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Protein Production & Purification

Michael Jeltsch

Practical course in protein purification (DPDR-305) &�Introduction to Cell and Molecular Biology�Methods (PROV-004)

Autumn term 2025/Spring term 2026

Protein purification

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Why to produce your own protein?

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  • Because nobody produces it.
  • Because it’s too expensive to buy it.
  • Because the commercial protein is bad quality.
  • Because you want to sell it.

Example VEGFR-3/Fc fusion protein (VGX-300/OPT-302/sozinibercept)

Commercial: For 50 µg (R&D Systems) $421

Selfmade: For 50 mg total costs excl. equipment ~$500 (vs. $421,000)

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The big picture

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(Incomplete) decision tree for protein production & purification

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Classification of expression systems

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Different types of expression

  • Stable expression
  • Nonviraldelivery
  • Inducible expression
  • Constitutive expression
  • Viraldelivery
  • Transient expression

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Different expression hosts

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  • BacteriaE. coli, Bacillus subtilis,Lactococcus, Pseudomonas
  • YeastSaccharomyces cerevisiae, Pichia pastoris
  • Insect cellsDrosophila (Schneider S2), Sf9, High5
  • Chemical Protein Synthesis
  • Cell-free expression
  • Mammalian cells

HEK293, CHO

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Bacterial expression

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  • Cheap & fast!
  • Some mammalian proteins can be expressed�easily in E. coli (no fancy post-translational modifications).
  • Sometimes 5% activity might be enough (IL-3)
  • Several commercial systems, e.g. pET, pBAD, GST
  • Secreted expression into periplasm is possible if the�protein does not feature too many disulfide bonds.
  • The first biopharmaceutical made with recombinant DNA tech-�nology was E. coli-produced human insulin (Humulin), still available.
  • Distribution of all biopharmaceuticals by expression system (2011):

E. coli

Yeast

Mammalian cells

%

31

15

43 ↑↑

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The lac operon

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  • Mostly relatively short promoters are used (Amp 105bp, EM7 48bp, T7 19bp)
  • No polyA, but other termination signals (GC-rich palindromes + polyT stretch)

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The lac operon

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The lac operon

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  • Mostly relatively short promoters are used (Amp 105bp, EM7 48bp, T7 19bp)
  • No polyA, but other termination signals (GC-rich palindromes + polyT stretch)

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More stringent control of expression: λDE3 strains

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E. coli DE3 strains are infected with a mutant λ virus (which cannot lyse the cell, but is integrated in the host genome).

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More stringent control of expression: Uninduced

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More stringent control of expression: Induced

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Bacterial expression

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  • Special E. coli strains for expression of proteins (protease-deficient): BL21, BL21(DE3) or BL21(DE3)pLysS�DE3 = T7 RNA polymerase under lacUV5/lacO control (genomic)�pLysS = T7 lysozyme, which inhibits T7 RNA polymerase
  • Many other systems with tighter regulation
  • Constitutive expression: EM7 promoter for non-toxic proteins
  • GOI up to 50% of total cell protein
  • Solubility: inclusion bodies (partially predictable,�main factor: charge)
  • Increasing the solubility: MBP (maltose binding protein)- or�GST (gluthathion-S-transferase)-tag; low temperature growth
  • Inclusion bodies can be useful for purification if they can be solubilized and refolded!

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Inducible expression in eukaryotic cell culture: Tet-On® system

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Dox (Tet-On, Clontech; T-Rex, LifeTechnologies), IPTG (LacSwitch, Agilent), Edcysone (Complete Control, Agilent), Mifepristone (GeneSwitch, LifeTechnologies), RSL1 (RheoSwitch, NEB), Cumate (Cumate gene switch), Me2+ (methallothionine promoter)...

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Yeast

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Yeast

  • Can be sometimes an alternative...
  • VEGF-C produced in yeast is active, while its closest homolog VEGF-D is inactive (glycosylation issue)

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Eukaryotic gene organization

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The Kozak sequence

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Efficient eukaryotic initiation requires a good Kozak sequence!

Marilyn Kozak used mammalian sequences! Insect cells, yeast, etc. have divergent initiation preferences (although the purin preference at -3 seems universal)

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To intron or not to intron

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  • Introns can increase expression levels and are included in some vectors (typically before the MCS)
  • Splice donor and splice acceptor sites are weakly defined, risk to activate „cryptic“ splice sites or to generate them de-novo
  • Can be checked, e.g. at http://spliceport.cbcb.umd.edu/

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To intron or not to intron

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Promoter choice

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  • Constitutive vs. inducible promoters
  • Promoter are species and cell-line specific (due to specific transcription factor binding sites)
  • To bypass this restriction, mostly viral promoters (which use general and virally encoded transcription factors) are used that function in most cell lines

Qin et al. (2010) Systematic Comparison of Constitutive Promoters and the Doxycycline-Inducible Promoter. PLoS ONE 5(5): e10611.

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PolyA signal

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polyA signal

  • Important for mRNA export from nucleus, mRNA stability and recruitment of ribosomes
  • Not as species-specific like promoters
  • In bacteria, polyadenylation promotes mRNA degradation.
  • No absolute requirement

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Insect cells

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Comparatively few insect cell lines:

  • Schneider S2 (Drosophila melanogaster)
  • Sf9, Sf21 (Spodoptera frugiperda)
  • Hi5 (BTI-TN-5B1-4, Trichoplusia ni)

Spodoptera frugiperda (fall armyworm)

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Commonly used insect cell expression systems

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Insect cell expression

Baculovirus

Stable transfection

Transient transfection

Drosophila S2 cells

Drosophila S2 cells

Sf9 cells

Hi5 cells

BmNPV:

Bombyx mori (both cells and larvae)

AcNPV:

Sf9,Sf21

Hi5

Bac-to-Bac®*

DES*

InsectSelect™*

*Invitrogen/LifeTechnologies/ThermoFisher

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Good to remember...

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  • Mammalian promoters (CMV, SV40, EF1α) do not work in insect cells! Special insect cell plasmids are needed. Baculoviral promoters do not work in S2 cells and S2 cell promoters do not work in Sf or Hi5 cells!
  • For secreted proteins: Mammalian signal peptides may or may not work!
  • Baculoviruses require class 1 biosafety level (they do efficiently infect mammalian cells, hence they are considered as gene therapy vectors)
  • Typically 3-4 weeks from ready construct to protein expression
  • Transfection of insect cells is not as straightforward as transfection of mammalian cells; fewer well-performing transfection reagents on the market than for mammalian cells (e.g. Qiagen's Effecten)
  • Insect cells don't need CO2-incubators and can be grown at RT!
  • Selection of stable cell lines is usually done without clonal isolation.

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Mammalian expression systems

  • Mostly stable cell lines are used:CHO (Chinese Hamster Ovary) cells, ~90% of all biopharmaceuticals293 HEK (Human Embryonic Kidney)
  • Transient transfection works as well (and is faster, but costs for transfection reagents become prohibitive)

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Production of recombinant proteins in mammalian hosts

  • Typical product titre: ~50mg/l (1986) vs. 4.7g/l (2004)
  • Sources of improvement:a) Cell density is 4-5x higher due to medium & fermentation optimization(e.g. roller-bottles vs. fermenter), host cell engineeringb) Production phase is 2-3x longer due to host cell engineering andfermentation optimizationc) Specific productivity is 5-10x higher due to HT screening, host-cellengineering (site-specific integration, protein folding and posttranslationalmodification enhancements)
  • Original CHO system1,2 has no IP issues, therefore it is still frequentlyused!

1. Kaufman, R et al. (1985) Coamplification and coexpression of human tissue-type plasminogen activator and murine dihydrofolate reductase in CHO cells. Mol Cell Biol 5, 1750-59.

2. Kingston RE et al. (2002) Amplification using CHO cell expression vectors. Curr Protoc Mol Biol Chapter 16: Unit 16.23.

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Enemies of physical stability

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Heat

pH

→ Denaturation/Aggregation

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Enemies of physical stability

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Why does the egg white denaturate despite no pH and temperature change?

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Enemies of physical stability: phase transitions

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Enemies of physical stability

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How to treat antibody solutions�(and generally proteins) in the lab

  • Temperature: Keep on ice!
  • pH: Never change the pH* (e.g. by diluting into a buffer with a different pH)!
  • Phase transitions: Avoid freezing and thawing! Avoid making bubbles when pipetting!

* and if you MUST do it, test it out on a small aliquot!

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Tricks to increase protein expression levels

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Possible protein concentrations in conditioned cell culture medium have been constantly rising: ~50mg/l (1986), 4.7g/l (2004), ~10g/l (2019)*

  • Higher cell density (medium and fermentation optimization, host cell engineering)
  • Longer production phase (host cell engineering, fermentation optimization)
  • Specific productivity (HT screening, host cell engineering, site-specific integration)

  1. Gene amplification systems (MTX, GST)
  2. Targeted integration
  3. Improved vectors
  4. Genetically engineering host cells (e.g. antiapoptotic, capacity for post-translational modification)
  5. Better screening methods
  6. Media optimization
  7. Better culture conditions (“process development innovations”)

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Cell line development

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The MTX gene amplification system

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The MTX gene amplification system

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From inoculation to harvest

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Cells don’t like to grow alone!

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Bioreactor types and operation modes

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Different operation

modes:

  • Batch: Inoculate final culture with cells. Done.
  • Fed-batch: Inoculate final culture with cells, but keep adding nutrients/medium during production (mostly glucose)
  • Continuous feed: Inoculate final culture with cells, add continuously medium during production and withdraw continuously medium & cells for purification.

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Bioreactors

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High-tech bioreactors do not necessarily result in higher yields compared to shaker flasks!

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cGMP facilities

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Pharmaceutical protein

Product

Cell line

Application

Retail price per kg

Rituximab

CHO

Lymphoma

$9,500,000

Eculizumab

NS0 (murine myeloma)

Paroxysmal nocturnal hemoglobinuria

$23,000,000

Recombinant human growth hormone

E. coli

GH deficiency

$137,000,000

rFVIIa

CHO

Hemophilia with antibodies against rFVIII

$2,070,000,000

rHepatitis B Surface Antigen

S. cerevisiae

Vaccine

$5,400,000,000

rFVIII

CHO

Hemophilia

$9,600,000,000

Industrial protein

Product

Cell line

Application

Retail price per kg

Cellulase

T. reesei

Fuel ethanol

$10

rβ-Glucosidase

E. coli

Fuel ethanol

$37

Retail pricing of recombinant proteins. rFVIIa—recombinant activated factor VII; rFVIII—recombinant factor VIII (https://doi.org/10.3390/pr7080476).

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cGMP facilities

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  • Recouping the development costs�(17% of revenue versus 2% average for a S&P500 company)
  • Clinical phase 3 trial costs: ~$41k per patient (https://aspe.hhs.gov/system/files/pdf/77166/rpt_erg.pdf)
  • Safety issues: keeping the culture contamination-free�(disposable bioreactors for up to 4000l, example of severe drug shortage due to contamination: Cerezyme for Gaucher disease)
  • Purity requirements for the end product and the starting material�(also for trivial chemicals such as water)
  • Quality control & regulatory oversight

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Purification of antibodies

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FC region

Bacterial

surface

proteins:

  • Protein A
  • Protein G
  • Protein L

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Purification of antibodies

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Species

Immunoglobulin

Protein A

Protein G

Protein L*

Human

lgG1

++++

++++

++++

lgG2

++++

++++

++++

lgG3

-

++++

++++

lgG4

++++

++++

++++

lgM

-

-

++++

lgA

-

-

++++

lgE

-

-

++++

Mouse

lgG1

+

++++

++++

lgG2a

++++

++++

++++

lgG2b

+++

+++

++++

lgG3

++

+++

++++

Rat

lgG1

-

+

++++

lgG2a

-

++++

++++

lgG2b

-

++

+

lgG2c

+

++

++++

Goat

lgG

+/-

++

-

Rabbit

lgG

++++

+++

+

Sheep

lgG

+/-

++

-

*Protein L binds only antibodies that contain the a subset of kappa light chains: human VκI, VκIII and VκIV (but not to VκII), mouse VκI.

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Purification of antibodies

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Polishing

  • Size-exclusion chromatography�(ideal for research but does not scale well since it requires a low Vsample/Vcolumn)
  • Ion exchange
  • “Mixed-mode resins” (e.g. hydroxyapatite:�ion exchange & hydrophobic�interaction)

Capture

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Intellectual property

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  • Many advances are kept proprietary (trade-secrets) and are not patented.
  • Other systems have been commercialized (i.e. are not available for academic research due to budget limitations).
  • Startup companies sometimes prefer old-fashioned systems, which are free from intellectual property rights.

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Expression of two or more genes from one plasmid

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GOI 1

GOI 2

Promoter 1

Promoter 2

GOI 1

GOI 2

Promoter

IRES

GOI 1

GOI 2

ATG

CTG

Promoter

internal ribosome entry site (IRES)

Ratio of expression between GOI1 and GOI2 can be regulated: IRES < cap-dependent translation, CTG << ATG

GOI 2

Promoter

2A element*

GOI 1

G↔A

non-AUG initiation

GOI 2

Promoter

intronic expression

intron

GOI 1

Prom.

intron

intron

intron

GOI 2

Promoter

„protein intron**“

intron

GOI 1

modified intein

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Comparison of expression systems

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Characteristics

Bacteria

Yeast

Insect cells

Mammalian cells

Cell cycle

very fast

fast

slow

slow

Cost of growth medium

low

low

high

high

Expression level

high

low - high

low - high

low - moderate

Secreted expression

to periplasm

yes

yes

yes

Posttranslational modifications

Protein folding

refolding often required

refolding rarely required

mostly proper folding

proper folding

cysteine bond formation

in periplasm (1)

yes

yes

yes

N-linked glycosylation

no (2)

high mannose type

simple, no sialic acid (3)

complex

O-linked glycosylation

no (2,4)

yes

yes

yes

Phosphorylation

no (2,4)

yes

yes

yes

N-terminal acetylation (protein stability)

no (5)

yes

yes

yes

Acylation

no

yes

yes

yes

γ-carboxylation (blood clotting cascade)

no

no

no

yes

1 except for modified strains, 2 under development, 3 except for Sf9 mimic™, 4 with exceptions, 5 yeast-NatB-transgenic E. coli

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Producing antibodies in the lab and in industry

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Why are hybridomas not used to produce antibodies in large scale?

  1. They are all initially inherently unstable (because they have a duplicate set of chromosomes); most of them stabilize after prolonged culture.
  2. Due to a), hybridomas are all a bit different from each other.

Antibody production workhorse: CHO (Chinese Hamster Ovary) cells

  1. Fast growth
  2. High protein production
  3. Can be grown as adherent and suspension cultures
  4. Mutant lines for cell line selection and amplification systems to increase protein production: Dhfr-negative CHO cells (e.g. CHO-DG44, evolution of CHO cells role in cell line development)

Why not to use transgenic animals to produce antibodies (e.g. sheep and goats who produce it in the milk)?

Making a CHO cell line takes about 6 weeks. Making a transgenic goat takes about 2 years (and establishing a trip of transgenic goats takes several years).

Why are animal cells used and not human cells?

Human cells have been/are used (e.g. HT-1080 for making Epo). However, there is concern about human viruses. Most human viruses do not propagate in rodent cells (see e.g. the vesivirus case).

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Methods & Tags

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Questions, contact

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