma, based on monolithic chromatographic support in immunoaffinity mode and downstream Hp N-glycome analysis by hydrophilic interaction ultrahigh-performance liquid chromatography with fluorescent detection (HILIC-UHPLC-FLR). Chromatographic monolithic supports in a 96-well format enable fast, efficient, and robust Hp enrichment directly from diluted plasma samples. The N-glycome analysis demonstrated that a degree of Hp deglycosylation differs depending on the conditions used for N-glycan release and on the specific glycosylation site, with Asn 241 being the most resistant to deglycosylation under tested conditions. HILIC-UHPLC-FLR analysis enables robust quantification of 28 individual chromatographic peaks, in which N-glycan compositions were determined by UHPLC coupled to electrospray ionization quadrupole time of flight mass spectrometry. The developed analytical approach enables fast evaluation of total Hp N-glycosylation and is applicable in large-scale studies.

Increasing yield of in vitro transcription reaction with at-line high pressure liquid chromatography monitoring.

The COVID-19 pandemic triggered an unprecedented rate of development of messenger ribonucleic acid (mRNA) vaccines, which are produced by in vitro transcription reactions. The latter has been the focus of intense development to increase productivity and decrease cost. Optimization of in vitro transcription (IVT) depends on understanding the impact of individual reagents on the kinetics of mRNA production and the consumption of building blocks, which is hampered by slow, low-throughput, end-point analytics. We implemented a workflow based on rapid at-line high pressure liquid chromatography (HPLC) monitoring of consumption of nucleoside triphosphates (NTPs) with concomitant production of mRNA, with a sub-3 min read-out, allowing for adjustment of IVT reaction parameters with minimal time lag. IVT was converted to fed-batch resulting in doubling the reaction yield compared to batch IVT protocol, reaching 10 mg/ml for multiple constructs. When coupled with exonuclease digestion, HPLC analytics for quantification of mRNA was extended to monitoring capping efficiency of produced mRNA. When HPLC monitoring was applied to production of an anti-reverse cap analog (ARCA)-capped mRNA construct, which requires an approximate 4:1 ARCA:guanidine triphosphate ratio, the optimized fed-batch approach achieved productivity of 9 mg/ml with 79% capping. The study provides a methodological platform for optimization of factors influencing IVT reactions, converting the reaction from batch to fed-batch mode, determining reaction kinetics, which are critical for optimization of continuous addition of reagents, thus in principle enabling continuous manufacturing of mRNA.

Sample displacement chromatography of monoclonal antibody charge variants and aggregates.

The rise of biosimilar monoclonal antibodies has renewed the interest in monoclonal antibody (mAb) charge variants composition and separation. The sample displacement chromatography (SDC) has the potential to overcome the low separation efficiency and productivity associated with bind-elute separation of mAb charge variants. SDC in combination with weak cation exchanging macroporous monolithic chromatographic column was successfully implemented for a separation of charge variants and aggregates of monoclonal IgG under overloading conditions. The charge variants composition was at-line monitored by a newly developed, simple and fast analytical method, based on weak cation exchange chromatography. It was proven that basic charge variants acted as displacers of IgG molecules with lower pI, when the loading was performed 1 to 1.5 pH unit below the pI of acidic charge variants. The efficiency of the SDC process is flow rate independent due to a convection-based mass transfer on the macroporous monolith. The productivity of the process at optimal conditions is 35 mg of purified IgG fraction per milliliters of monolithic support with 75-80% recovery. As such, an SDC approach surpasses the standard bind-elute separation in the productivity for a factor of 3, when performed on the same column. The applicability of the SDC approach was confirmed for porous particle-based column as well, but with 1.5 lower productivity compared to the monoliths.

Guanidine improves DEAE anion exchange-based analytical separation of plasmid DNA.

Elution of strong and weak anion exchangers with sodium chloride gradients is commonly employed for analysis of sample mixtures containing different isomers of plasmid DNA. Gradient elution of a weak anion exchanger (diethylaminoethyl) in the presence of guanidine hydrochloride (Gdn) roughly doubles resolution between open-circular (oc) and supercoiled (sc) isomers. It also improves resolution among sc, linear, and multimeric/aggregated forms. Sharper elution peaks with less tailing increase sensitivity about 30%. However, elution with an exclusively Gdn gradient to 900 mM causes more than 10% loss of plasmid. Elution with a sodium chloride gradient while maintaining Gdn at a level concentration of 300 mM achieves close to 100% recovery of sc plasmid while maintaining the separation improvements achieved by exclusively Gdn elution. Corresponding improvements in separation performance are not observed on a strong (quaternary amine) anion exchanger. Other chaotropic salts do not produce a favorable result on either exchanger, nor does the inclusion of surfactants or EDTA. Selectivity of the diethylaminoethyl-Gdn method is orthogonal to electrophoresis, but with better quantification than agarose electrophoresis, better quantitative accuracy than CE, and resolution approaching CE.

Removal of empty capsids from adeno-associated virus preparations by multimodal metal affinity chromatography.

Separation of empty and full adeno-associated virus capsids by multimodal metal affinity chromatography was investigated using a positively charged metal affinity ligand. A subpopulation of empty capsids eluted first, followed by full capsids, and later by more empty capsids and debris. Empty and full capsid composition of chromatography fractions was evaluated by cesium chloride density gradient centrifugation followed by stratigraphic flow analysis of the centrifuge tube contents, monitored by intrinsic fluorescence. Columns charged with barium, calcium, magnesium, zinc, manganese, and ferric ions gave similar results with respect to capsid separation. Charging with cupric ions maintained resolution between early-eluting empty capsids and full capsids but caused them to elute at lower conductivity. Empty and full capsids were fractionated with Tris-borate gradients, sodium chloride gradients, and magnesium chloride gradients. Recovery of full serotype 9 capsids was 100% with complete elimination of empty capsids. All metal ions bound contaminant subsets that required sodium hydroxide for removal. Columns charged with ferric iron and manganese bound more contaminants than all other metals. Columns charged with calcium, magnesium, barium, and copper bound the least. Contaminant binding on zinc-charged columns was intermediate between the two groups.

Multiple-Monitor HPLC Assays for Rapid Process Development, In-Process Monitoring, and Validation of AAV Production and Purification.

HPLC is established as a fast convenient analytical technology for characterizing the content of empty and full capsids in purified samples containing adeno-associated virus (AAV). UV-based monitoring unfortunately over-estimates the proportion of full capsids and offers little value for characterizing unpurified samples. The present study combines dual-wavelength UV monitoring with intrinsic fluorescence, extrinsic fluorescence, and light-scattering to extend the utility of HPLC for supporting development of therapeutic AAV-based drugs. Applications with anion exchange (AEC), cation exchange (CEC), and size exclusion chromatography (SEC) are presented. Intrinsic fluorescence increases sensitivity of AAV detection over UV and enables more objective estimation of empty and full capsid ratios by comparison of their respective peak areas. Light scattering enables identification of AAV capsids in complex samples, plus semiquantitative estimation of empty and full capsid ratios from relative peak areas of empty and full capsids. Extrinsic Picogreen fluorescence enables semiquantitative tracking of DNA with all HPLC methods at all stages of purification. It does not detect encapsidated DNA but reveals DNA associated principally with the exteriors of empty capsids. It also enables monitoring of host DNA contamination across chromatograms. These enhancements support many opportunities to improve characterization of raw materials and process intermediates, to accelerate process development, provide rapid in-process monitoring, and support process validation.

Scale-Up of Plasmid DNA Downstream Process Based on Chromatographic Monoliths.

Purification of high-quality plasmid DNA in large quantities is a crucial step in its production for therapeutic use and is usually conducted by different chromatographic techniques. Large-scale preparations require the optimization of yield and homogeneity, while maximizing removal of contaminants and preserving molecular integrity. The advantages of Convective Interaction Media® (CIM®) monolith stationary phases, including low backpressure, fast separation of macromolecules, and flow-rate-independent resolution qualified them to be used effectively in separation of plasmid DNA on laboratory as well as on large scale. A development and scale-up of plasmid DNA downstream process based on chromatographic monoliths is described and discussed below. Special emphasis is put on the introduction of process analytical technology principles and tools for optimization and control of a downstream process.

The development of a monolith-based purification process for Orthopoxvirus vaccinia virus Lister strain.

The purification of large viruses remains an important field of research and development. The development of efficient purification trains is restricted by limited analytical methods, as well as by the complexity of large viruses, as well as the high variability in starting material from cell culture. Vaccinia virus holds great potential as an oncolytic and immunotherapeutic vaccine against a broad spectrum of cancers. In this work, monolith-based capture and polishing chromatographic steps for vaccinia virus Lister strain has been developed. Virus produced in CV-1 cells was harvested and passed through a 0.8µm pre-filter before loading onto CIEX, AIEX and HIC CIM monoliths. Without the need for nuclease treatment, up to 99% of the total DNA loaded can be removed from the vaccinia feed stream by the CIM OH monolith, which also reduces the total protein concentration in the product pool to LLOQ levels, and achieves infectious virus recoveries of 90%. Binding capacities of greater than 1×109pfu of vaccinia per mL of matrix were obtained on both CIM SO3 and CIM OH monoliths. Multiple orthogonal analytical methods have been used to develop process knowledge and understanding.

Production of ß-Lactoglobulin hydrolysates by monolith based immobilized trypsin reactors.

Tryptic hydrolysis of ß-Lactoglobulin (ß-Lg) is attracting more and more attention due to the reduced allergenicity and the functionality of resulting hydrolysates. To produce hydrolysates in an economically viable way, immobilized trypsin reactors (IMTRs), based on polymethacrylate monolith with pore size 2.1 µm (N1) and 6 µm (N2), were developed and used in a flow-through system. IMTRs were characterized in terms of permeability and enzymatic activity during extensive usage. N1 showed twice the activity compared with N2, correlating well with its almost two times higher amount of immobilized trypsin. N2 showed high stability over 18 cycles, as well as over more than 30 weeks during storage. The efficiency of IMTRs on hydrolyzing ß-Lg was compared with free trypsin, and the resulting hydrolysates were analyzed by MALDI-TOF/MS. The final hydrolysis degree by N1 reached 9.68% (86.58% cleavage sites) within 4 h, while only around 6% (53.67% cleavage sites) by 1.5 mg of free trypsin. Peptides analysis showed the different preference between immobilized trypsin and free trypsin. Under the experimental conditions used in this study, the potential cleavage site Lys135 -Phe136 was resistant against the immobilized trypsin in N1.