From UNIT 6.3
Preparation and Extraction of Insoluble (Inclusion-Body) Proteins from Escherichia
coli
Contributed by Ira Palmer and Paul T. Wingfield
National Institutes of Health
Bethesda, Maryland
--------------------------------------------------------------------------------
High-level expression of many recombinant proteins in Escherichia coli
leads to the formation of highly aggregated protein commonly referred
to as inclusion bodies (UNITS 5.1 & 6.1). Inclusion bodies are normally
formed in the cytoplasm; alternatively, if a secretion vector is used,
they can form in the periplasmic space.
Inclusion bodies recovered from cell lysates by low-speed centrifugation
are heavily contaminated with E. coli cell wall and outer membrane components.
The latter are largely removed by selective extraction with detergents
and low concentrations of either urea or guanidine·HCl to produce
so-called washed pellets. These basic steps result in a significant purification
of the recombinant protein, which usually makes up ~60% of the washed
pellet protein. The challenge, therefore, is not to purify the recombinant-derived
protein, but to solubilize it and then fold it into native and biologically
active protein.
Basic Protocol 1 describes preparation of washed pellets and solubilization
of the protein using guanidine·HCl. The extracted protein, which
is unfolded, is either directly folded as described in UNIT 6.5 or further
purified by gel filtration in the presence of guanidine·HCl as
in Basic Protocol 2. A support protocol describes the removal of guanidine·HCl
from column fractions so they can be monitored by SDS-PAGE (UNIT 10.1).
BASIC PROTOCOL 1
PREPARATION AND EXTRACTION OF INSOLUBLE (INCLUSION-BODY) PROTEINS FROM
ESCHERICHIA COLI
Bacterial cells are lysed using a French press, and inclusion bodies in
the cell lysate are pelleted by low-speed centrifugation. The pellet fraction
is washed (preextracted) with urea and Triton X-100 to remove E. coli
membrane and cell wall material. Guanidine·HCl (8 M) and dithiothreitol
(DTT) are used to solubilize the washed pellet protein. Extraction with
the denaturant simultaneously dissociates protein-protein interactions
and unfolds the protein. As a result, the extracted protein consists (ideally)
of unfolded monomers, with sulfhydryl groups (if present) in the reduced
state.
Materials
E. coli cells from fermentation (UNIT 5.3) containing the protein of interest
Lysis buffer (see recipe)
Wash buffer (see recipe), with and without urea and Triton X-100
Extraction buffer (see recipe)
250- and 500-ml stainless steel beakers
0.22-µm syringe filters (e.g., Millex from Millipore)
20-ml disposable syringe
Additional equipment for breaking cells, homogenizing cells and pellets
and centrifuging at low and high speeds (UNIT 6.2)
Break cells and prepare clarified lysate
Place thawed E. coli cells in a stainless steel beaker. Add 4 ml lysis
buffer per gram wet weight of cells. Keep bacterial cells cool by placing
the beaker on ice in an ice bucket.
The cells can be pretreated with lysozyme prior to lysis in the French
press. Lysozyme treatment involves incubating cells ~20 min at 20°
to 25°C in lysis buffer supplemented with 200 µg/ml lysozyme,
with intermittent homogenization using a tissue grinder. It should be
emphasized that this optional step is carried out before French press
breakage and is not simply an alternative method of cell breakage (compare
the comments made in the annotation to step 4 of UNIT 6.2). Its purpose
is to aid removal of the peptidoglycan and outer membrane protein contaminants
during the washing steps (steps 6 to 9; for further details see UNIT 6.1
and Fig. 6.1.5). An example of this approach is given in Basic Protocol
1 of UNIT 6.5.
Suspend cells using a Waring blender and homogenize using the Polytron
tissue-grinder homogenizer until all clumps are disrupted, as described
in UNIT 6.2, step 3.
Lyse cells with two passes through the French pressure cell operated at
16,000 to 18,000 lb/in2 (with the high-ratio setting, pressure gauge readings
between 1011 and 1135), chilling the cell suspension to 4°C after
each pass, as described in UNIT 6.2, steps 2 and 4.
Reduce the viscosity of the suspension by sonicating 5 min at full power
with 50% duty cycle (on for 5 sec, off for 5 sec) using an ultrasonic
homogenizer, as described in UNIT 6.2, step 5.
Clarify the lysed cell suspension by centrifuging 1 hr at 22,000×g
(12,000 rpm in a JA-14 rotor in a Beckman J2-21M centrifuge), 4°C.
Unbroken cells, large cellular debris, and the inclusion body protein
will be pelleted.
The JA-14 rotor uses 250-ml centrifuge bottles. For processing smaller
volumes the Beckman JA-20 rotor (or equivalent) with 50-ml tubes can be
used, at 13,500 rpm (22,000×g).
The procedure for dealing with insoluble inclusion-body proteins now diverges
from that for purifying soluble proteins (UNIT 6.2).
Prepare washed pellets
Carefully pour off the supernatant from the pellet. Using a tissue homogenizer,
suspend the pellet with 4 to 6 ml wash buffer per gram wet weight cells.
Complete homogenization of the pellet is important to wash out soluble
proteins and cellular components. Removal of cell wall and outer membrane
material can be improved by increasing the amount of wash solution to
10 ml per gram cells.
The concentration of urea and Triton X-100 in the wash buffer can be varied.
The urea concentration is usually between 1 and 4 M; higher concentrations
may result in partial solubilization of the recombinant proteins. The
usual detergent concentration is 0.5% to 5%. Triton X-100 will not solubilize
inclusion body proteins; it is included to help extract lipid and membrane-associated
proteins.
Centrifuge the suspension 30 min at 22,000×g (12,000 rpm in JA-14),
4°C. Discard supernatant and, using the tissue homogenizer, suspend
the pellet in 4 to 6 ml wash buffer per gram wet weight of cells.
Repeat step 7 two more times.
If the supernatant is still cloudy or colored, continue washing the pellet
until the supernatant is clear.
Suspend the pellet with wash buffer minus the Triton X-100 and urea, using
4 to 6 ml buffer per gram wet cells. Centrifuge 30 min at 22,000 x g (12,000
rpm in JA-14), 4°C.
The final wash removes excess Triton X-100 from the pellet.
If necessary the washed pellets can be stored at -80°C. It is better
to store material at this stage rather than after the extraction stage
(see comments to step 13).
Extract recombinant protein from washed pellets with guanidine·HCl
Using the tissue homogenizer, suspend the pellet with guanidine·HCl-containing
extraction buffer. Use 0.5 to 1.0 ml buffer per gram wet weight of original
cells if the extract will be subjected to gel filtration, and 2 to 4 ml
buffer if the extract will be used in protein folding procedures. Perform
this step at room temperature.
To estimate the amount of recombinant protein in the washed pellets, use
the following guidelines. (1) An expression level of 1% corresponds to
~1 mg recombinant protein per 1 g wet cells. (2) The recovery of highly
aggregated recombinant protein in the washed pellets is ~75% that originally
present in the cells. (3) About 60% of the total washed pellet protein
is recombinant-derived. Thus, if 50 g cells is processed and the expression
level is 5%, the washed pellets contain ~200 mg recombinant protein.
The total amount of recombinant-derived protein in washed pellets can
be directly determined by measuring the total protein concentration or
by analyzing the washed pellets via SDS-PAGE (see Support Protocol and
UNIT 10.1) to determine the proportions of the protein constituents.
For gel-filtration purposes, the pellets from 50 g wet weight E. coli
cells are solubilized with 40 to 50 ml extraction buffer (see Basic Protocol
2); the concentration of recombinant protein in the extract will be 4
to 5 mg/ml. For direct protein folding (UNIT 6.5), the pellets are extracted
with 100 to 200 ml buffer, and the concentration of recombinant protein
1 to 2 mg/ml. If the washed pellet is heavily contaminated with outer
cell wall and peptidoglycan material, the extract must be diluted further
with extraction buffer (usually 1:1 to 1:3) to reduce the viscosity before
it can be used for chromatography.
Centrifuge the suspension 1 hr at 100,000×g (30,000 rpm in Ti45
rotor in a Beckman Optima XL-90 ultracentrifuge), 4°C.
For volumes <250 ml the Beckman 70Ti rotor (capacity 6× 39 ml)
can be used at 32,000 rpm (~100,000×g).
Carefully pour off the supernatant from the pellet. Filter the supernatant
through a 0.22-µm syringe filter attached to a 20-ml disposable
syringe.
The filter removes unpelleted large cell wall debris that will clog most
chromatography columns.
Use the clarified inclusion body extract for preparing folded protein
(UNIT 6.5) or purify further by gel filtration (see Basic Protocol 2).
The extract can be stored at -80°C until required. Freeze in plastic
(or polyethylene) containers rather than glass. Divide sample into 10-
to 20-ml aliquots instead of freezing in one large lot and fill containers
to only 50% to 75% capacity.
--------------------------------------------------------------------------------
Table 6.3.1. Gel-Filtration Matrices Suitable for Use with Solutions Containing
Guanidine Hydrochloride
--------------------------------------------------------------------------------
Matrixa Mass range (kDa)
--------------------------------------------------------------------------------
Native proteins Unfolded proteinsb Reference
--------------------------------------------------------------------------------
Sepharose L-6B 10-4,000 1-80 Mann and Fish (1972)
Bio-Gel A-5m 10-5,000 1-80 Mann and Fish (1972)
Sepharose CL-4B 60-20,000 10-300 Mann and Fish (1972)
Sephacryl S-100 HR 1-100 <1-30c --
Sephacryl S-200 HR 5-250 1-50 Belew et al. (1978)
Sephacryl S-300 HR 10-1,500 1-100c --
Sephacryl S-400 HR 20-8,000 1->100c --
Superdex 75 3-70 <1-25 I.P. and P.T.W. (unpub. observ.)
Superdex 200 10-600 <1-80 I.P. and P.T.W. (unpub. observ.)
--------------------------------------------------------------------------------
aAll resins are from Pharmacia Biotech except Bio-Gel A 5m, which is from
Bio-Rad. The Sepharose and Bio-Gel matrices are normally run under low
pressure; all other resins can be run under low or medium pressure. Medium
pressure is achieved using one of the chromatography pumps indicated in
Basic Protocol 2; the pumps are normally included in the Pharmacia Biotech
FPLC or BioPilot systems.
bData on the fractionation range in the unfolded state refer to proteins
unfolded with guanidine·HCI; however, the guidelines also apply
to proteins unfolded and eluted with urea (assuming they are random coils).
cEstimates based on fractionation range for native proteins.
|