FPLC chromatography: pressure class, resins and methods
Fast protein liquid chromatography is a separate instrument class from analytical HPLC for two reasons that are easy to overlook: the flow path is biocompatible, because stainless steel and proteins interact badly, and the pressure class is low, because the soft resins that separate proteins collapse under pressure. This page covers specifying one and building methods it can run alone.
- the absorbance the run is followed on, beside conductivity and pH
- 280 nm
- the flow path that separates this instrument class from analytical HPLC
- biocompatible
- the electronic records rule covering the system's run record
- Part 11
Figures in this panel are the detection convention and the flow path property that define the instrument class, with the records rule the run is kept under, linked in the sources below. They are identifiers, not prices: BioBricks publishes verified prices for synthesis services only, and does not imply an instrument price index it has not measured.
- 4 vendor service pages verifiedevery figure matched verbatim to the vendor's page
- Quoted and dated, never estimatedlast verification pass 2026-08-24
- 1 service classes coveredeach with measured search demand behind it
Specifying and running the system
- Insist on a biocompatible flow path. Titanium and polymer wetted parts rather than stainless steel, because iron surfaces adsorb and can oxidise proteins, and because the high salt buffers used here corrode steel. This is the property that distinguishes the instrument class more than any performance figure.
- Match the pressure class to the resins you will use. Agarose and other soft resins compress at pressures an analytical system generates routinely. A protein system runs at a few bar to a few tens of bar, and a column compressed once does not recover.
- Monitor absorbance, conductivity and pH together. Absorbance at two hundred and eighty nanometres follows the protein; conductivity tells you the gradient was actually delivered; pH tells you the buffer system is doing what the method says. A run followed on absorbance alone hides the two commonest failures.
- Build the whole train as one method. Capture, a loop, and a polishing size exclusion step chained in one method removes the overnight gap where an acidic eluate sits and aggregates. That chaining is the single largest recovery gain automation offers on a protein purification.
- Set the safety limits before the first unattended run. A pressure alarm at the column's specification rather than the pump's, an air sensor on the inlet, and pause rather than continue on alarm. Most overnight column losses are an emptied buffer bottle or a blocked frit that the system pushed through.
Each FPLC column as a managed asset
Number every column, log cycles and back pressure, clean it with a documented procedure between proteins and store it in the specified solution. Carryover between two constructs on a shared affinity column is real and is exactly what a later analysis finds and nobody can explain.
Watch back pressure at constant flow over a column's life. A rising trend is a bed approaching the end of its useful life, and replacing it on schedule is cheaper than losing a batch to it.
Buffers, and the volume nobody plans for
Protein purification consumes buffer in litres, and preparing it, filtering it and degassing it is real laboratory time. At pilot scale the buffer hold area becomes a constraint on the process design itself.
Prepare fresh, filter, label with composition and date, and do not top up a bottle. Microbial growth in aqueous buffer blocks frits and adds baseline noise, and it is entirely preventable.
What the run record should carry
The chromatogram with every trace, the method as executed, the column identity and cycle number, the buffer lots and which fractions were pooled under which rule. That set makes a purification reproducible and an anomaly diagnosable a year later.
Define pooling as a rule in the method rather than by eye in the morning. Automated pooling on absorbance thresholds is reproducible between batches; a person deciding is not.
Preparative and analytical systems answer different questions
One system is built to recover material in a usable state: moderate pressure, biocompatible flow path, large injection volumes, fraction collection and buffers at physiological conditions. The other is built to measure: high pressure, small volumes, sharp peaks and a detector optimised for quantification.
They overlap enough to confuse a purchase and not enough to substitute. A laboratory purifying protein and then analysing it needs both, and buying one to do both ends with material that is either poorly recovered or poorly measured.
Biocompatibility is a specification
Stainless steel releases ions that damage some proteins and bind others, so protein systems use inert flow paths throughout. Salt gradients at high concentration also corrode a flow path not designed for them, which shortens the instrument's life and contaminates the product.
Where a purification feeds a sensitive downstream assay or a regulated product, the wetted materials are part of the specification and belong in the purchase decision rather than being discovered afterwards.
Disposable chromatography columns, and where they fit
A prepacked single use column removes packing, cleaning validation and the cross contamination argument, and it is the default at clinical scale and for multi-product facilities. What it costs is a consumable per batch and a supplier qualification, since the resin's own lot and the packing quality are now someone else's process under their change control. Ask for the column's own qualification data, the acceptance criteria on bed integrity, and how a batch of columns is released, because a badly packed column is a failed step you paid for.
normal phase vs reverse phase chromatography, decided by solubility
Reverse phase runs a non-polar phase with a polar eluent and retains by hydrophobicity, which covers most small molecules and peptides. Normal phase inverts both and retains by polarity, which is what separates positional isomers, lipids and compounds that will not dissolve in water. The sample decides: solubility first, then whether the separation you need is by polarity or by shape. Normal phase also costs solvent handling and longer equilibration, since traces of water move retention noticeably.
downstream purification, and the order of the train
Downstream processing runs in a fixed order for a reason: clarify to remove cells and debris, capture to bind the product out of a large dilute volume, one or two intermediate and polishing steps to remove what capture could not, and a final concentration and buffer exchange into formulation. Each step should reduce volume or impurity, ideally both, and each costs yield, which is why three well chosen steps beat five. Design it from the impurity profile rather than from a list of available resins.
simulated moving bed chromatography, and what continuous buys
Simulated moving bed operation connects several columns in a loop and moves the inlet and outlet ports around it, so a binary separation runs continuously with the feed entering all the time and two product streams leaving. It uses far less solvent and far less resin per kilogram than repeated batch injections, which is why it carries large chiral and sugar separations. The costs are the control system, a process that has to be modelled rather than scaled by arithmetic, and a validation of a steady state instead of a batch.
A dialysis bag, and when dialysis beats a column
Dialysis exchanges buffer through a membrane by diffusion, slowly and gently, with no dilution and no surface for the protein to stick to, which is why it holds up for fragile material and for removing small molecules such as imidazole or a reducing agent overnight. Its costs are time and volume: hours to days, and a large bath. A desalting column or a spin concentrator does the same job in minutes with some dilution and some loss to the resin, which is the right trade for a hardy protein in a hurry.
Common questions
- FPLC vs HPLC: what is the difference in protein chromatography?
- Flow path materials and pressure class. Protein systems use biocompatible titanium and polymer wetted parts and run at low pressure to suit soft resins; analytical HPLC uses stainless steel at high pressure for small rigid particles.
- Can I run protein separations on an analytical HPLC?
- For some robust applications on rigid media, yes. For soft resins and for proteins sensitive to metal surfaces, the pressure will compress the bed and the flow path may cost you activity, so the answer is usually no.
- Why monitor conductivity as well as absorbance?
- Because conductivity shows whether the salt gradient was actually delivered. A run that failed because a buffer line ran dry looks like a protein problem on the absorbance trace alone, and the conductivity trace makes it obvious.
- Does the system need to be in a cold room?
- For marginally stable proteins, yes, and many purifications that fail overnight at room temperature succeed cold. A refrigerated cabinet is the alternative where a cold room is not available.
- Can one system purify and analyse protein?
- Poorly. A preparative system is built to recover material intact at moderate pressure with fraction collection; an analytical system is built to measure. A laboratory doing both usually needs both.
Get a shortlist for your project
Browse by service class
Sources
Cite or embed this figure
The median advertised gene synthesis price per base pair in the US research synthesis services market was $0.11 in August 2026, across 4 verified vendor service pages recorded in BioBricks Synthesis Price Index.
Cite as: "BioBricks Synthesis Price Index", updated 2026-08-24, https://biobricks.org/fplc-chromatography/.