PEPTIDE PURIFICATION

Peptide APIs:Separation & Preparative Purification

Microwants peptide purification solutions — starting from the six adjustable parameters of modified silica, with stationary phase selection and process notes for seven classes of peptide structure, mapped onto specific Daisogel grades. Supported by packing stations, DAC packing support and process development services.

Peptide API Purification

Analysis and Preparative Purification Solutions for Peptide APIs

For solid-phase synthesized peptides, lipopeptides and cyclic peptides, we provide chromatographic solutions from method development through crude preparative purification to industrial scale-up. Peptide impurities are structurally very close to the main component, so two or more separation mechanisms in combination are generally needed to reach API-grade purity.

Reversed-Phase Preparative Purification

Reversed-phase chromatography is the main mode in preparative peptide purification. With TFA or ammonium acetate / phosphate mobile phase systems, C18 media at 100–120 Å give good selectivity for most peptides of 10–40 residues. Loading and resolution must be calibrated batch by batch against crude purity, and parameters from another batch should generally not be carried over directly.

Daisogel C18 COSMOSIL 5C18-AR-II SilicaOne preparative media
57 / 59preparative steps use acetonitrile as the strong eluent
Read more · Chapter 5 →

Orthogonal modes and impurity control

Deletion peptides, diastereomers, and acetylation and trifluoroacetylation by-products are close in properties to the main peak, and a single reversed-phase method generally cannot resolve them all. Ion exchange separates by net charge and HILIC by hydrophilicity, giving orthogonal confirmation against reversed phase for cross-checking release purity.

IEX ion exchange HILIC Orthogonal confirmation
13 / 21products use two steps in series, switching the system or the pH between them
Read more · Chapter 6 →

Lipopeptides and long-chain peptides

Lipopeptides and GLP-1 class long-chain peptides are more hydrophobic and readily show peak broadening and reduced recovery on conventional 100 Å media. The usual change is to a 120–300 Å wide-pore substrate with a C8 or C4 bonded phase, together with a somewhat higher column temperature and organic proportion, to improve mass transfer and recovery.

120–300 Å C8 / C4 bonded phases Wide-pore substrates
C8 / C4Lipidated peptides move to a shorter chain to suppress excessive retention and on-column aggregation
Read more · Chapter 7 →

Amino acid composition and chiral purity

The PEPONE-24 multifunctional peptide cleavage system carries out hydrolysis pretreatment under temperature-controlled, sealed conditions, and is used with pre-column derivatization for amino acid composition analysis. The DL-amino acid kit serves as a reference standard for calibrating the D/L ratio in the hydrolysate.

PEPONE-24 cleavage system DL-Amino Acid Kits Composition analysis
7 classesstructural classes, each with its own impurity profile and confirmation methods
Read more · Chapter 14 →

Preparative column packing and process scale-up

From semi-preparative to industrial scale, bed uniformity affects resolution more than the medium itself. Microwants supplies packing stations, self-packed preparative columns and dynamic axial compression (DAC) packing support, and can assist with scale-up validation and efficiency assessment at Ø200–600 mm.

Packing stations DAC Packing Support Process Development
236Daisogel specifications, matched by pore size / particle size / phase / grade
Read more · Chapter 21 →

Recommended configuration for a peptide laboratory

The core set from analytical method development to preparative purification

COSMOSIL 5C18-AR-II analytical columns Daisogel C18 preparative media PEPONE-24 peptide cleavage system Preparative column packing service
Get the solution →
The technical basis for the five capability modules above is set out in the Modified Silica and Peptide Purification Technical Overview below. Six parts · 22 chapters · a modified silica selection matrix for seven classes of peptide structure · statistics on systems and parameter ranges from 59 preparative steps across 21 products · a complete mapping from structural class to Daisogel grade, organized by structural chemistry rather than by product name.
Full technical overview

Modified silica and peptide purification: a full analysis reorganized by structural class, separation handle and surface parameters

The difficulty in peptide purification lies not in the target molecule but in how closely the impurities resemble it structurally. The text follows one axis throughout: structural class → critical impurities → separation handle → modified silica → process parameters. It first explains the six adjustable parameters of modified silica and how to derive the separation handle, then works through the impurity profile, surface parameter combination and process notes for seven classes of peptide structure, then draws out the selection rules for pore size, chain length, endcapping and metal content, and finally arrives at process parameter ranges, scale-up and the mapping to Daisogel grades.

Version2026-08 technical review
Main axisStructural class × modified silica × process
Coverage7 structural classes · 22 chapters · 59 preparative steps across 21 products
Evidence gradingIndustry consensus / record statistics / manufacturer data / to be measured

SummaryTen core conclusions

Structural class
7 classes
Lipidated metabolic peptides, disulfide peptides, macrocyclic peptides, radioconjugates, protein/PEG conjugates, fermentation peptides, short and modified peptides
Process sample
21 / 59
Summary statistics on mobile phase systems and gradients from 59 preparative steps across 21 products
Adjustable parameters
6
Pore size, particle size, alkyl chain length, bonding density, endcapping, metal content
Daisogel specifications
236
The number of pore size × particle size × bonded phase × grade combinations available on this site
1
The selection chain starts from the structure, not from the column. The workable order is "structural class → critical impurities → separation handle → modified silica → process parameters". Establish first which physicochemical property differs between the target peptide and its main impurities (hydrophobicity, net charge, molecular size, hydrophilicity, configuration), then choose the surface modification that amplifies that difference, and only then adjust gradient and column temperature. Choosing the column first and fitting conditions to it afterwards converges slowly in peptide systems, where impurities and the main peak are so alike.
2
Reversed phase occupies the main axis. Of the 59 preparative steps collected, 57 use acetonitrile as the strong eluent and 2 use methanol; the aqueous phase contains phosphoric acid or phosphate in 27, acetic acid in 23 and TFA in 21, with triethylamine as counter-ion in 20, ammonia for pH adjustment in 13 and ammonium salt systems in 7. All are reversed-phase ion-pair systems; the orthogonal axes (IEX / HILIC / SEC / normal phase) fill gaps rather than carry the main line. Record statistics
3
Modified silica has only six adjustable parameters. Pore size, particle size, alkyl chain length, bonding density (carbon load), endcapping and substrate metal content. Almost every stationary phase problem met in peptide purification — tailing, low recovery, unresolved isomers, short column life — can be brought back to one or two of these six without needing a more elaborate explanation.
4
Pore size steps up with the molecule's hydrodynamic radius. Conventional synthetic peptides (10–40 residues) transfer mass adequately at 100–120 Å; insulin-type peptides and those prone to aggregation move to 200 Å; denatured proteins and large fragments use 300 Å; SEC polishing of conjugates enters the 1000–2000 Å ultra-wide-pore range. Too small a pore shows as peak broadening and reduced recovery; too large a pore sacrifices surface area and loading. Industry consensus
5
There is no "longer is better" in alkyl chain length. Lipidated metabolic peptides carry a C16–C20 fatty diacid side chain and are over-retained on C18, which promotes on-column aggregation, showing as broad peaks, low recovery and reduced loading; moving to C8 or C4 brings the retention window back into a controllable range. Conversely, hydrophilic short peptides are barely retained on conventional C18 and need a high-surface-area or hydrophilically modified C18, not a shorter chain.
6
Endcapping is a selectivity variable, not merely a measure of quality. Full endcapping suppresses ionic interaction between residual silanols and basic residues, improving tailing; while a non-endcapped product retains surface silanols that provide hydrogen bonding — a second selectivity that C18 and C8 do not have — which is useful for near-isomers that conventional reversed phase cannot resolve. Whether to endcap depends on whether that interaction is wanted, not on purity as such.
7
Disulfide peptides and radioconjugates are sensitive to substrate metal content. Transition metals can catalyse disulfide exchange on the column, generating scrambled isomers with the same sequence but a different disulfide topology; chelating radioligands compete for coordination with metals leached from the substrate, affecting specific activity. For these two classes, "ultra-high-purity silica (total Al, Fe, Ti and Zr below 10 ppm)" becomes a prerequisite rather than an option. Manufacturer data
8
Preparative gradients are generally very shallow. Of the 59 preparative steps, the 57 with a resolvable main elution segment have a median slope of 0.10 %B/min, an interquartile range of 0.089–0.233 %B/min, a minimum of 0.067 %B/min and a maximum of 0.44 %B/min; the median total step duration is 71 min, over a range of 40–160 min. Resolution in preparative peptide work comes from gradient slope and bed quality, not from a higher flow rate. Record statistics
9
Two-step processes are the norm, not the exception. Thirteen of the 21 products use two preparative steps in series. The two steps usually switch the ion-pair system or the pH — a common combination is an acidic ion-pair system in the first step and a near-neutral buffer in the second, or the reverse. Elution order changes after the switch, so the two steps are orthogonal rather than a repetition of the same separation handle. Record statistics
10
The conclusions map onto specific grades. Lipidated metabolic peptides map to the 100 Å C8 / C4 flagship series and non-endcapped C4; disulfide peptides and radioconjugates to the ultra-high-purity and wide-pH series; hydrophilic short peptides to high-surface-area or low-carbon-load hydrophilically modified C18; large conjugates to 300 Å wide pore and 1000–2000 Å ultra-wide pore. Chapter 21 gives the full mapping from the seven structural classes to Daisogel grades.
Part One Why peptide purification rests on modified silica

1Starting materials and sources of impurities

The difficulty in preparative peptide purification lies not in the target molecule but in how closely the impurities in the crude resemble it structurally. Understanding which step generates each impurity determines which property to look for a difference in.

1.1 Three main source routes

Source routeRepresentative productsOrder of crude purityMain impurity types
Solid-phase synthesis (SPPS)Leuprorelin, triptorelin, cetrorelix, the semaglutide backboneCrude purity usually 50%–75%Deletion peptides, truncated peptides, racemates, residual side-chain protecting groups, trifluoroacetylation adducts
Recombinant expressionInsulin and its analogues, some fusion peptidesDepends on expression and initial captureHost protein, misfolded species, enzymatic cleavage by-products, deamidation variants
Fermentation and semi-synthesisDaptomycin, micafungin, telavancinFermentation broth is coarsely fractionated on resin before polishingLipid chain homologues, pigments, isomerization products, fermentation impurities

1.2 How small the difference between impurity and main peak is

Most impurities from a synthetic route differ from the target peptide by only one residue, one acyl group or one chiral centre. For a deletion peptide, the change in hydrophobicity from one missing non-polar residue may correspond to only a few percentage points of organic phase in reversed phase; a racemate has exactly the same molecular formula, and its reversed-phase retention difference is often near the limit of detection. This is why preparative peptide work generally uses gradients of the order of 0.1 %B/min — resolution has to be bought from gradient slope and column efficiency.

Impurities close in hydrophobicity to the main peak
  • Deletion and truncated peptides: one or more residues short
  • Trifluoroacetylation adducts: TFA residues from cleavage and lyophilization forming amides with side-chain amines
  • Mono- and di-acylation by-products and lipid chain isomers of lipidated peptides
  • Lipid chain homologues of fermentation peptides (differing by one or two carbons)
Impurities barely differing in hydrophobicity
  • Racemates and diastereomers: same molecular formula, different configuration
  • Scrambled disulfides: same sequence, different disulfide topology
  • Deamidation variants: Asn→Asp / iso-Asp, changing one charge only
  • Conformational isomers and cyclic dimers of macrocyclic peptides
Asparagine (Asn)
Asn, asparagine
The deamidation precursor, with a neutral amide side chain
Aspartic acid (Asp)
Asp, aspartic acid
The deamidation product, carrying one more negative charge — better resolved by IEX
L-alanine
L-Ala
Target configuration
D-alanine
D-Ala
The racemic impurity, with a molecular formula identical to the L form

Fig. 1 Four residue-level examples. The middle pair is deamidation before and after: a neutral amide becomes a carboxyl, changing reversed-phase retention little but altering the net charge, so ion exchange resolves it. The right pair is a pair of enantiomers: neither reversed phase nor ion exchange resolves them, so a chiral column or pre-column derivatization is needed. The structures show only the backbone and key functional groups; stereochemistry follows the original literature.

2The role of each substrate: silica, polymer and soft gel

Silica is not the only substrate for preparative chromatography. Choosing it is not a default but a consequence of the pressure, packing scale and resolution required in preparative peptide work.

Substrate typeMechanical strengthpH toleranceEfficiencyPosition in a peptide process
Spherical porous silica (bonded phase)Withstands industrial DAC packing pressureConventional products about pH 2–8; base-stable grades extend to pH 1.5–11High, with particle sizes down to 3 μmThe mainstay of preparative and polishing work; all 59 preparative steps collected fall into this category
Polymer microspheres (PS-DVB)Pressure resistant, with solvent-dependent swellingpH 1–13 throughoutLower than silica of the same particle sizeCleaning under strongly alkaline conditions and applications needing special selectivity
Macroporous adsorption resinSoft, low-pressure operationWideLowCoarse fractionation and decolorization of fermentation broth, as a volume-reduction step before polishing
Agarose / dextran soft gelsLow, requiring a low-pressure columnWideLowAffinity capture, IEX and SEC polishing of conjugates
Why silica dominates peptide polishing
  • Efficiency matches a shallow gradient.A gradient of the order of 0.1 %B/min only converts into resolution when efficiency is high enough, and the efficiency of spherical silica at 5–15 μm is beyond what soft gels and resins can reach.
  • It withstands DAC packing.Industrial scale requires dynamic axial compression to keep the bed uniform, so the substrate must not fracture under compression and operating pressure.
  • The surface chemistry can be tuned finely.Chain length, bonding density, endcapping and pore size can be combined independently, giving a matched surface for each structural class.
  • Batch consistency is controllable.Pore size distribution, surface area and metal content can be characterized batch by batch, which suits process validation and regulatory filing.

The limits of a silica substrate are equally clear: a conventional bonded phase run above pH 8 for long periods hydrolyses the siloxane skeleton; where alkaline conditions are required, use a base-stable product or move to a polymer substrate. See Chapter 18.

3Six adjustable parameters of surface modification

In process terms, "modified silica" resolves into six parameters that can be specified independently. These six form the coordinate system for every selection discussion that follows.

ParameterUsual valuesDirect effectHow it shows in a peptide process
Pore size60 / 100 / 120 / 200 / 300 Å, ultra-wide 1000 / 2000 ÅThe upper molecular size that can enter the pores, and the surface areaToo small a pore broadens peaks and reduces recovery; too large a pore reduces loading
Particle sizeAnalytical 3–5 μm; preparative 7–20 μm; coarse fractionation 30–50 μmEfficiency and column pressureHalving the particle size raises efficiency and roughly quadruples pressure drop, and must match the bed length and the equipment's pressure rating
Alkyl chain lengthC18 (ODS) / C8 / C4 / alkyl phenyl / aminopropylThe strength and type of hydrophobic retentionDetermines whether the target peptide's retention window falls at a workable organic proportion
Bonding density (carbon load)About 3%–24%Retention strength, loading, compatibility with aqueous conditionsHigh carbon load raises loading and retention; low carbon load suits hydrophilic peptides and fully aqueous mobile phases
EndcappingFully endcapped / non-endcappedThe accessibility of residual silanolsEndcapping suppresses tailing of basic residues; non-endcapped provides additional hydrogen bonding selectivity
Substrate metal contentUltra-high-purity grades keep Al+Fe+Ti+Zr below 10 ppmMetal catalysis and competition for chelationA prerequisite for suppressing on-column exchange in disulfide peptides and for maintaining specific activity in radiopeptides

3.1 What the surface groups actually look like

Surface silanols
Surface silanols
The unmodified substrate, the source of hydrogen bonding and ionic interaction
C18 octadecyl
C18 · ODS
The strongest hydrophobic retention; the mainstay for conventional synthetic peptides
C8 octyl
C8 · octyl
Moderate hydrophobicity; common for lipidated peptides and insulin-type molecules
C4 butyl
C4 · butyl
Weak hydrophobicity; for strongly hydrophobic samples and denatured proteins
Alkyl phenyl
Alkyl phenyl (C4Ph)
Hydrophobicity plus π–π interaction, giving selectivity for aromatic residues
Pentafluorophenylpropyl
Pentafluorophenylpropyl (PFP)
Dipole and configurational selectivity, for epimers and diastereomers
Aminopropyl
Aminopropyl (APS)
HILIC and normal phase, for hydrophilic peptides and carbohydrates
Trimethylsilyl endcapping
Trimethylsilyl endcapping
Occupies residual silanols, suppressing tailing of basic residues

Fig. 2 Eight surface groups. The grafting anchor is drawn throughout as (HO)₃Si–, the convention used across this site: in the real material that silicon is linked to the silica surface network by one to three Si–O–Si bonds, and no free trihydroxysilane exists. All structures are rendered by RDKit from SMILES and have passed molecular formula and ring count assertions. Product parameters are at the Daisogel product pageandChromatographic Silica Fundamentals

Part Two From structural features to the separation handle

4Deriving the separation handle

The "separation handle" is the physicochemical difference between the target peptide and its main impurities that chromatography can amplify. Fixing the separation handle amounts to fixing which class of surface modification to use.

Separation handleThe difference amplifiedCorresponding chromatographic modeCorresponding surface modificationTypical impurities addressed
HydrophobicityNon-polar surface areaReversed phase (RP)C18 / C8 / C4Deletion peptides, truncated peptides, acylation by-products
Net chargeThe number and pKa of ionizable groupsIon exchange (IEX)Strong and weak anion and cation exchange groupsDeamidation variants, charge variants
Molecular sizeHydrodynamic radiusSize exclusion (SEC)Wide-pore and ultra-wide-pore substratesAggregates, dimers, large truncated fragments
HydrophilicityDensity of polar groupsHILICBare silica / aminopropyl / amide / zwitterionicHydrophilic short peptides, glycosylation variants, salts
Configuration and shapeSpatial arrangement, with the same molecular formulaHigh-selectivity reversed phase / chiral phasesPentafluorophenyl, phenyl, polysaccharide chiral selectorsEpimers, diastereomers, conformational isomers
Hydrogen bonding accessibilityDonors and acceptors able to interact with silanolsNon-endcapped reversed phase / normal phaseNon-endcapped C4, diolNear-isomers that conventional reversed phase cannot resolve
How to use the derivation in four steps
  • Step 1 List the impurities.Enumerate the possible impurities from the synthetic or fermentation route, without letting the chromatogram prejudge it.
  • Step 2 Find the difference.For each impurity, decide which of the six properties above differs from the target peptide.
  • Step 3 Rank them.Take the separation handle for the impurity at the highest level, or with the strictest regulatory limit, as the main handle for the first process step.
  • Step 4 Add an orthogonal step.For impurities the first step cannot resolve, pick a different separation handle for the second. See Chapter 6 and conclusion 9.

5The reversed-phase backbone: system distribution across 59 preparative records

The statistics below come from mobile phase records for 59 preparative steps across 21 products. The basis is "this component appears in the mobile phase of this step"; one step may contain several components, so the percentages sum to more than 100%. This section gives only the system distribution and parameter ranges, not the complete gradient for each product.

Aqueous componentNumber of stepsShare of 59Function
Phosphoric acid / phosphate2746%Strong buffering with a wide controllable pH range and a low UV cut-off
Acetic acid2339%Volatile and relatively easy to remove in work-up; a weak ion-pairing agent
Trifluoroacetic acid (TFA)2136%A strong ion-pairing agent that improves peak shape, but residues form the trifluoroacetate salt
Triethylamine (as counter-ion)2034%Paired with an acid to set pH, while also shielding residual silanols
Ammonia (pH adjustment)1322%Moves the system to neutral or weakly alkaline, changing the elution order
Ammonium salts (ammonium acetate / sulfate)712%Volatile or semi-volatile systems at neutral pH, common as the second step
Formic acid47%MS-friendly; for oral products and where on-line MS monitoring is needed
Citric acid23%A low-pH buffer with weak chelating action
Tris12%Buffering on the weakly alkaline side, used as an orthogonal system in a second step
Perchloric acid12%A strong ion-pairing agent, used for particular cyclic peptides
Strong eluent

Acetonitrile 57 / 59 Methanol 2 / 59

The low viscosity and low UV absorbance of acetonitrile make it more stable over long shallow gradients; methanol appears only in a few steps, used to change selectivity.

pH distribution

The pH values recorded:1.8 / 2.0 / 2.1 / 2.25 / 2.3 / 2.5 / 3.0 / 3.5 / 6.0 / 6.5 / 7.0 / 7.5 / 8.0

These fall clearly into two clusters, acidic (1.8–3.5) and neutral to weakly alkaline (6.0–8.0); two-step processes commonly switch between the clusters, rearranging the elution order.

Gradient and duration

Median slope of the main elution segment 0.10 %B/min, interquartile 0.089–0.233, extremes 0.067–0.44

Median total step duration 71 min, range 40–160 min. Most processes use a three-part form: an isocratic equilibration segment → a rapid step increase → a shallow elution gradient.

Trifluoroacetic acid
Trifluoroacetic acid (TFA)
Used in 21 of 59 steps. Pairs with the peptide's basic residues to form a neutral ion pair, improving peak shape; residues form the trifluoroacetate salt and must be exchanged in a later step
Heptanesulfonic acid
Heptanesulfonic acid
An alkylsulfonic ion-pairing agent. Provides an extra hydrophobic anchor for hydrophilic short peptides, pulling the retention window back from near the dead volume into a usable range

Fig. 3 Two classes of ion-pairing agent. TFA is a volatile acid: strongly effective, but salt formation must be considered in work-up; alkylsulfonic agents are non-volatile, with a marked retention effect but a corresponding demand on downstream desalting.

6Orthogonal axes: where IEX, HILIC, SEC and normal phase fill the gaps

Reversed phase deals with most differences in hydrophobicity; the remaining impurities need a different separation handle. Which orthogonal axis to choose is determined by the type of impurity left.

Residual impurityRecommended orthogonal axisStationary phasePoint
Deamidation variants, charge variantsIon exchange (IEX)Strong and weak anion and cation exchange groupsA salt or pH gradient, resolving a difference of one charge unit
Aggregates, dimersSize exclusion (SEC)Wide-pore and ultra-wide-pore spherical silicaIsocratic operation; the pore size must cover the size range of both target and aggregates
Hydrophilic impurities, salts, glycosylation variantsHILICBare silica / aminopropyl / amide / zwitterionicStart at high organic and elute by lowering it; the elution order is roughly the reverse of reversed phase
Epimers, diastereomersHigh-selectivity reversed phasePentafluorophenyl, phenylπ–π and dipole interactions superimposed on hydrophobicity; small changes in column temperature amplify the selectivity difference
Conformational isomers, hydrophobic impuritiesNormal phaseBare silica, diol, aminopropylNon-aqueous or low-water systems, with selectivity weakly correlated to reversed phase
Near-isomers that conventional reversed phase cannot resolveNon-endcapped reversed phaseNon-endcapped C4Silanol hydrogen bonding superimposed on weak hydrophobicity, forming a second interaction
Orthogonal does not mean changing the column

In most of the recorded two-step processes, the stationary phase type was not changed at all; the mobile phase system was switched: an acidic ion-pair system in step one and a near-neutral ammonium salt in step two. The peptide's net charge differs at the two pH values, so its interaction with the stationary phase changes and the elution order is rearranged — which already constitutes effective orthogonality. Changing the stationary phase chemistry is one way of achieving orthogonality, not the only way. The test is whether the elution orders of the two steps are decorrelated, not whether the hardware changed. Record statistics

Part Three Seven structural classes × modified silica × process

The seven classes below follow the order "structural features determine the separation difficulty, and the difficulty determines the modified silica". Each gives the structural difficulty, the recommended combination of surface parameters, and the system and parameter ranges obtained from the preparative records. The Daisogel grades and specifications cited are the stated values from theproduct pageson this site.

7A · Linear lipidated metabolic peptides

Representative products Semaglutide, tirzepatide, retatrutide, cagrilintide, liraglutide, mazdutide

7.1 Structural difficulty

What these have in common is a C16–C20 fatty diacid side chain on the backbone, usually attached through a γ-Glu and AEEA linker. The lipid chain has two consequences: the molecule is far more hydrophobic than an ordinary peptide of the same length and is over-retained on C18; and it tends to self-associate in aqueous solution, forming aggregates at the column head and within the bed, showing as peak broadening, reduced loading and unstable recovery. The impurities closest in properties to the target are mono- and di-acylation by-products, des-AA deletion peptides and lipid chain positional isomers, all three differing very little from the target in polarity.

Octadecanedioic acid
Octadecanedioic acid
The acyl part of the lipidated side chain. One end forms an amide to the linker, the other retains a free carboxyl
γ-Glu–AEEA linker
γ-Glu–AEEA linker fragment
Connects the lipid chain to the lysine side chain of the backbone, with two ethylene glycol units providing flexibility and a hydrophilic balance

Fig. 4 The two parts of the lipidated side chain. The hydrophobic end and the hydrophilic linker together determine how these molecules behave in reversed phase: the hydrophobic end provides strong retention while the linker reduces the tendency to aggregate.

7.2 Modified silica selection

Parameter combination
  • Alkyl chain length C8 or C4, not C18. A shorter chain reduces excessive retention of the lipidated side chain and suppresses on-column aggregation
  • Pore size Most products (4–5 kDa) transfer mass adequately at 100–120 Å; those with a marked tendency to aggregate, or larger, move to 200 Å
  • Particle size 8–10 μm is usual in preparative work, balancing efficiency against pressure drop on an industrial column
  • Endcapping Fully endcapped, to suppress tailing from residual silanols
  • Bonding density High bonding density to maintain loading, compensating for the lower retention of a shorter chain
Corresponding Daisogel grade
  • SP-100-8-C8-PK 100 Å / 8 μm / 320 m²·g⁻¹ / 11.0% carbon. The PK series is the base-stable, high-strength flagship, suiting semaglutide, retatrutide and similar Manufacturer data
  • SP-100-10-C8-PK The 10 μm grade in the same series, for larger column diameters or where pressure drop must be reduced
  • SP-100-8-C4-NP 100 Å / 8 μm / 450 m²·g⁻¹ / 10.0% carbon, non-endcapped C4. Silanol hydrogen bonding provides selectivity C8 does not have, suiting cagrilintide and similar
  • SP-200-10-C8-BIO The 200 Å wide-pore, pH-tolerant grade, for larger molecules or products needing alkaline cleaning

Grades and specifications are in the Daisogel product page"III. C8 series" and "V. C4 series".

7.3 Process notes

ItemValue and practiceBasis
Mobile phase systemAcidic side: TFA, or TFA with acetic acid, adjusted to about pH 2 with triethylamine or ammonia; neutral side: phosphoric acid with acetic acid, or a low-concentration ammonium salt at pH 6–8Record statistics
Two-step combinationThe two steps switch between acidic and neutral systems. More alternative schemes were recorded for this class than for any other, with several systems often screened in parallel for the same productRecord statistics
GradientA step increase to the starting B%, then a shallow gradient; the main elution slope for this class mostly falls between 0.09 and 0.14 %B/min, with steps of 66–100 minRecord statistics
Anti-aggregation measuresUrea or isopropanol added to the load to suppress on-column aggregation; the concentration must be established by measurement for each productTo be measured
Column temperatureA moderately raised column temperature improves mass transfer and peak shape, with the upper limit set by the stability of the target peptideIndustry consensus
LoadingBelow the stated loading of the same medium for conventional peptides, since aggregation reduces effective capacity; must be calibrated batch by batchTo be measured

8B · Disulfide and cyclic disulfide peptides

Representative products Linaclotide, octreotide, bivalirudin, etelcalcetide, somatostatin, terlipressin, carbetocin

8.1 Structural difficulty

Peptides with one to three disulfide bonds generate scrambled disulfide isomers during oxidative folding: identical in sequence, differing only in disulfide topology, with the same molecular formula and almost identical hydrophobicity. These impurities are both hard to resolve and liable to keep forming during chromatography — neutral to alkaline conditions and transition metals both promote on-column disulfide exchange. The process constraint is therefore not only resolution but "do not create new impurities".

Cystine disulfide bridge
Cystine · disulfide bridge
Two cysteine residues joined by S–S. With several cysteine pairs on one chain the pairing is not unique, and the wrong pairing gives a scrambled isomer
Surface silanols
Substrate surface
Transition metals (Al, Fe, Ti, Zr) residual in the silica substrate can catalyse disulfide exchange; ultra-high-purity substrates keep the total below 10 ppm

Fig. 5 The two concerns with disulfide peptides: the disulfide bridge itself, and the metals in the substrate that may catalyse its exchange.

8.2 Modified silica selection

Parameter combination
  • Alkyl chain length Mainly C18, since these are mostly short to medium peptides for which conventional hydrophobic retention is sufficient
  • Pore size 100–120 Å
  • Particle size 5–10 μm; a shallow gradient needs adequate efficiency
  • Metal content An ultra-high-purity substrate, to suppress on-column disulfide exchange
  • pH tolerance A wide-pH product makes alkaline regeneration convenient, but the operating segment should still stay on the acidic side
Corresponding Daisogel grade
  • SP-120-10-ODS-BIO 120 Å / 10 μm; the BIO series has improved high-density bonding and full endcapping, with a stated pH stability range of 1.5–11 and regeneration with aqueous NaOH Manufacturer data
  • SP-100-10-ODS-P 100 Å / 10 μm / 450 m²·g⁻¹ / 17% carbon. P denotes the ultra-high-purity grade, with total Al, Fe, Ti and Zr below 10 ppm
  • SP-120-10-ODS-RPS 120 Å / 10 μm, the general-purpose reversed-phase mainstay with good acid resistance, suiting processes that run on the acidic side for long periods
  • SP-100-10-ODS-HP 24% carbon and 450 m²·g⁻¹ surface area, for folding isomers that are very hard to resolve, trading stronger retention for selectivity

8.3 Process notes

ItemValue and practiceBasis
pH controlKeep the operating segment acidic. The aqueous pH recorded for this class clusters at 1.8–2.5, with TFA, phosphoric acid and phosphate as the main acidsRecord statistics
Column temperatureRun on the low side, to slow disulfide exchange; the exact temperature must be established together with the peptide's on-column stabilityIndustry consensus
GradientFolding isomers need a shallower gradient. The main-segment slope recorded for this class is mostly 0.10–0.13 %B/min, with steps of the order of 70 minRecord statistics
Metal controlChoose an ultra-high-purity substrate; where necessary add a low concentration of chelating agent to the mobile phase, after assessing its effect on detection and work-upTo be measured
Oxidative foldingCarried out in dilute solution to suppress intermolecular mispairing; the dilution factor and the volume burden are the trade-off point between yield and throughputIndustry consensus
Release confirmationThe collected fraction must have its disulfide connectivity confirmed by native mass spectrometry or peptide mapping; reversed-phase purity alone does not prove the topology is correctIndustry consensus

9C · Macrocyclic and synthetic macrocyclic peptides

Representative products Oral PCSK9 macrocyclic peptides, complement inhibitor macrocycles, synthetic macrocycles containing D-amino acids

9.1 Structural difficulty

A macrocyclic backbone restricts conformational freedom, giving two characteristic impurity types: conformational isomers, which interconvert slowly on the chromatographic timescale and therefore appear as several peaks; and cyclic dimers and epimers. Oral products carry a further constraint: the limits on deletion peptides and potential genotoxic impurities are usually stricter, and the method must be MS-compatible for on-line confirmation.

9.2 Modified silica selection

Parameter combination
  • Main phase C18 or C8, 5 μm / 100–120 Å
  • High-selectivity phase Pentafluorophenyl (PFP) resolves epimers and conformational isomers better than a conventional alkyl phase; alkyl phenyl provides π–π interaction
  • Normal phase support Bare silica or a diol phase, for orthogonal confirmation of conformational isomers
  • Choice of acid Formic acid rather than TFA for oral products and on-line MS
Corresponding Daisogel grade
  • SP-100-8-C4Ph-HP 100 Å / 8 μm / 450 m²·g⁻¹ / 16.0% carbon, alkyl-phenyl bonded, giving π–π recognition in addition to hydrophobic interaction Manufacturer data
  • SP-100-10-C4Ph-HP The 10 μm preparative grade in the same series
  • SP-120-5-ODS-RPS 120 Å / 5 μm, for method development and semi-preparative work
  • SP-120-10-P (bare silica) Ultra-high-purity spherical bare silica, for normal phase and as support in resolving conformational isomers

Pentafluorophenyl is not in the current Daisogel bonded phase range; where required it can go through Custom Bonded Phasesassessment; one racemate separation step in the preparative records used a pentafluorophenyl column.

9.3 Process notes

  • System The reversed-phase aqueous component is low-concentration formic acid or TFA. The recorded racemate separation used a low-pH ammonium salt aqueous phase on a pentafluorophenyl column, run isocratically at low organic — isocratic rather than gradient, which indicates the separation relies on selectivity rather than eluting strength. Record statistics
  • Column temperature Configurational selectivity is temperature sensitive, and a small change in temperature can widen or narrow the resolution of epimers; this is the main optimization variable for this class.
  • Orthogonality Reversed phase resolves configuration and normal phase resolves conformation; the two correlate weakly, which suits them to cross-checking release purity.

10D · Peptide radioconjugates

Representative products ¹⁷⁷Lu-labelled somatostatin receptor and PSMA-targeting peptide conjugates

10.1 Structural difficulty

These molecules comprise a targeting peptide, a linker and a chelator (of the DOTA class), and purification faces three constraints at once: the chelator is highly sensitive to trace metals, and any metal from the substrate, reagents or containers occupies coordination sites and lowers specific activity; the radionuclide half-life is limited, so everything after labelling must be completed within hours; and purification of the cold precursor and purification after labelling are two different kinds of step.

10.2 Modified silica selection

Parameter combination
  • Cold precursor preparation C18, 100–120 Å, 5–10 μm, on an ultra-high-purity, low-metal substrate
  • Post-labelling purification A C18 SPE cartridge to remove free radionuclide and reducing agent quickly, in a matter of minutes
  • Metal control Metal removal across the whole chain: substrate, mobile phase, tubing and containers
Corresponding Daisogel grade
  • SP-100-10-ODS-P The ultra-high-purity grade, with total metal impurities below 10 ppm, for cold precursor preparation Manufacturer data
  • SP-120-10-ODS-BIO Wide pH tolerance, allowing alkaline regeneration between batches to clear residual metal
  • SPEONE SPE Cartridges Rapid post-labelling purification and solvent exchange; see SPE cartridges on the product page

10.3 Process notes

  • Labelling buffer A sodium acetate system at weakly acidic pH, with an antioxidant to suppress radiolysis. Concentration and temperature are set by the radionuclide and chelator.Industry consensus
  • Time budget The whole sequence from labelling to release must fit within the window allowed by the radionuclide half-life, so chromatographic steps should be as short and as few as possible.
  • Metal removal Metal leaching from glassware, corrosion products from stainless steel tubing and the metal background of mobile phase reagents must each be assessed separately.

11E · Peptide–protein and PEG conjugates

Representative products Antibody–peptide conjugates, PEGylated complement inhibitor peptides, peptide–Fc fusions

11.1 Structural difficulty

The finished product is a biomacromolecule, and the quality attributes shift from "peptide purity" to conjugation degree distribution, PEG polydispersity, aggregates, host protein and endotoxin. The peptide chemistry exists only before conjugation: the peptide fragment itself still goes through reversed-phase preparative work, while purification after conjugation moves into the protein process paradigm.

11.2 Modified silica selection

StageModeBase matrixNotes
Peptide fragment preparationReversed phaseC18 / C8,100–200 ÅAs for a conventional synthetic peptide; residual solvent and ion-pairing agent must be controlled before conjugation
CaptureAffinityProtein A class soft gelsNon-silica substrates
PolishingIon exchange / hydrophobic interactionIEX and HIC mediaResolves the conjugation degree distribution and charge variants
Final polishingSize exclusionWide-pore and ultra-wide-pore spherical silicaRemoval of aggregates, run isocratically
Corresponding Daisogel grade
  • SP-300-10-C4-BIO 300 Å / 10 μm, low carbon load C4, for reversed-phase separation of denatured proteins and large peptide fragments Manufacturer data
  • SP-300-20-C4-P 300 Å / 20 μm, listed on the product page as suitable for erythropoietin (EPO) purification
  • SWP ultra-wide-pore series Two grades, SP-1000 and SP-2000 (1000 Å / 2000 Å), surface area 15–25 m²·g⁻¹, particle sizes 3–20 μm, available as bare silica and as bonded phases, for biomacromolecules that conventional narrow-pore silica cannot separate
  • JNC Cellufine Cellulose Media Soft gel capture and polishing; see product pages

12F · Fermentation-derived peptides and lipopeptides

Representative products Micafungin, telavancin and daptomycin-class cyclic lipopeptides

12.1 Structural difficulty

Fermentation-derived material has two characteristics: the lipid chain homologue profile varies between batches, with homologues differing by only one or two carbons, so reversed-phase retention differences are small but numerous; and the broth itself contains pigments, endotoxin and a large impurity load, so the burden on the crude is far higher than for a synthetic peptide. Some products also have characteristic chemical instability, requiring limits on temperature, light and pH.

12.2 Modified silica selection

Parameter combination
  • Initial purification Coarse fractionation and decolorization on macroporous adsorption resin, reducing the volume before polishing
  • Polishing C18, pore size 200–300 Å to accommodate the size of cyclic lipopeptides, particle size 10–15 μm
  • Supporting Normal-phase bare silica to remove fat-soluble impurities
  • Batch consistency Requires a substrate with consistent pore size distribution and carbon load between batches, or homologue resolution will drift with the medium lot
Corresponding Daisogel grade
  • SP-200-10-ODS-RPS 200 Å / 10 μm; the product page notes that this pore size balances surface area, separation speed and solvent consumption Manufacturer data
  • SP-200-15-ODS-RPS The 15 μm preparative grade, for larger column diameters
  • SP-300-15-ODS-BIO 300 Å / 15 μm, with wide pH tolerance for alkaline cleaning between batches, suiting the column regeneration needs of fermentation material
  • SP-200-15-P (bare silica) Normal phase for removing fat-soluble impurities

12.3 Process notes

  • System The aqueous phases recorded for this class are mainly low-concentration ammonium salts or organic acids, with single steps running to 90 min or more and main-segment slopes of the order of 0.14 %B/min; there are also two-step processes that switch both the acid and the strong eluent at once. Record statistics
  • Stability limits Products prone to isomerization need defined temperature limits, protection from light and pH control, with the limits set by that product's stability studies.To be measured
  • Batch variation Variation in the homologue profile of fermentation material requires margin in the process, usually absorbed by multidimensional chromatography and dynamic adjustment of the collection window.

13G · Short peptides, D-amino acid and hydrophilically modified peptides

Representative products Thymopentin, thymalfasin, difelikefalin, gonadorelin, carbetocin, synthetic peptides containing several D-amino acids

13.1 Structural difficulty

Three separate problems: short and hydrophilic peptides are barely retained on conventional C18 and co-elute with salt; products containing D-amino acids have diastereomers with the same molecular formula and similar hydrophobicity; and short peptides are hard to desalt, because their retention window overlaps that of the salt.

13.2 Modified silica selection

QuestionSolutionModified silicaDaisogel equivalent
Weak retention of hydrophilic peptidesRaise the surface area and carbon loadHigh-surface-area C18SP-100-10-ODS-P(450 m²·g⁻¹ / 17%C)、SP-100-10-ODS-HP(450 m²·g⁻¹ / 24%C)
Weak retention of hydrophilic peptidesIon-pair enhancementConventional C18 plus an alkylsulfonic agentSP-120-10-ODS-RPS
Phase collapse in a fully aqueous mobile phaseHydrophilically modified low carbon load C18Low carbon load hydrophilically modified C18SP-120-10-ODS-BP(carbon content 10%–15%; the product page states it can be used in 100% aqueous mobile phase)
A hydrophilic separation handleHILICAminopropyl / bare silicaSP-120-10-APS-PSP-60-5-APS-PSP-100-10-P Bare silica
DiastereomersHigh-selectivity reversed phaseAlkyl phenyl / pentafluorophenylSP-100-8-C4Ph-HP; the pentafluorophenyl phase requires a custom assessment
Desalting short peptidesReversed-phase desalting or solid phase extractionLow carbon load C18SP-120-10-ODS-BP, SPEONE SPE cartridges
The product page's technical note on the BP series

The ODS-BP series uses a bonding method that keeps the long C18 chains extended even in low-alcohol solutions, with a carbon content of 10%–15% and a stated ability to run in 100% aqueous mobile phase, maintaining baseline stability at neutral pH without buffer salts or ion-pairing agents. The typical applications listed on the product page include oligosaccharides, amino acids, small peptides, nucleotides and organic acids. Manufacturer data

13.3 Process notes

  • System Two approaches were recorded for this class: pushing the pH to the alkaline side to enhance retention differences between short peptides, with main-segment slopes as low as the order of 0.08 %B/min; and keeping the same acid system across both steps while moving the pH from acidic to near neutral, achieving orthogonality through the change in net charge. Record statistics
  • Column temperature Diastereomers and hydrophilic peptides are often separated at a lower column temperature, to amplify the selectivity difference.Industry consensus
  • Ion-pair residues Non-volatile ion-pairing agents create a downstream desalting burden; confirm the removal scheme before choosing one.

14Master matrix: seven structural classes × eight dimensions

CategoryMain impuritiesSeparation handleAlkyl phasePore sizeParticle sizeKey secondary attributeDaisogel first choice
A Linear lipidated metabolic peptidesMono/di-acylation, des-AA, lipid chain isomersHydrophobicity (aggregation suppressed)C8 / C4100–200 Å8–10 μmFully endcapped, high bonding densitySP-100-8-C8-PK
SP-100-8-C4-NP
B Disulfide and cyclic disulfide peptidesScrambled disulfide isomersHydrophobicity + conformationC18100–120 Å5–10 μmUltra-high-purity, low metal, acid resistantSP-120-10-ODS-BIO
SP-100-10-ODS-P
C Macrocyclic and synthetic macrocyclic peptidesConformational isomers, cyclic dimers, epimersConfiguration and shapeC4Ph / C18 / PFP100–120 Å5–10 μmπ–π selectivity, MS-friendly acidSP-100-8-C4Ph-HP
SP-120-5-ODS-RPS
D Peptide radioconjugatesFree radionuclide, dechelated speciesHydrophobicity (fast)C18100–120 Å5–10 μmMetal removal across the whole chain, time budgetSP-100-10-ODS-P
SPEONE solid phase extraction
E Protein and PEG conjugatesConjugation degree distribution, aggregates, host proteinCharge + sizeMainly C4, with the bulk of the work outside reversed phase300 Å and above10–20 μmWide pore and ultra-wide poreSP-300-10-C4-BIO
SWP series
F Fermentation-derived peptides and lipopeptidesLipid chain homologues, pigments, isomerization productsHydrophobicity (homologues)C18200–300 Å10–15 μmBatch consistency, alkaline regenerationSP-200-10-ODS-RPS
SP-300-15-ODS-BIO
G Short peptides and hydrophilically modified peptidesCo-elution with salt, diastereomersHydrophilicity / configurationHigh-surface-area C18 / BP / APS60–120 Å5–10 μmHigh carbon load or hydrophilically modifiedSP-100-10-ODS-HP
SP-120-10-ODS-BP

The grades in the table are starting points matched on parameters, not the only answer. Actual selection should take account of crude purity, the pressure rating of the available equipment, the target loading and the work-up scheme, and be confirmed at bench scale. Full specifications are at the Daisogel product page, and documentation at 。

Part Four Cross-cutting rules for selecting modified silica

Read across the seven classes and the selection rules converge to four: pore size scales with molecular size, chain length is chosen by the separation difficulty rather than by hydrophobicity alone, endcapping and bonding density set the balance between peak shape and loading, and metal content and pH tolerance are prerequisites that decide whether a medium can be used at all.

15The pore size ladder: from 60 Å to 2000 Å

The purpose of pore size is to let the target move freely in and out of the pores. When the molecule's hydrodynamic radius approaches the pore size, intraparticle diffusion is impeded, showing as peak broadening and reduced recovery; when the pore is far larger than the molecule, surface area falls geometrically and loading falls with it. Bigger is therefore not better; the pore should just cover the molecule.

Pore sizeStated Daisogel surface areaSuited toCorresponding structural class in this text
60 ÅAbout 450 m²·g⁻¹Small molecules and very short peptides, normal phase and HILICThe HILIC step for class G short peptides
100 Å320–450 m²·g⁻¹Conventional synthetic peptides, lipidated metabolic peptides, disulfide peptidesA / B / C / D
120 ÅAbout 300 m²·g⁻¹The general-purpose reversed-phase mainstay, 10–40 residue peptidesB / C / F / G
200 ÅAbout 200 m²·g⁻¹Insulin-type molecules, cyclic lipopeptides, molecules prone to aggregationA / F
300 ÅAbout 100 m²·g⁻¹Denatured proteins, large peptide fragments, oligonucleotidesE / F
1000 / 2000 Å(SWP)15–25 m²·g⁻¹Biomacromolecules that conventional narrow-pore silica cannot separateE

The surface areas are the ranges stated on the Daisogel product pages; different grades at the same pore size differ.Manufacturer data

The trade-off between pore size and loading

Moving from 100 Å to 300 Å reduces surface area to roughly a third, and the usable adsorption area per unit mass of medium falls with it. If the target peptide has no mass transfer problem at 100 Å, choosing a large pore simply because the molecule "is fairly big" usually loses loading and throughput for nothing. The basis for the decision should be the measured peak shape and recovery, not the molecular weight.

16Alkyl chain length and carbon load

Chain length determines the type and strength of hydrophobic retention, and carbon load determines the depth of retention and the loading at a given chain length. The two must be read together: a low carbon load C18 does not necessarily retain more strongly than a high carbon load C8.

Bonded phaseDaisogel carbon content rangeRetention characteristicsSuited toNot suited to
C18(ODS)7%–24%, banded by gradeThe strongest hydrophobic retentionConventional synthetic peptides, disulfide peptides, fermentation peptides, hydrophilic short peptides (choosing a high carbon load grade)Lipidated metabolic peptides (over-retained, promoting aggregation)
C86%–15.5%Moderate hydrophobicityLipidated metabolic peptides, insulin-type molecules, samples over-retained on C18Hydrophilic short peptides (insufficient retention)
C43%–10%Weak hydrophobicityDenatured proteins, large peptide fragments, very hydrophobic samplesConventional short to medium peptides (insufficient retention)
Alkyl phenyl (C4Ph)16.0%Hydrophobicity plus π–πPeptides containing aromatic residues, epimers and diastereomersSamples with no aromatic structure and no configurational problem
Aminopropyl (APS)2%–5%Hydrophilic interaction / normal phaseHydrophilic short peptides, carbohydrates, HILIC stepsThe main preparative step for hydrophobic peptides
Where a high carbon load is used

The Daisogel HP series C18 has 24% carbon and 450 m²·g⁻¹ surface area, extending retention while raising loading; the product page positions it for "small molecules and peptides with more demanding separation requirements, and for improving selectivity on very difficult separations". Used for hydrophilic short peptides and for resolving near-isomeric impurities.Manufacturer data

Where a low carbon load is used

The BP series C18 has 10%–15% carbon, with a bonding method that keeps the C18 chains extended in low-alcohol solutions, stated to be usable in 100% aqueous mobile phase and to maintain baseline stability at neutral pH without buffer salts or ion-pairing agents. Used for hydrophilic peptides, desalting and where LC-MS compatibility is needed.Manufacturer data

17Endcapping, bonding density and residual silanols

The bonding reaction cannot cover every silanol on the silica surface, and what remains are the "residual silanols". Endcapping uses a small silylating reagent after bonding to occupy those sites. Whether to endcap is a directional choice in peptide purification.

Endcapped products
  • Suppress ionic interaction between basic residues (Lys, Arg, His) and silanols
  • Peak symmetry improves and the tailing factor falls
  • Batch-to-batch selectivity is more consistent, because it does not depend on the distribution of residual silanols
  • The Daisogel PK, P, HP, BIO and RPS series are all endcapped products
Non-endcapped products (NP series)
  • The retained surface silanols provide hydrogen bonding, a second selectivity beyond hydrophobicity
  • Suited to near-isomers that conventional C18 / C8 cannot resolve
  • The product page positions C4-NP as "separation through silanol interaction where a distinctive selectivity is needed"Manufacturer data
  • The cost is that basic peptides may tail, which has to be compensated by a mobile phase counter-ion such as triethylamine
Trimethylsilyl endcapping
Endcapping: trimethylsilyl occupying the site
Residual silanols are occupied by a small silane and ionic interaction is suppressed
C4 butyl
Non-endcapped C4
Butyl provides weak hydrophobicity while the neighbouring unoccupied silanols provide hydrogen bonding, the two combining into a mixed mode

Fig. 6 The difference between endcapped and non-endcapped is what remains on the surface besides the alkyl chain. The process criterion is whether the separation needs that hydrogen bonding interaction.

Triethylamine in the mobile phase does the same job

Twenty of the 59 preparative steps collected contain triethylamine. Besides setting pH, its other role is to compete with residual silanols, reducing tailing of basic peptides. This means "degree of endcapping" and "mobile phase counter-ion" are two solutions to the same problem, which can substitute for or be combined with one another. Which to use depends on how much non-volatile material the work-up can tolerate. Record statistics

18Metal content and pH tolerance

18.1 Metal content

The Daisogel "P" grade denotes ultra-high-purity silica, with total Al, Fe, Ti and Zr below 10 ppm; the BIO and HSA series, although not marked P, also use an ultra-high-purity silica substrate. The manufacturer analyses metal impurities by XRF and ICP and provides the data to customers.Manufacturer data

Mechanism by which metals actConsequenceStructural classes affected
Transition-metal catalysed disulfide exchangeNew scrambled disulfide isomers form on the column, and purity falls with residence timeB disulfide peptides
Metals occupying chelation sitesSpecific activity falls and free chelator increasesD radioconjugates
Metals coordinating to acidic residuesPeak tailing, retention drift, reduced recoveryPeptides with several Asp / Glu residues
Metal-catalysed oxidationSecondary impurities such as Met oxidation and Trp degradationProducts with readily oxidized residues

18.2 pH tolerance and column regeneration

A conventional bonded silica normally runs at pH 2–8. The Daisogel BIO series product page states a pH stability range of 1.5–11, regenerable by flushing with aqueous NaOH; the alkali tolerance data given for the PK series is that the bare silica withstands more than 170 column volumes of dilute NaOH flushing before the particles dissolve.Manufacturer data

What alkali tolerance is actually for in a peptide process
  • Column regeneration.Fermentation material and low-purity synthetic crude accumulate strongly retained impurities on the column, and alkaline cleaning is the usual way to clear them.
  • Selectivity on the alkaline side.Thirteen of the recorded steps use ammonia to push the pH to 6.0–8.0, and running on the alkaline side requires a substrate that can take it.
  • Column life and cost per unit of throughput.Whether alkaline cleaning is possible directly affects the number of usable cycles, and at kilogram-scale industrial purification this carries considerable weight in cost.

Note that alkali tolerance means the substrate and bonded layer do not degrade appreciably under the cleaning conditions; it is not a recommendation to run at high pH for long periods. The operating pH should still be set by the stability of the target peptide and the separation required.

Part Five Process parameters and scale-up

19Gradient, column temperature and loading

19.1 Gradient form: three segments

The 59 preparative steps collected are highly consistent in gradient form, which resolves into three segments:

① Isocratic equilibration

Hold the starting B% for 5–10 min, to let the sample focus at the column head after loading and the baseline settle. The recorded starting B% ranges from 2% to 20%.

② Step increase

Raise B% over 1–5 min to close to the elution point of the target peptide. This segment flushes weakly retained impurities away quickly and shortens the total run time.

③ Shallow elution gradient

The main separation segment. Median slope 0.10 %B/min, interquartile range 0.089–0.233 %B/min. Resolution is produced here.

ParameterSummary statistics (57 steps with a resolvable gradient segment)Notes
Main-segment slopeMinimum 0.067, Q1 0.089, median 0.100, Q3 0.233, maximum 0.44 %B/minThe more structurally similar impurities there are, the shallower the slope
Total step durationMinimum 40 min, median 71 min, maximum 160 minIncluding the equilibration and step segments
Starting B%2%–20%Hydrophilic peptides at the low end, lipidated peptides and cyclic lipopeptides at the high end
Final B%9%–66%Directly related to the hydrophobicity of the target peptide
Strong eluentAcetonitrile in 57 steps, methanol in 2Methanol is used to change selectivity

The above are summary statistics from the preparative records of 21 products; complete methods for individual products are not published. Gradient design for a new product can start from these ranges, but the actual slope must be set by the resolution obtained at bench scale. Record statistics

19.2 Column temperature

Column temperature is a two-way variable in preparative peptide work: raising it improves mass transfer, lowers viscosity and column pressure, and improves peak shape; lowering it suppresses on-column chemistry (disulfide exchange, isomerization, epoxide opening) and may amplify configurational selectivity. The direction is set by the on-column stability of the target peptide, not by mass transfer efficiency alone.

PreferenceApplicable classesPurpose
Higher column temperatureA lipidated metabolic peptides, F fermentation cyclic lipopeptidesSuppresses on-column aggregation, improves mass transfer and peak shape
Lower column temperatureB disulfide peptides, C epimers, G diastereomers and chemically unstable productsSuppresses on-column chemical change and amplifies configurational selectivity
AmbientConventional synthetic peptidesThe default where there is no particular constraint

The exact temperature must be established from the product's on-column stability studies; no general figure is given here.To be measured

19.3 Loading

Loading depends on crude purity, target purity, the acceptable yield loss and the surface area of the medium; it is not an inherent constant of the medium. The usable loading on the same column can differ several fold between crude at 50% and at 75% purity. In practice the inflection point is found from a bench-scale loading curve, then scaled linearly by column volume, with margin left for industrial batches. To be measured

Three checks that often get skipped
  • Matching the solvent strength of the load to the mobile phase.Where the load has a higher organic proportion than the starting B%, the sample does not focus at the column head, showing as a broadened front — easily overlooked when isopropanol is used to suppress aggregation of lipidated peptides.
  • Extra-column volume.The tubing, flow cell and collection valves of a preparative system add extra-column volume that dilutes components already separated, which matters appreciably over a long shallow gradient.
  • The basis for the collection window.Collecting by time and collecting by signal threshold behave differently under batch variation; state which governs and record it.

20From the analytical column to the industrial DAC column

A substantial part of the resolution in preparative peptide work comes from the quality of the bed rather than from the medium. The same lot of medium can give very different resolution in a uniform bed and in a non-uniform one, and this becomes more pronounced at large column diameters.

ScaleTypical column diameterParticle sizePacking methodWhat matters
Method Development4.6–10 mm3–5 μmSlurry packingEstablishing resolution and selectivity, fixing the system and gradient
Semi-preparative20–50 mm5–10 μmSlurry or axial compressionLoading curve, collection window, recovery
Pilot100–200 mm10–15 μmDynamic axial compression (DAC)Bed uniformity, pressure drop, efficiency acceptance
Industrial200–600 mm and above10–20 μmDACBatch consistency, column life, solvent recovery
What is held constant on scale-up
  • Bed length (which sets the plate number)
  • Linear velocity in cm·h⁻¹ (not volumetric flow rate)
  • Gradient slope expressed in column volumes (%B per CV), not in time
  • Loading per unit mass of medium, mg·g⁻¹
What changes on scale-up
  • The share of extra-column volume falls, so peak shape usually improves
  • Pressure drop changes with column diameter and particle size, so equipment margin must be recalculated
  • Packing uniformity carries more weight, and the DAC compression factor must be calibrated
  • Solvent consumption and recovery cost enter the decision and may in turn change the choice of system
Efficiency acceptance and problem diagnosis

After packing, a DAC column should be accepted on theoretical plate number and peak asymmetry, with reduced plate height h as the usual criterion. Where the packing fails, first distinguish between a medium problem, a packing process problem and a system extra-column effect before deciding whether to repack. This site provides DAC Packing SupportDAC Packing Problem Diagnosisand Column Packing Service; piston seals and frits are covered at Piston sealsand Piston frits

Part Six Implementation and selection

21Structural class → Daisogel grade mapping

This chapter maps the parameter conclusions above back onto the Daisogel specifications available on this site. The parameters listed are the stated values from the product pages, and grades are read under the coding rule "SP-pore size-particle size-bonded phase-grade". Manufacturer data

21.1 The Daisogel coding rule at a glance

Code segmentMeaningValue
① ShapeParticle formSP (spherical)
② Pore sizeIn Å60 / 100 / 120 / 200 / 300; SWP ultra-wide 1000 / 2000
③ Particle sizeIn μm3 / 4 / 5 / 7 / 8 / 10 / 15 / 20 / 30 / 40 / 50
④ Bonded phaseStationary phase typeODS / C8 / C4 / C1 / C4Ph / APS; no marking means bare silica
⑤ GradePurity and process gradeP (ultra-high purity) / PK / HP / RPS / BP / BIO / NP
⑥ EndcappingSilanol state(NE) means non-endcapped; no marking means an endcapped product

"P" denotes ultra-high-purity silica with total Al, Fe, Ti and Zr below 10 ppm; the BIO and HSA series, although not marked P, also use ultra-high-purity silica. The full rule and all specifications are at the Daisogel product page

21.2 Grades by structural class

Structural classFirst choice gradePore size / particle sizeSurface area · carbon contentReason for selection
A Linear lipidated metabolic peptidesSP-100-8-C8-PK100 Å / 8 μm320 m²·g⁻¹ · 11.0%A shorter chain suppresses over-retention and on-column aggregation; PK is the base-stable, high-mechanical-strength flagship series
SP-100-8-C4-NP100 Å / 8 μm450 m²·g⁻¹ · 10.0%Non-endcapped C4, where silanol hydrogen bonding provides selectivity C8 does not have
SP-200-10-C8-BIO200 Å / 10 μmAbout 200 m²·g⁻¹ · 6%–12%A larger pore with wide pH tolerance, for products prone to aggregation or needing alkaline cleaning
B Disulfide and cyclic disulfide peptidesSP-120-10-ODS-BIO120 Å / 10 μmAbout 300 m²·g⁻¹ · 8%–20%High-density bonding with full endcapping, stated pH 1.5–11, regenerable with NaOH
SP-100-10-ODS-P100 Å / 10 μm450 m²·g⁻¹ · 17%An ultra-high-purity substrate with metal impurities below 10 ppm, suppressing on-column disulfide exchange
SP-100-10-ODS-HP100 Å / 10 μm450 m²·g⁻¹ · 24%Very high carbon content, for folding isomers that are extremely hard to resolve
C Macrocyclic and synthetic macrocyclic peptidesSP-100-8-C4Ph-HP100 Å / 8 μm450 m²·g⁻¹ · 16.0%Alkyl-phenyl bonded, adding π–π recognition to hydrophobicity, for epimers and conformational isomers
SP-120-5-ODS-RPS120 Å / 5 μmAbout 300 m²·g⁻¹ · 17%General-purpose reversed phase for method development and semi-preparative work
D Peptide radioconjugatesSP-100-10-ODS-P100 Å / 10 μm450 m²·g⁻¹ · 17%An ultra-high-purity substrate, reducing competition from metals for the chelation sites
SP-120-10-ODS-BIO120 Å / 10 μmAbout 300 m²·g⁻¹Wide pH tolerance, for alkaline cleaning between batches to clear residues
E Protein and PEG conjugatesSP-300-10-C4-BIO300 Å / 10 μmAbout 100 m²·g⁻¹ · 3%–9%Large-pore, low carbon load C4, matched to denatured proteins and large peptide fragments
SP-300-20-C4-P300 Å / 20 μmAbout 100 m²·g⁻¹Listed on the product page as suitable for EPO purification
SWP series (SP-1000-10 / SP-2000-10 and others)1000 / 2000 Å / 3–20 μm15–25 m²·g⁻¹Ultra-wide-pore bare and bonded silica, for biomacromolecules that conventional narrow-pore silica cannot separate
F Fermentation-derived peptides and lipopeptidesSP-200-10-ODS-RPS200 Å / 10 μmAbout 200 m²·g⁻¹The product page notes that 200 Å balances surface area, separation speed and solvent consumption
SP-300-15-ODS-BIO300 Å / 15 μmAbout 100 m²·g⁻¹Large pore with wide pH tolerance, matched to the size of cyclic lipopeptides and to frequent alkaline cleaning
SP-200-15-P (bare silica)200 Å / 15 μmAbout 200 m²·g⁻¹Normal phase for removing fat-soluble impurities
G Short peptides and hydrophilically modified peptidesSP-100-10-ODS-HP100 Å / 10 μm450 m²·g⁻¹ · 24%High surface area and high carbon load, enhancing retention of hydrophilic short peptides
SP-120-10-ODS-BP120 Å / 10 μmAbout 300 m²·g⁻¹ · 10%–15%Hydrophilically modified, low carbon load, usable in 100% aqueous mobile phase, suiting desalting and LC-MS
SP-120-10-APS-P120 Å / 10 μmAbout 300 m²·g⁻¹ · 2%–4%Aminopropyl phase, for HILIC and normal-phase separation of hydrophilic peptides
SP-100-8-C4Ph-HP100 Å / 8 μm450 m²·g⁻¹ · 16.0%High-selectivity separation of diastereomers

21.3 Supporting product lines

StageProduct or service on this sitePurpose
Method DevelopmentCOSMOSIL columnsHPLCONE ColumnsEstablishing resolution and selectivity at the analytical and semi-preparative stage
Stationary phase screeningDaisogel COMPASS pre-screening kitRapid orientation across several bonded phases and pore sizes
Preparative mediaThe full Daisogel rangeSilicaOneThe main media for preparative and industrial purification
Special selectivityCustom Bonded PhasesPhases not covered by the current range (pentafluorophenyl, for example) can be assessed for customization
Packing and scale-upColumn Packing MachinesPacking ServiceDAC Packing SupportBed uniformity and efficiency acceptance
Composition confirmationMultifunctional Peptide Cleavage SystemsDL-Amino Acid KitsAmino acid composition analysis and calibration of the D/L ratio
Contract process workProcess DevelopmentImpurity PreparationCustom ServicesMethod development, impurity reference standard preparation and custom manufacture
Metal removalMetal scavenging solutionsControl of residual catalyst metals in synthetic peptides

22One-page reference and data basis

22.1 One-page reference: from symptom to action

ObservationPossible causeFirst actionSee
Broad target peak and low recovery, with a hydrophobic sampleOn-column aggregation or over-retentionMove from C18 to C8 / C4; add an anti-aggregation component to the load; raise the column temperature moderatelyChapters 7 and 16
Peak tailing, with a sample containing several basic residuesIonic interaction with residual silanolsSwitch to a fully endcapped product, or add triethylamine to the mobile phaseChapter 17
Purity falling with run time, with disulfide bonds presentOn-column disulfide exchangeLower the column temperature, move the pH to the acidic side, switch to an ultra-high-purity substrateChapters 8 and 18
The target peptide is barely retained and co-elutes with saltStrongly hydrophilic, with insufficient hydrophobic retentionMove to a high carbon load C18; or add an alkylsulfonic ion-pairing agent; or switch to HILICChapter 13
Two peaks that never separate, with the same molecular formulaConfigurational or conformational isomersSwitch to an alkyl phenyl or pentafluorophenyl phase; fine-tune the column temperature; consider normal phase as an orthogonal stepChapter 9
Reversed-phase purity passes but IEX shows extra peaksDeamidation or charge variantsAdd IEX as a second step, or adjust the pH of the first stepChapter 6
Resolution after scale-up is below bench scaleA non-uniform bed, or extra-column volumeCheck the packed efficiency and pressure drop, and quantify the extra-column volumeChapter 20
Column pressure rising batch by batch with falling efficiencyAccumulation of strongly retained impuritiesEstablish an alkaline regeneration procedure; requires a base-stable substrateChapter 18

22.2 Data basis

MarkingMeaningWhat it covers in this text
Industry consensusCommon practice in published textbooks and reviewsPore size to molecular size correspondence, the direction of column temperature, principles of orthogonal combination
Record statisticsSummary statistics from 59 preparative steps across 21 productsMobile phase system distribution, gradient slope ranges, pH distribution, proportion using two steps
Manufacturer dataStated catalogue valuesDaisogel pore size, particle size, surface area, carbon content, pH range and metal impurity limits
To be measuredVaries considerably; must be established at bench scaleLoading, exact column temperature, anti-aggregation agent concentration, stability limits

22.3 Scope

  • The parameter statistics in this text are based on 21 products, mostly synthetic peptides with some fermentation peptides, and cannot represent every peptide product; the slope and duration ranges are a starting point for design, not a specification.
  • The seven structural classes are divided by separation difficulty, and one product may fall into two classes at once (both a disulfide peptide and containing D-amino acids, for example); in that case the separation handle for the first step should be set by the impurity present at the highest level or with the strictest limit.
  • The grades listed are starting points matched on parameters and do not constitute a process recommendation for any particular product; actual selection must take account of the properties of the crude, the equipment available and the regulatory requirements, and be confirmed at bench scale.
  • The pentafluorophenyl phase is not in the current Daisogel range; what is said about it here comes from published literature and one instance in the preparative records, and it can go through a bonded phase customization assessment if required.

AppendixPrincipal source categories

CategoryNotes
Preparative record summaryMobile phase systems and elution gradients for 59 preparative steps across 21 products. Only the system distribution and parameter ranges are published here; complete methods for individual products are not, and no specific condition is tied to any specific product
Process parameters by structural classStationary phase, mobile phase, gradient, flow rate and column temperature, loading and key control points, compiled for the seven structural classes
Manufacturer product dataPore size, particle size, pore volume, surface area, carbon content, pH range, metal impurity limits and coding rules as stated in the Daisogel catalogue
Published textbooks and reviewsCommon practice for reversed phase, ion exchange, HILIC and size exclusion in peptide separation
Existing content on this siteChromatographic Silica FundamentalsColumn FundamentalsDAC Packing SupportPharmacopoeia

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