Research Highlight
A Validation Pathway for Continuous Peptide Chromatography
Continuous chromatography is already in production use for synthetic peptides and oligonucleotides. What has been missing is a published account of how to validate it for a regulatory filing. This study provides one, and carries it through four qualification runs at commercial scale.
Process Characterization and Performance Qualification of MCSGP
Competing interests, as disclosed by the authors: Ralf Eisenhuth was employed by Bachem AG and Thomas Müller-Späth by YMC ChromaCon. The research received no external funding.
Citation (BibTeX)
@article{eisenhuth2025process,
title = {Process Characterization and Performance Qualification of MCSGP},
author = {Eisenhuth, Ralf and M{\"u}ller-Sp{\"a}th, Thomas},
journal = {Processes},
volume = {13},
number = {12},
pages = {3950},
year = {2025},
doi = {10.3390/pr13123950}
}
MCSGP purifies continuously, recycling impure side fractions between two columns so that high yield and high purity are reached together. It does that by running to predefined recycling and collection windows, cycle after cycle, for hours or days — without the mid-run adjustment to pooling boundaries that an operator can make in batch chromatography. The chromatographic separation therefore has a greater influence on final product quality, and correspondingly more weight falls on the control strategy around it.
That makes validation a more demanding exercise. How do you show, in a regulatory filing, that a process running to fixed windows for days will deliver the right material every cycle?
This study is the first published Process Characterization and Process Performance Qualification approach for MCSGP, worked through on a commercial peptide. It identifies which process parameters actually matter, defines a supervision strategy for runs that last days, and confirms both across four qualification runs at manufacturing scale.
The study is a collaboration between Bachem AG and YMC ChromaCon, with Bivalirudin as the test system. It sits alongside an earlier characterization and validation study for CaptureSMB, the simpler twin-column capture process, and extends that thinking to gradient purification.
1. Why This Study Matters: A Gap Between Practice and Paperwork
MCSGP is in operation at several companies and research institutes, purifying synthetic peptides and oligonucleotides at production scale. Its appeal is well documented: internal recycling of impure side fractions lets it reach high yield and high purity at the same time, with a high degree of automation, fewer in-process controls and a lower process mass intensity than batch chromatography.
Regulatory validation is a separate matter from process performance, and it has its own structure. The FDA Process Validation guideline sets out three elements:
- Process Design Builds scientific understanding of the process. Process Characterization is the central piece: identifying which parameters could affect critical quality attributes, testing the high-ranked ones experimentally, and defining the ranges within which quality is met.
- Process Performance Qualification Confirms that the equipment and process perform as intended and can manufacture reproducibly at commercial scale. At least three consecutive representative batches are run under normal operating conditions, in the actual facility, with trained operators and qualified equipment.
- Continued Process Verification Ongoing monitoring once routine manufacturing is under way. This study covers the first two elements; the third is outside its scope.
None of that framework is specific to continuous chromatography, and the paper’s finding is that it largely does not need to be. What was missing was a worked example showing how it applies to a process whose defining feature — recycling material between two columns — has no counterpart in batch operation.
Where MCSGP differs, and where it does not
The paper separates the purification into two parts: the chromatographic part, which is identical for batch and MCSGP, and the product collection and recycling part, which is specific to MCSGP. The list of process parameters is therefore largely the same as for a batch process, with a few additions covering the recycling and collection step.
The practical difference is how many elutions it takes to generate meaningful data. For a batch purification, one elution per tested parameter is considered sufficient. An MCSGP experiment needs at least three cycles with two elutions each — enough to confirm that the process has reached cyclic steady state, that impurities are not accumulating through the weak or strong recycling streams, and that changes in column load caused by internal recycling do not affect the outcome.
2. The Study at a Glance
Bivalirudin was used as the test system: a 20-amino-acid direct thrombin inhibitor with a molecular weight of 2,180 g/mol, produced by solid-phase peptide synthesis and supplied as crude material of 81% purity. The target for the product pool was more than 99.0% purity, with the added constraint that the impurity profile had to be comparable to the legacy batch process.
Process parameters classified as critical after characterization
Gross-to-gross yield across the campaign, against 57% for the legacy batch process
In-process controls per kg of product, down from 81
kg/kg process mass intensity for the purification stage, down from around 5,200
What was run, and on what
Process Characterization
Carried out on a Contichrom CUBE 30 system. Four potentially critical parameters were varied one at a time, with at least five MCSGP cycles at each set point to confirm cyclic steady state. The two elutions per cycle were pooled and analyzed by HPLC for purity, individual impurities and yield.
Process Performance Qualification
Carried out on a Contichrom TWIN 500 system with two 30 cm internal diameter dynamic axial compression columns. A pre-PPQ GMP run of eleven elutions was followed by a campaign of four multiday MCSGP runs. All runs used AutoPeak UV-based process control, with detection at 280 nm.
3. How Far the Parameters Were Pushed
Most of the 34 identified parameters were never tested experimentally, and the reasoning behind that is worth following. Large-scale MCSGP equipment holds most parameters within narrow limits by construction. A Contichrom TWIN system has four three-head pumps — two for gradient generation, one for feeding, one for in-line dilution, cleaning-in-place and equilibration — and each is controlled by a dedicated flow meter with a calibration tolerance of ±2%.
Whether that ±2% matters depends entirely on what the pump is doing. For equilibration, in-line dilution, cleaning-in-place and chase washes, a 2% variation is negligible. For column load it is not: a 2% change alters the peak shape, which can shift what ends up inside the recycling zones. So the same tolerance makes one parameter well-controlled and another potentially critical, and only the second needs an experiment.
That assessment left four parameters to test. Each was then varied well beyond the range it covers in production.
- Linear velocity
- Displacer slope
- Column load
- Detection wavelength
What the equipment actually does. Each flow meter on the TWIN pumps carries a ±2% calibration tolerance, and eluent preparation adds to the spread on the gradient slope. These are the ranges routine manufacturing has to live with.
- Linear velocity
- ±2%
- Displacer slope
- ±8%
- Column load
- ±2%
- Detection λ
- ±1.6 nm
Ranges as reported in Table 4 of the study. Each row is drawn to its own tested range, so the inner bar shows how much of that range normal operation occupies rather than a shared scale. Colors identify the parameter, following Figure 3 of the paper; they do not indicate good or bad.
A Simple Analogy
Testing a bridge does not mean driving the expected traffic across it. It means loading it far past anything it will carry in service, and watching for the first sign of movement.
That is what the tested ranges are for. A gradient slope that varies by ±8% in production was pushed to ±25%; a column load that varies by ±2% was pushed to ±10%. If quality holds across a range several times wider than reality, the margin between normal operation and any observable effect is large — and that margin is what a control strategy is built on.
4. What Process Characterization Found
Every set point produced product above the 99.0% purity specification. Across all the characterization runs the average pool purity was 99.30%, and every individual value fell inside a band of ±3 standard deviations, that is 99.30% ± 0.32%. Since ±3σ captures roughly 99.7% of expected values for a normal distribution, the effect of the parameter variations was statistically indistinguishable from ordinary process noise. On purity alone, all four parameters would have been classified as non-critical, and the proven acceptable range would have been the full characterized range.
Purity did not identify the critical parameter. The impurity profile did.
Each eluate pool was also examined for individual impurities. Those profiles were consistent across every run but one: at −25% displacer slope, a single impurity rose from below the limit of quantitation to 0.13%. Small in absolute terms, but the specification required the impurity profile to be comparable to the legacy process, and it no longer was.
On that basis gradient slope was designated a critical process parameter, and the variance permitted during routine manufacturing was reduced through organizational measures. Column load, elution flow rate and detection wavelength were designated non-critical. The gross-to-gross yields were also evaluated; excluding the shallow-slope run, they fell between 60% and 65%.
Why one factor at a time, rather than a designed experiment
The choice of OFAT over DoE is argued explicitly, and the reasoning is specific to peptides. Related substances in a peptide tend to behave as regular samples, with similar retention behavior under gradient conditions, so the primary observable effect of parameter variation is the width of the overall peak rather than a change in resolution. Purity changes in MCSGP then tend to come from misalignment between the peak and the fixed recycling and collection zones.
That creates a practical hazard for a designed experiment. Combinations that cumulatively broaden or narrow the peak — a lower column load with a steeper slope and a wavelength shift that lowers the signal, for instance — can push the peak far enough out of alignment with fixed zones to fail the run, forcing repeated iterations of the DoE setup. OFAT does not reveal interactions between parameters, which is a real limitation, but it allows much wider ranges to be tested. For molecules with stringent purity specifications the paper recommends including the combinations that produce the narrowest and broadest peaks as fixed experiments, and considering smaller ranges.
5. Supervising a Process That Runs for Days
An MCSGP process producing eluate continuously for several days presents a sampling problem that batch chromatography does not. Collecting and analyzing every main cut separately is not cost-effective at production scale, but sampling too little leaves the process unsupervised. The answer here is a two-phase strategy.
- Start-up: intensive monitoring Every main cut is analyzed by an in-process control method until three criteria for cyclic steady state are met — comparable impurity profiles for the main cuts, good overlay of the UV traces on each column, and comparable main cut volume on a column basis.
- Steady state: strategic sampling Once those criteria are satisfied, HPLC sampling drops to two samples per day. Supervision then rests on three elements together: the strategic samples, the online UV trace overlay, and the recorded main cut volume per column.
The approach is aligned with the risk management expectations for product availability set out in ICH Q9 (R1).
AutoPeak as Process Analytical Technology
Underpinning the strategy is AutoPeak, which monitors UV at the column outlets and starts and stops the recycling and collection phases from absolute and relative UV triggers rather than from the clock. The main cut borders are set as UV thresholds entered into the control. Because the cut points track the peak rather than elapsed time, retention time shifts that accumulate over a long run do not move the pool composition.
The qualification runs illustrate this. Over PPQ batch 1, a slight peak shift appeared from cycle to cycle; when the traces were realigned to the AutoPeak trigger point marking the start of product collection, they overlaid exactly. On that basis the paper positions AutoPeak as Process Analytical Technology in the sense of the FDA PAT guidance — a framing supported by the FDA Process Validation and PAT guidance documents and by ICH Q8, Q11 and Q13, which explicitly support real-time monitoring as part of a control strategy.
6. The PPQ Campaign: Full Results
A pre-PPQ GMP run came first: eleven elutions, 1.5 kg of crude purified to 0.8 kg of intermediate at 99.6% purity, with a PMI of 1,402 kg/kg for the purification alone. The qualification campaign then ran four multiday MCSGP runs, the last batch split into two parts, to cover a range of batch sizes.
All four produced consistent elution profiles, main cut sizes and product purities. Comparing the third elution — the first at cyclic steady state — with elution 106 of the longest run showed the impurity profile holding across the full duration, and purity for every full elution stayed within the ±3σ band anticipated from characterization.
- Crude in 54.5 kg at 81% purity
- MCSGP 397 elutions over 235 hours, producing 1,576 L of main cut
- SPE 42 elutions over 65 hours on the same system and columns, alternately loading and eluting with a sharp gradient, producing 631 L of main cut
- API out 33.6 kg at 99.2% purity — a gross-to-gross yield of 62%, or 76% effective yield taking product and crude purity into account
- Total 300 hours of chromatography operating time
Against the legacy process
Swipe the table sideways to see the legacy and MCSGP columns.
| Metric | Legacy batch process | MCSGP with AutoPeak |
|---|---|---|
| Bivalirudin target purity >99.0% · impurity profile comparable to legacy | ||
| Column configuration | One 60 cm i.d. column | Two 30 cm i.d. columns |
| Gross-to-gross yield | 57% | 62% |
| In-process controls per kg | 81 | 3.2 |
| In-process controls, whole campaign | 2,753 | 108 |
| Process mass intensity, purification stage | ~5,200 kg/kg | 1,400 kg/kg |
Source: Eisenhuth and Müller-Späth, Processes 2025, 13, 3950 (CC BY). The legacy figure is the existing Bivalirudin batch process, which includes extensive side-cut re-chromatography.
Experimental conditions
Bivalirudin, a 20-mer direct thrombin inhibitor, 2,180 g/mol, from crude of 81% purity produced by solid-phase peptide synthesis.
C-18 stationary phase with a TFA / acetonitrile / water solvent system. UV detection at 280 nm.
Contichrom CUBE 30 (YMC ChromaCon, Zurich), with at least five MCSGP cycles per set point.
Contichrom TWIN 500 (YMC America) with 30 cm internal diameter dynamic axial compression columns.
Waters CSH C18, 1.7 µm, with a TFA / acetonitrile mobile phase on an Acquity UPLC system.
AutoPeak UV-based control active on all MCSGP runs, setting recycling and collection phases from absolute and relative UV triggers.
7. What This Means for Peptide Manufacturing
On the evidence here, the regulatory framework does not need reinventing for continuous chromatography. The parameter list is largely the batch list, the risk assessment is the standard one, and the qualification requirement is the standard three-batch expectation. What changes is the number of elutions needed to generate data, and the shift from correcting a process to supervising one.
That is a useful result for anyone weighing continuous purification against the validation work it would imply. Of 34 identified parameters, four warranted experiments and one turned out to be critical — and the paper notes that those same four would also be investigated during characterization of the corresponding batch process. The characterization burden is comparable; the difference is material consumption, since cyclic steady state has to be confirmed from successive identical elution profiles. In this study that extra experimental time was minimized by daisy-chaining the required MCSGP runs and executing them automatically.
The operational advantages appear in the campaign figures rather than in the validation argument. Running uninterrupted over several days, with the control strategy supported by online measurement, produced a substantial reduction in analytical sampling and process mass intensity alongside a higher gross yield. The authors also note that data integrity and electronic batch record handling requirements are identical for batch and MCSGP.
What the study does not claim
- One molecule, one site. The approach was demonstrated on Bivalirudin at a single manufacturer. The paper states directly that for different peptides or oligonucleotides, other parameters may be identified as potential CPPs. The four tested here are not a general list.
- The legacy comparison is not a controlled experiment. The 57% yield, 81 IPCs per kg and ~5,200 kg/kg PMI describe the existing batch process for this peptide, which includes extensive side-cut re-chromatography. The paper presents them as reference figures for the legacy process, not as a controlled comparison run alongside the MCSGP campaign.
- Two of the three validation elements. The study covers Process Characterization and Process Performance Qualification. Continued Process Verification, the ongoing monitoring phase, is outside its scope.
- Column lifecycle is excluded. The paper omits it deliberately, noting it is usually stand-alone work extending well beyond the manufacture of PPQ batches.
- Crude lots still need checking individually. The impurity profile has to be assessed case by case for each new crude lot with a small-scale use test until enough upstream batch experience exists to define standard parameters.
- The authors have a commercial interest. Ralf Eisenhuth was employed by Bachem AG, which manufactures the peptide, and Thomas Müller-Späth by YMC ChromaCon, which commercializes MCSGP. The paper discloses both.
8. Key Terms in This Study (Glossary)
| Term | Definition |
|---|---|
| AutoPeak | UV-based process control that starts and stops MCSGP recycling and collection phases from absolute and relative UV triggers at the column outlets, rather than from elapsed time. |
| Critical process parameter (CPP) | A process parameter whose variation has a demonstrated impact on a critical quality attribute, and which therefore has to be controlled within defined limits. |
| Critical quality attribute (CQA) | A property of the product that must fall within a defined range to ensure quality. The criteria used in this study were product purity, levels of individual related substances, and yield. |
| Continued Process Verification (CPV) | The third element of FDA Process Validation: ongoing monitoring of the process during routine commercial manufacturing. |
| Cyclic steady state | The condition in a continuous process where each cycle reproduces the previous one. Confirmed here from comparable impurity profiles, overlaid UV traces and consistent main cut volumes. |
| Design of Experiments (DoE) | An experimental strategy that varies several parameters together, revealing interactions between them. Not used here — see OFAT. |
| Displacer slope | The rate at which the eluting solvent strength increases during the gradient. The one parameter classified as critical in this study. |
| FMEA | Failure Mode and Effect Analysis, a structured risk assessment used to rank process parameters by their potential impact on quality attributes. |
| Gross-to-gross yield | Mass of API produced divided by mass of crude loaded, ignoring the purity and peptide content of the crude. Used here for consistency with the legacy process. |
| In-process control (IPC) | An analytical test performed on material during manufacturing to confirm the process is performing as intended. |
| Main cut | The product fraction collected from an elution, with its borders set in this process by UV thresholds entered into AutoPeak. |
| MCSGP | Multicolumn Countercurrent Solvent Gradient Purification: a continuous twin-column gradient chromatography process that recycles impure side fractions internally rather than discarding them. |
| OFAT | One Factor At A Time: varying a single parameter per experiment. Does not reveal interactions, but allows much wider ranges to be tested than a designed experiment. |
| Process Analytical Technology (PAT) | A framework for designing and controlling manufacturing through timely measurement of critical attributes, set out in FDA guidance and supported by ICH Q8, Q11 and Q13. |
| Process Characterization (PC) | The part of Process Design that identifies potential critical process parameters, tests the high-ranked ones experimentally, and defines the ranges within which quality attributes are met. |
| Process Mass Intensity (PMI) | Total mass of material input per unit mass of product. Reported here for the purification stage only. |
| Process Performance Qualification (PPQ) | The second element of Process Validation: demonstrating at commercial scale, in the actual facility, that the process consistently delivers product meeting specification. |
| Proven Acceptable Range (PAR) | The range of a process parameter within which quality attributes are demonstrated to be met. Where a parameter shows no effect, the PAR is the full characterized range. |
| ±3σ band | Three standard deviations either side of the mean, capturing roughly 99.7% of expected values for a normal distribution. Used here as the threshold for distinguishing a real effect from process noise. |
9. Frequently Asked Questions
Yes, and this study is the first published account of how. It applies the standard FDA Process Validation framework to MCSGP, working through Process Characterization and Process Performance Qualification for the purification of Bivalirudin. The process parameter list turns out to be largely the same as for batch chromatography, with a few additions covering the recycling and collection step, and the qualification requirement is the standard expectation of at least three consecutive representative batches.
In this case, four of 34 identified parameters warranted experimental testing: linear elution velocity, gradient slope, column load, and detection wavelength. Of those, only gradient slope was ultimately classified as a critical process parameter. The paper is explicit that this is molecule-specific — for different peptides or oligonucleotides, other parameters may prove critical.
Because purity was not the attribute that moved. Every run produced pool purity above 99.0%, within a ±3σ band of 99.30% ± 0.32% — statistically indistinguishable from process noise. The individual impurity profiles told a different story: at −25% displacer slope, one impurity rose from below the limit of quantitation to 0.13%. Since the specification required the impurity profile to be comparable to the legacy process, that single change was enough to classify the parameter as critical and tighten its permitted variance.
Fewer, once the process is at cyclic steady state. In this campaign the number of in-process controls fell from 81 per kg for the legacy batch process to 3.2 per kg — 108 tests across the whole campaign against 2,753. The supervision strategy front-loads the sampling: every main cut is analyzed during start-up until steady state criteria are met, after which HPLC sampling drops to two samples per day, backed by online UV trace overlay and main cut volume recording.
Yes. Where one elution per tested parameter is considered sufficient for a batch purification, an MCSGP experiment needs at least three cycles with two elutions each, so that cyclic steady state can be confirmed and impurity accumulation through the recycling streams ruled out. The paper notes this requirement, and that in this study the extra experimental time was minimized by daisy-chaining the required runs and executing them automatically.
The paper positions it as PAT in the sense of the FDA PAT guidance. AutoPeak monitors UV at the column outlets and uses absolute and relative triggers to start and stop the recycling and collection phases, so the cut points follow the peak rather than the clock. The FDA Process Validation and PAT guidance documents, together with ICH Q8, Q11 and Q13, explicitly support PAT and real-time monitoring as part of a control strategy.
Commercial scale. Four multiday MCSGP runs on a Contichrom TWIN 500 system with two 30 cm internal diameter columns processed 54.5 kg of crude Bivalirudin into 33.6 kg of API at 99.2% purity, across 397 MCSGP elutions over 235 hours plus a solid phase extraction step of 42 elutions over 65 hours on the same equipment.
Yes. It is published open access under a CC BY license in Processes (MDPI), so it can be read, downloaded and reused with citation. The full parameter tables, the characterization results and the qualification campaign data are in the article itself.