Design and purification of proteins Biotechnology project, 18/05/09
Marielle Brockhoff, Aurore Lacas , Raphael Lieberherr Sebastian Olényi, Morgane Perdomini, Zrinka Raguz,
Protein functions ØTransport (O2) ØRecognition (antibodies) ØStructure/Architectur e ØCatalysis (enzymes) ØCommunication (hormon)
insulin production
ORGAN
ORGANIS M
Islet of Langerhans
TISS UE
FUNCTIONS INFORMATION DNA
CELL (and NUCLEUS)
genetic information of insulin DNA
≈ Book
CHROMOSOME 11
≈ Chapter
Insulin GENE
≈ Sentence
CODON
.A . … .
C G T
G T A
≈ Word 469 letters CG AT
from dna to insulin - DNA -
Codon
C GA T
- Insulin -
Gl y
Ile
Va l
Gl u
Gl n
Cy s
Protein = succession of amino acids
Posttranslational modifications As p
Hi s
Th r r
Th r
S
e
r
A
Insulin correctly folded
g
Protein structure Primary structure
Secondary structure
Tertiary structure
Quaternary structure
Insulin Structure 469 letters 156 amino acids 51 amino acids. two chains linked by disulfide bonds
Insulin function Transport
of glucose requires insulin ØType 1 diabetes ØType 2 diabetes
http://www.lillydiabetes.com/content/how-insulin-works.jsp
Protein Design
Making entirely new or modifying proteins for example as drugs
Protein factories: From bacteria to banana
Different advantages
Different modification techniques
Bacteria: viral transformation, artifical competence (chemicals, electroporation) Plants: Agrobacterium, particle bombardment, electroporation, viral transformation Humans, Animals: Chemistry, heat shock, electroporation, viral transformation
Recombinant DNA Technology in the Synthesis Since 1921: Treatement with insulin derived from animals Bovine & porcine insulin slightly different from human insulin Sometimes inflammation at injection sites Fear: long term complications Solution: Inserting insulin gene into E.coli to produce identical human insulin using Recombinant DNA Technology
Manufacturing synthetic human insulin
Synthesis of the DNA containing the nucleotide sequences of the A and B polypeptide chains of insulin
Manufacturing synthetic human insulin Plasmid
Plasmid + restriction enzyme
Insertion of the insulin gene into plasmid (circular DNA) Restriction enzymes cut plasmidic DNA DNA ligase agglutinates the insulin gene and the plasmidic DNA
Plasmid + insulin gene
Manufacturing synthetic human insulin
Introduction of recombinant plasmids into bacteria: E. coli E.coli = factory for insulin production Using E. coli mutants to avoid insulin degradation Bacterium reproduces the insulin gene replicates along with plasmid
E. Coli
Manufacturing synthetic human insulin
Formed protein partly of a byproduct the A or B chain of insulin
Extraction and purification of A and B chains byproduc
byproduc
Insulin A-chain
Insulin B-chain
Manufacturing synthetic human insulin
Connection of A- and B-chain Reaction: Forming disulfide cross bridges Result: Pure synthetic human insulin
Insulin production Today
Yeast cells as growth medium Secretion of almost complete human insulin Minimization of complex and purification procedures
Yeast
Insulin
Protein purification Definition Protein purification is a series of processes intended to isolate a single type of protein from a complex mixture of proteins
The applications of purified proteins
Degree of purity Depends on the application of the protein!!! Industrial
applications: not so strict… Food and pharmaceuticals high
level required, >99.99% Degree is set by the FDA (Food and Drug Administration)
Properties of proteins used for the purification Differences in proprieties allow a separation of different proteins Properties come from
Amino acids composition Amino adic chain length Structure/shape of the protein (folding of the amino acid chain)
Properties of proteins used for the purification I.
Size
Properties of proteins used for the purification I.
Size
I. s II. Charge
++ - +-- +- ++ +++ - - -++ + + + - + +
+
o
-
Properties of proteins I. S used for the purification II. .
III. Solubility: pH, T, [Salt]
-+
-+
-+ -+
-+ + Salt
-+ -+
-+
I. S Properties of proteins II. . used for the purification III. . IV. Hydrophobicity
I. S Properties of proteins II. . used for the purification III. . IV. Hydrophobicity I. II. III. IV.
S . . .
V. Specific binding proprieties
Protein Purification Protein Location intracellular: sonication extracellular Purification: concentrate proteins, seperate proteins Filtration and chromatography
Index - Filtration - Gel Filtration - Ion Exchange chromatography - Affinity Chromatography
Ultra Filtration Use: concentration, desalting of proteins, change buffer Membran: Pore size = 10-5 -10-2mm² Dialysis
Chromatography Purification using specifique protein properties, as: size, charge, hydrophobicity or biorecognition Stationary phase: inert material, or coated material Mobile phase: buffer
Gel Filtration Mild conditions (according to protein) With any buffer Isocratic Porous matrix in the spherical beads Small proteins diffuse into pores, stay longer
Ion Exchange Chromatography IEX Net surface charge According to pH and the number and exposure of amino acids Charge = 0 at pI pH > pI protein – pH < pI protein +
Steps in IEX Matrix with bound groups that are charged Equilibration: adjust pH in order that protein of interest binds to column Elution by changing the ionic strength or the pH Proteins with highest charge elute latest
Affinity chromatography One step Specific binding between protein and ligand (eg substrate, substrate analogue, inhibitor, cofactor) His tag binds to metal ions
Poly His Tag Commonly used for recombinant proteins Ni2+ binds (His)6
Eluting with imidazole
Insulin purification Extraction (separation of Bacteria/Yeasts) Purification (separation of other proteins) : Cation exchange chromatography OD measurement Precipitation with Zinc
Insulin extraction Secretion of insulin in medium: add sequence to insulin gene Clarification of culture medium: isopropanol added to medium, centrifugation and filtration
Bacteria
CENTRIFUGATION
Medium
get rid of Bacteria/Yeasts
Medium with insulin
Insulin Purification Ex:
Cation exchange Chromatography, SP Sepharose Fast Flow Resin –CH2SO3 Total
ionic capacity: 180-250μmol/ml gel Recommended flow rate: 100-300 cm/h Particle size range: 45-165 μm Working pH range: 4-13 Maximum temperature: 30°C
Cation exchange Chromatography Resin Regeneration: 0.5N NaOH => resin is clean Equilibration: 20mM sodium citrate buffer at pH 4.0 => fixation Na+ Mix with insulin diluted with 20mM citrate buffer at pH 4.0 => positively charged Loading of column and flow rate of 200cm/h => fixation of insulin
•CH2
X
REGENERATION
SO3-
Y
resin
EQUILIBRATION
•CH2
Na+
ADD MIX
•CH2
SO3-
+
SO3-
Na+
insulin
+
+
Cation exchange Chromatography Washing: 20mM citrate buffer => elimination of molecules not fixed Elution: 100mM tris HCl, pH 7.5 buffer, flow rate of 100cm/h => replacement of insulin by H+
•CH2
+ •CH2
SO3-
+
Low HCl concentration
+
ELUTION
SO3-
•CH2
+H
SO3-
+
+H
Fraction with buffer and no insulin
Fraction with insulin
Determination of fractions containing insuline OD 280nm Aromatic amino acid absorb at 280nm => detection of protein presence in solution A= εlC ε280nm=0.55 x 104 M-1cm-1
Phenylalanin
Tryptophan
Tyrosin
Precipitation with Zinc Add ZnCl2 to purified insulin and adjust pH to 6 => precipitation Refrigerator (8 °C) for at least 6h Centrifugation 5000rpm Drying of pellet => dry insulin
Yield for ion exchange chromatography and precipitation: around 75%
CONCLUSION Production
of proteins is a big market Example: Lilly Insulin production since 1923
Nessecity
of good design and purification protocol
Thank you for your attention Questions?