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Int. J. Biomol. Biomed.
Jayanth et al
1
RESEARCH PAPER OPEN ACCESS
Cloning and expression of Human glutamic acid decarboxylase
(GAD 65) gene in Escherichia coli
Meghana Kolavalli Jayanth, Paramanahally Hanumanthe Gowda Ramanjini Gowda,
Neha Guleria*, Satish Kumar Kariyaiah
Department of Plant Biotechnology, University of Agricultural Sciences, GKVK, Bangalore, India
Key words: Diabetes mellitus, GAD65, SDS-PAGE, Western blot.
Article Published: 31 August 2016
Abstract
Diabetes is a chronic autoimmune disease characterized by the inability of body to produce or respond to insulin
a hormone required by body to burn glucose for energy. Type I Diabetes mellitus, also known as Insulin
Dependent Diabetes mellitus is a most frequent chronic disease of childhood, afflicts 0.2-0.3% of human
individuals due to auto immune destruction of insulin secreting pancreatic β cells. GAD65 is the major auto
antigen in Insulin Dependent Diabetes Mellitus (IIDM). Thus, this project is aimed at expression of GAD65 in E.
coli. GAD65 gene was cloned into pET-28a bacterial expression vector and expression was studied in BL21 DE3
cells. Different parameters of induction like isopropyl-β-D-thiogalactopyranoside (IPTG), temperature, time
interval were standardized. The recombinant clones induced with 2 μM of IPTG at 30oC for 4 h at flask level
produced the protein upto 537μg/ml. Furthermore, the specificity of the purified recombinant protein was
confirmed by western blot analysis using monoclonal antibodies. This work establishes a strategy in E. coli for the
expression of GAD65 with optimized parameters.
*Corresponding Author: Neha Guleria  neha.gul5@gmail.com
International Journal of Biomolecules and Biomedicine (IJBB)
ISSN: 2221-1063 (Print), 2222-503X (Online)
http://www.innspub.net
Vol. 5, No. 2, p. 1-8, 2016
Int. J. Biomol. Biomed.
Jayanth et al
2
Introduction
Diabetes mellitus is a disease or disorder that is
gaining importance and increasing at the alarming
rate, which is also called as hyperglycemia where the
blood glucose level is higher than the normal.
According to World Health Organization, there are
mainly two principle types of diabetes; Type 1
diabetes (juvenile or insulin dependent diabetes) and
type 2 diabetes (insulin independent diabetes).Type
1diabetes an autoimmune form of diabetic disorder
where the insulin producing β cells of the pancreatic
islets are destroyed. It is commonly seen in children
and the worldwide numbers of prevalent cases of T1D
in children (<15 years) have increased and the
estimates indicate that there are almost 500,000
children aged under 15 years with T1D worldwide
(Patterson et al., 2014). In this type of diabetes, the
autoimmune response occurs against self-antigens
which include insulin, intracellular membrane
proteins such as GAD, IA2, ZnT8 transporter protein
(La Torre and Lernmark, 2010; Wenzlau et al., 2009).
There is currently no cure for T1D and the only
available treatment is insulin therapy. Insulin therapy
can lead to hypoglycemia if the doses are not taken
properly without monitoring blood glucose level and
patients requires two or more injections of insulin
daily which is painful. (Alvarez et al., 2013).In this
regard, GAD65 a major auto antigen have much
potential as an important marker for the prediction,
diagnosis and in the prevention of T1D in humans.
Autoantibodies to GAD65 are observed months to
years before the clinical onset of diabetes and are
present in the sera of 70–80% of patients with T1D
and this anti-GAD 65 antibodies are now serving as
an important marker for the prediction and diagnosis
of type 1 diabetes (Jayakrishnan et al., 2011; Oak et
al., 2011; Wang et al., 2012).
Glutamic acid decarboxylase is an enzyme which is
involved in the production of Gamma amino butyric
acid (GABA) by the decarboxylation of glutamate is
an inhibitory neurotransmitter in neurons and
pancreatic beta cells. This GAD exists in two major
protein isoforms.
One isoform has a molecular size of 65kDa and is
termed GAD 65, while the second one, of 67kDa size,
is termed GAD67 (Towns and Pietropaolo, 2011). The
GAD65 enzyme isolation in large quantities from the
human pancreatic (beta cells) tissue is unrealistic so
the expression of GAD 65 enzyme as a recombinant
protein in heterologous system is mandatory. The
large scale production of GAD 65 enzyme currently
involves the use of baculovirus infected Sf9 insect
cells and methylo-trophic yeast (Mauch et al., 1993;
Moody et al., 1995). However, these expression
system are technically, economically demanding and
highly vulnerable to contamination.
Number of heterologous biopharmaceutical proteins
expressed in E. coli which are at commercial level are
innumerable when compared to all other hosts system
this is because of reasons like, it is inexpensive, offers
rapid culture times and the ability to achieve high
biomass and high protein yields (Assenberg et al.,
2013). E. coli expression system remain to be the first
choice for laboratory investigations, scaling up
activities at commercial level and are useful
benchmark for comparison among various expression
platforms. The sufficient quantity of soluble and
functional recombinant GAD 65 protein is required to
carry out any molecular and immunological studies.
Poor expression of protein because of cellular toxicity
and formation of inclusion bodies are the major
hindrance in recombinant protein expression.
Therefore, this study was carried out for the
optimization of different parameters to enhance GAD
65 protein expression and purification in E. coli.
Materials and methods
Bacterial strains, plasmids and growth conditions
The E. coli strains DH5α and BL21 (DE3) were used
for the cloning and expression experiments. The
expression vector pET-28a used in this study was
purchased from Novogen, USA. The pTNT vector
carrying GAD 65 gene was provided by Ake
Lernmark, Professor, Lund University Sweden. The E.
coli was grown in Luria Bertini Broth (LB) at 37°C
with shaking 200rpm or on LB plates solidified with
1.5 w/v agar.
Int. J. Biomol. Biomed.
Jayanth et al
3
As per the requirement LB broth and agar plates were
supplemented with kanamycin in a final
concentration of 50 mg/L. The GAD 65 gene was
cloned and maintained in pTNT cloning vector.
Bacterial expression vector pET-28a was selected to
express the gene encoding for GAD 65 protein in E.
coli. It contains T7 promoter driven expression of
recombinant proteins with the addition of a 19 amino
acid N-terminal fusion tag containing a 6X His tag
followed by a thrombin protease cleavage site. Two
stop codons are included in the vector at the C-
terminal cloning site with kanamycin resistance
(nptII) gene as selection marker and poly linker
sequence with multiple cloning sites (Fig. 1.). This
vector replicates in E. coli through it sp BR322 origin
of replication. Plasmid DNA was isolated and purified
using QIA prep Miniprep Kit (Qiagen, USA) according
to the manufacturer protocol.
Fig. 1.Vector map of recombinant pET-28a_GAD 65.
Primer designing for the cloning of GAD65 gene
Oligonucleotides primers were designed for PCR
amplification of GAD65 gene. To facilitate the cloning
of GAD 65 gene into the expression vector pET-28a,
NcoI restriction site was inserted in the forward
primer (5’-atatcatg CCATGGCTAGCCCAGGCT-3’)
and XhoI site in the reverse primer sequence (5’- ccg
CTCGAGTAAATCTTGTCCAAGGCG-3’) due to the
absence of the two sites in the GAD 65 gene.
Cloning of GAD65 gene into bacterial expression
vector pET-28a
The GAD 65 gene in the pTNT vector was used as a
template and was amplified with Pfu poly
meraseusing a pair of gene specific primers GAD65
XhoI forward primer and GAD65 NcoI reverse primer
in 50 µL reaction mixture.
The programme is as follows; Initial denaturation at
98°C for 3 minutes followed by 30 cycles of final
denaturation at 98°C for 10 sec, annealing at 60°C for
30 sec and extension at 68°C for 1 min with a final
extension for 7 min at 68°C. The PCR product was
resolved on 1 per cent agarose gel and the 1.75 Kb
GAD 65 gene was eluted from the agarose using
Qiagen gel elution kit. The purified PCR product
(GAD 65 gene) was restriction digested in 50µL
reaction mixture (2µg DNA, XhoI and NcoI).
The bacterial expression vector pET-28a was restriction
digested with XhoI and NcoI. The pET-28avector carries
an N-terminal 6X His tag. The GAD65 gene was cloned
to the upstream of N-terminal coding portion of pET-
28a vector (Fig. 1.).
Int. J. Biomol. Biomed.
Jayanth et al
4
The digested PCR product was ligated into digested pET-
28a vector in 1:3 ratio using T4 DNA ligase enzyme. The
ligated mixture was transformed into E. coli DH5α
competent cells by electroporation as described by Sam
brook and Russel (2001). Transform ants were screened
using 50 mg/l kanamycin selection.
To confirm the recombinant clones, the colony PCR
was done using a pair of gene specific primers.
Further these clones were also confirmed by
restriction digestion with NcoI and XhoI and
confirmed on 0.8% agarose gel.
GAD 65 protein expression
The E. coli BL 21 competent cells were transformed
with confirmed recombinant clone as described by
Sam brook and Russel (2001) and screened using 50
mg/Lkanamycin selection. The single colony was
cultured by inoculating it in 10 mL LB broth
containing kanamycin (50 mg/L) and incubated at
37°C overnight. From the overnight grown culture
one mL was inoculated into 100 mL LB broth to make
1:100 dilution and incubated at 37°C until the OD
reached 0.4-0.6. At this point, different parameters
were used to optimize GAD 65 protein expression in
E. coli i.e., different IPTG concentration (0.1, 0.3, 0.5,
0.7, 1, 1.5, 2.0, 2.5, 3.0 3.5 and 4.0 µM), temperature
(25°C and 30°C) and time interval (4, 8, 12, 16 and 18
h). The cells were harvested by centrifugation at
10000 rpm for 15 min at 4°C.
GAD 65 protein extraction and purification
The harvested cells were suspended in lysis buffer
[(1X PBS,), 7µL PMSF and 1mg/m Llysozyme] and
incubated on ice for 15 min. Cells were lysed by
sonication at 200-300 W for 15 min with alternative
10 sec sonication and 10 sec rest on ice. The cells were
sonicated and pelleted out at 10000 rpm for 10 min at
4°C. The supernatant was collected and subjected for
purification using Ni-NTA agarose column. The
column of Ni-NTA agarose was prepared, equilibrated
and activated with 1X PBS. The column was loaded
with protein sample and flow throw was collected.
The column was washed with 1X PBS to remove
unbound foreign or host proteins. Then the GAD 65
protein was eluted from the column using different
concentration of imidazole (50, 150,250 mM). The
concentration of purified GAD 65 protein isolated
from E. coli BL 21 cell was measured by using
Bradford protein assay (Bradford, 1976).
SDS PAGE and Western blot analysis
The purified GAD 65 protein was analyzed by SDS-
PAGE as per the standard procedure of Lamelli
(1970). The protein samples were prepared by
denaturing the proteins by boiling for 15 min with
SDS loading dye. The protein samples were run on 12
per cent acrylamide gel along with standard protein
marker. Further the expression of the GAD 65 protein
was confirmed by western blot as per the standard
protocol of Tow bin et al., 1979. The protein bands
were transferred from SDS-PAGE gel to activated
PVDF membrane by electro blotting. The unspecific
protein binding sites were blocked with blocking
buffer containing skimmed milk and incubated at
37°C for 1 h. Then the membrane was washed with
PBST and incubated for 1 h at 37°C with GAD65
monoclonal antibody. The binding of the antibody
was visualized using goat antibody antimouse Ig G
conjugate with peroxidase.
Results and discussion
Generation of recombinant clones of pET-
28a_GAD65
The E. coli strain DH5αwas transformed with the
ligation mixture and the recombinants were grown on
kanamycin selection media. The colony PCR resulted
in the amplification of GAD65 gene, amplicon size
~1.75Kb. (Fig. 2.). Further, restriction digestion of
recombinant clones with XhoI and NcoI restriction
enzymes resulted in linearization of pET-28a vector
(~5.23 kb) and the release of the GAD 65 gene
(~1.75Kb). This confirms the proper integration of the
gene into the expression vector. Thereafter, clones are
designated as recombinant clones (Fig. 3.).
Int. J. Biomol. Biomed.
Jayanth et al
5
Fig. 2. Colony PCR of transformed colonies of pET-28 a_GAD 65 gene. M: 1 Kb DNA ladder; lane 1: Negative
control, lane 2: Positive control; lane 3-10: PCR amplicon of GAD 65 gene.
Fig. 3. Confirmation of recombinant pET-28a_GAD
65 gene construct with XhoI and NcoI restriction
digestion. M: 1Kb DNA ladder; Lane 1: undigested
pET-28a vector; lane 2: undigested recombinant pET-
28a GAD65 gene construct; lane 3-4: Restriction
digestedre combinant pET-28a GAD65 construct.
Effect of IPTG concentration on gene expression
Different parameters like IPTG concentration,
induction temperature and length of induction
influences both the solubility and yield of the protein.
For the expression vector pET-28a_GAD 65, the
foreign protein expression was triggered by adding
IPTG into the culture medium. The Fig. 4. showed
overall growth pattern of recombinant clones on
different concentrations of IPTG ranging from 0.1,
0.3, 0.5, 0.7, 1.0, 1.5, 2.0, 2.5, 3.0, 3.5, 4.0 µM.
Although the maximum cell growth was observed at
0.3 to 0.5µ M IPTG.
The optimum growth and maximum expression i.e.
530μg/mL of protein was seen at 2.0 µM IPTG at
30°C after 4 h of induction (Fig. 4.). The decrease in
protein expression after 2 µM IPTG concentration is
may be due to the fact that further increase in IPTG
concentration acts as inhibitory for the bacterial cells.
Lower IPTG concentration, lower temperature with
longer induction time leads to the slower expression
rate of the protein which allows better folding of the
protein but reduces yield. The higher IPTG
concentration with shorter induction time at low
temperature may allow higher properly folded protein
expression which leads to increased yields of protein
(Tolia and Joshua- Tor, 2006). As the GAD 65 gene
was cloned into pET-28a expression vector, it has lacI
promoter which codes for repressor protein and a T7
promoter which is specific to only T7 RNA
polymerase. The control of pET expression system is
accomplished through the lac promoter and operator.
Addition of IPTG displaces the repressor from
the lac operator and induces the expression of T7
RNA polymerase which in turn transcribes the target
gene cloned into the pET-28a bacterial expression
vector system. By adjusting the concentration of
IPTG, expression can be regulated from very low level
expression up to the robust, fully induced expression
levels commonly associated with pET vectors
(German and Eduardo, 2014).
Int. J. Biomol. Biomed.
Jayanth et al
6
Fig. 4. Effect of IPTG concentrations on bacterial cell growth and GAD 65 protein expression.
Effect of different temperature and time interval on
gene expression
The optimum temperature for E. coli growth is 37°C
but induction for recombinant protein expression are
carried out at low temperature to retain the solubility
(folding) of the expressed protein. The recombinant
clones showed maximum growth at 37°C as compared
with the other temperatures. Although the cells grew
well at 37°C but the protein expression was not
maximum at this temperature. At 25°C with 4, 8, 12,
16, 18 h time interval the protein expression was 259,
391, 498, 250 and 245μg/mL respectively while at
30°C with same length of induction period, the GAD
65 protein expression was 537, 436, 319, 298 and 256
μg/mL respectively. Hence, E. coli cells induced at
30°C for 4 h and 25°C for 12 h at 2 μM IPTG
concentration showed the highest GAD65 protein
expression of 537 μg/mL and 498 μg/mL respectively
(Fig. 5.). This may be due to slower expression rate at
25°C when compared to 30°C. The temperature is
known to influence the expression of recombinant
proteins in E. coli. When the temperature decreases,
induction time increases because of reducing culture
temperature usually leads to slower growth of
bacteria and slower rate of protein production (Gong
et al., 2009). The bacterial growth at 37°C causes
some proteins to accumulate as inclusion bodies,
while incubation at 30°C leads to soluble, active
protein (Vera et al., 2007).
Fig. 5. Effect of different induction temperatures and
time intervals on GAD 65 protein expression. The
error bars indicate the standard deviation.
Expression and Purification of GAD 65 protein
After the optimization of the different parameters, the
histidine tag fused GAD 65 protein expressed in E.
coli BL 21 cell was extracted and purified by metal
affinity chromatography. The purification of protein
is essential for any biochemical analysis, therapeutics
or structural studies. The GAD 65 protein samples
were passed through Ni-NTA agarose column and the
optimum elution of GAD65 protein was obtained
when 250 mM imidazole was used. Similar result was
reported by Papouchado et al., (1997) where they
expressed GAD 65 protein as a fusion protein with
thioredoxin which helped in the purification of GAD
65 protein. The purified GAD 65 protein expressed in
E. coli was confirmed by SDS-PAGE where 65 kDa
GAD 65 protein band was observed (Fig. 6A.).
Int. J. Biomol. Biomed.
Jayanth et al
7
Similarly, Rohmah et al., (2013) reported 65 kDa
GAD 65 protein band on SDS-PAGE. This may be due
to the correct expression and proper folding of
GAD65 protein in E coli. Further it was confirmed by
western blotting using monoclonal antibody. The
presence of single 65 kDA protein band on the PVDF
membrane confirmed the expression of GAD 65
protein (Fig.6B.).
This is in line with Papouchado et al., (1997) who
expressed GAD 65 protein in E. coli. The expression
and subsequent purification of recombinant proteins
are widely employed in biochemical and molecular
studies.
A powerful purification method involves the use of
peptide affinity tags, which are fused to the protein of
interest and used to expedite protein purification via
affinity chromatography (Bornhorst and Falke,
2000). Hence, immobilized metal-affinity
chromatography (IMAC) can be used to purify
recombinant proteins containing a short affinity tag
consisting of polyhistidine residues, theoredoxin
residues etc., and the Ni NTA passed protein could
keep its function.
Fig. 6. SDS-PAGE and western blot analysis of recombinant GAD 65 protein expressed in E. coli. (A) Lane M:
Protein ladder; lane 1: Purified protein sample (B) Western blot analysis. Lane M: Protein ladder; lane 1-4: GAD
65 protein samples expressed in E. coli.
In conclusion, the different parameters were
standardized for the expression of GAD 65 protein in
E. coli. The protein produced can be aimed at
developing a diagnostic kit for the prediction of
insulin-dependent diabetes mellitus (Type-1).
Acknowledgements
Authors are highly thankful to the Dr. Ake Lernmark,
Sweden for providing the GAD 65 gene construct.
References
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Bradford MM. 1976. A rapid and sensitive method
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Cloning and expression of Human glutamic acid decarboxylase (GAD 65) gene in Escherichia coli

  • 1. Int. J. Biomol. Biomed. Jayanth et al 1 RESEARCH PAPER OPEN ACCESS Cloning and expression of Human glutamic acid decarboxylase (GAD 65) gene in Escherichia coli Meghana Kolavalli Jayanth, Paramanahally Hanumanthe Gowda Ramanjini Gowda, Neha Guleria*, Satish Kumar Kariyaiah Department of Plant Biotechnology, University of Agricultural Sciences, GKVK, Bangalore, India Key words: Diabetes mellitus, GAD65, SDS-PAGE, Western blot. Article Published: 31 August 2016 Abstract Diabetes is a chronic autoimmune disease characterized by the inability of body to produce or respond to insulin a hormone required by body to burn glucose for energy. Type I Diabetes mellitus, also known as Insulin Dependent Diabetes mellitus is a most frequent chronic disease of childhood, afflicts 0.2-0.3% of human individuals due to auto immune destruction of insulin secreting pancreatic β cells. GAD65 is the major auto antigen in Insulin Dependent Diabetes Mellitus (IIDM). Thus, this project is aimed at expression of GAD65 in E. coli. GAD65 gene was cloned into pET-28a bacterial expression vector and expression was studied in BL21 DE3 cells. Different parameters of induction like isopropyl-β-D-thiogalactopyranoside (IPTG), temperature, time interval were standardized. The recombinant clones induced with 2 μM of IPTG at 30oC for 4 h at flask level produced the protein upto 537μg/ml. Furthermore, the specificity of the purified recombinant protein was confirmed by western blot analysis using monoclonal antibodies. This work establishes a strategy in E. coli for the expression of GAD65 with optimized parameters. *Corresponding Author: Neha Guleria  neha.gul5@gmail.com International Journal of Biomolecules and Biomedicine (IJBB) ISSN: 2221-1063 (Print), 2222-503X (Online) http://www.innspub.net Vol. 5, No. 2, p. 1-8, 2016
  • 2. Int. J. Biomol. Biomed. Jayanth et al 2 Introduction Diabetes mellitus is a disease or disorder that is gaining importance and increasing at the alarming rate, which is also called as hyperglycemia where the blood glucose level is higher than the normal. According to World Health Organization, there are mainly two principle types of diabetes; Type 1 diabetes (juvenile or insulin dependent diabetes) and type 2 diabetes (insulin independent diabetes).Type 1diabetes an autoimmune form of diabetic disorder where the insulin producing β cells of the pancreatic islets are destroyed. It is commonly seen in children and the worldwide numbers of prevalent cases of T1D in children (<15 years) have increased and the estimates indicate that there are almost 500,000 children aged under 15 years with T1D worldwide (Patterson et al., 2014). In this type of diabetes, the autoimmune response occurs against self-antigens which include insulin, intracellular membrane proteins such as GAD, IA2, ZnT8 transporter protein (La Torre and Lernmark, 2010; Wenzlau et al., 2009). There is currently no cure for T1D and the only available treatment is insulin therapy. Insulin therapy can lead to hypoglycemia if the doses are not taken properly without monitoring blood glucose level and patients requires two or more injections of insulin daily which is painful. (Alvarez et al., 2013).In this regard, GAD65 a major auto antigen have much potential as an important marker for the prediction, diagnosis and in the prevention of T1D in humans. Autoantibodies to GAD65 are observed months to years before the clinical onset of diabetes and are present in the sera of 70–80% of patients with T1D and this anti-GAD 65 antibodies are now serving as an important marker for the prediction and diagnosis of type 1 diabetes (Jayakrishnan et al., 2011; Oak et al., 2011; Wang et al., 2012). Glutamic acid decarboxylase is an enzyme which is involved in the production of Gamma amino butyric acid (GABA) by the decarboxylation of glutamate is an inhibitory neurotransmitter in neurons and pancreatic beta cells. This GAD exists in two major protein isoforms. One isoform has a molecular size of 65kDa and is termed GAD 65, while the second one, of 67kDa size, is termed GAD67 (Towns and Pietropaolo, 2011). The GAD65 enzyme isolation in large quantities from the human pancreatic (beta cells) tissue is unrealistic so the expression of GAD 65 enzyme as a recombinant protein in heterologous system is mandatory. The large scale production of GAD 65 enzyme currently involves the use of baculovirus infected Sf9 insect cells and methylo-trophic yeast (Mauch et al., 1993; Moody et al., 1995). However, these expression system are technically, economically demanding and highly vulnerable to contamination. Number of heterologous biopharmaceutical proteins expressed in E. coli which are at commercial level are innumerable when compared to all other hosts system this is because of reasons like, it is inexpensive, offers rapid culture times and the ability to achieve high biomass and high protein yields (Assenberg et al., 2013). E. coli expression system remain to be the first choice for laboratory investigations, scaling up activities at commercial level and are useful benchmark for comparison among various expression platforms. The sufficient quantity of soluble and functional recombinant GAD 65 protein is required to carry out any molecular and immunological studies. Poor expression of protein because of cellular toxicity and formation of inclusion bodies are the major hindrance in recombinant protein expression. Therefore, this study was carried out for the optimization of different parameters to enhance GAD 65 protein expression and purification in E. coli. Materials and methods Bacterial strains, plasmids and growth conditions The E. coli strains DH5α and BL21 (DE3) were used for the cloning and expression experiments. The expression vector pET-28a used in this study was purchased from Novogen, USA. The pTNT vector carrying GAD 65 gene was provided by Ake Lernmark, Professor, Lund University Sweden. The E. coli was grown in Luria Bertini Broth (LB) at 37°C with shaking 200rpm or on LB plates solidified with 1.5 w/v agar.
  • 3. Int. J. Biomol. Biomed. Jayanth et al 3 As per the requirement LB broth and agar plates were supplemented with kanamycin in a final concentration of 50 mg/L. The GAD 65 gene was cloned and maintained in pTNT cloning vector. Bacterial expression vector pET-28a was selected to express the gene encoding for GAD 65 protein in E. coli. It contains T7 promoter driven expression of recombinant proteins with the addition of a 19 amino acid N-terminal fusion tag containing a 6X His tag followed by a thrombin protease cleavage site. Two stop codons are included in the vector at the C- terminal cloning site with kanamycin resistance (nptII) gene as selection marker and poly linker sequence with multiple cloning sites (Fig. 1.). This vector replicates in E. coli through it sp BR322 origin of replication. Plasmid DNA was isolated and purified using QIA prep Miniprep Kit (Qiagen, USA) according to the manufacturer protocol. Fig. 1.Vector map of recombinant pET-28a_GAD 65. Primer designing for the cloning of GAD65 gene Oligonucleotides primers were designed for PCR amplification of GAD65 gene. To facilitate the cloning of GAD 65 gene into the expression vector pET-28a, NcoI restriction site was inserted in the forward primer (5’-atatcatg CCATGGCTAGCCCAGGCT-3’) and XhoI site in the reverse primer sequence (5’- ccg CTCGAGTAAATCTTGTCCAAGGCG-3’) due to the absence of the two sites in the GAD 65 gene. Cloning of GAD65 gene into bacterial expression vector pET-28a The GAD 65 gene in the pTNT vector was used as a template and was amplified with Pfu poly meraseusing a pair of gene specific primers GAD65 XhoI forward primer and GAD65 NcoI reverse primer in 50 µL reaction mixture. The programme is as follows; Initial denaturation at 98°C for 3 minutes followed by 30 cycles of final denaturation at 98°C for 10 sec, annealing at 60°C for 30 sec and extension at 68°C for 1 min with a final extension for 7 min at 68°C. The PCR product was resolved on 1 per cent agarose gel and the 1.75 Kb GAD 65 gene was eluted from the agarose using Qiagen gel elution kit. The purified PCR product (GAD 65 gene) was restriction digested in 50µL reaction mixture (2µg DNA, XhoI and NcoI). The bacterial expression vector pET-28a was restriction digested with XhoI and NcoI. The pET-28avector carries an N-terminal 6X His tag. The GAD65 gene was cloned to the upstream of N-terminal coding portion of pET- 28a vector (Fig. 1.).
  • 4. Int. J. Biomol. Biomed. Jayanth et al 4 The digested PCR product was ligated into digested pET- 28a vector in 1:3 ratio using T4 DNA ligase enzyme. The ligated mixture was transformed into E. coli DH5α competent cells by electroporation as described by Sam brook and Russel (2001). Transform ants were screened using 50 mg/l kanamycin selection. To confirm the recombinant clones, the colony PCR was done using a pair of gene specific primers. Further these clones were also confirmed by restriction digestion with NcoI and XhoI and confirmed on 0.8% agarose gel. GAD 65 protein expression The E. coli BL 21 competent cells were transformed with confirmed recombinant clone as described by Sam brook and Russel (2001) and screened using 50 mg/Lkanamycin selection. The single colony was cultured by inoculating it in 10 mL LB broth containing kanamycin (50 mg/L) and incubated at 37°C overnight. From the overnight grown culture one mL was inoculated into 100 mL LB broth to make 1:100 dilution and incubated at 37°C until the OD reached 0.4-0.6. At this point, different parameters were used to optimize GAD 65 protein expression in E. coli i.e., different IPTG concentration (0.1, 0.3, 0.5, 0.7, 1, 1.5, 2.0, 2.5, 3.0 3.5 and 4.0 µM), temperature (25°C and 30°C) and time interval (4, 8, 12, 16 and 18 h). The cells were harvested by centrifugation at 10000 rpm for 15 min at 4°C. GAD 65 protein extraction and purification The harvested cells were suspended in lysis buffer [(1X PBS,), 7µL PMSF and 1mg/m Llysozyme] and incubated on ice for 15 min. Cells were lysed by sonication at 200-300 W for 15 min with alternative 10 sec sonication and 10 sec rest on ice. The cells were sonicated and pelleted out at 10000 rpm for 10 min at 4°C. The supernatant was collected and subjected for purification using Ni-NTA agarose column. The column of Ni-NTA agarose was prepared, equilibrated and activated with 1X PBS. The column was loaded with protein sample and flow throw was collected. The column was washed with 1X PBS to remove unbound foreign or host proteins. Then the GAD 65 protein was eluted from the column using different concentration of imidazole (50, 150,250 mM). The concentration of purified GAD 65 protein isolated from E. coli BL 21 cell was measured by using Bradford protein assay (Bradford, 1976). SDS PAGE and Western blot analysis The purified GAD 65 protein was analyzed by SDS- PAGE as per the standard procedure of Lamelli (1970). The protein samples were prepared by denaturing the proteins by boiling for 15 min with SDS loading dye. The protein samples were run on 12 per cent acrylamide gel along with standard protein marker. Further the expression of the GAD 65 protein was confirmed by western blot as per the standard protocol of Tow bin et al., 1979. The protein bands were transferred from SDS-PAGE gel to activated PVDF membrane by electro blotting. The unspecific protein binding sites were blocked with blocking buffer containing skimmed milk and incubated at 37°C for 1 h. Then the membrane was washed with PBST and incubated for 1 h at 37°C with GAD65 monoclonal antibody. The binding of the antibody was visualized using goat antibody antimouse Ig G conjugate with peroxidase. Results and discussion Generation of recombinant clones of pET- 28a_GAD65 The E. coli strain DH5αwas transformed with the ligation mixture and the recombinants were grown on kanamycin selection media. The colony PCR resulted in the amplification of GAD65 gene, amplicon size ~1.75Kb. (Fig. 2.). Further, restriction digestion of recombinant clones with XhoI and NcoI restriction enzymes resulted in linearization of pET-28a vector (~5.23 kb) and the release of the GAD 65 gene (~1.75Kb). This confirms the proper integration of the gene into the expression vector. Thereafter, clones are designated as recombinant clones (Fig. 3.).
  • 5. Int. J. Biomol. Biomed. Jayanth et al 5 Fig. 2. Colony PCR of transformed colonies of pET-28 a_GAD 65 gene. M: 1 Kb DNA ladder; lane 1: Negative control, lane 2: Positive control; lane 3-10: PCR amplicon of GAD 65 gene. Fig. 3. Confirmation of recombinant pET-28a_GAD 65 gene construct with XhoI and NcoI restriction digestion. M: 1Kb DNA ladder; Lane 1: undigested pET-28a vector; lane 2: undigested recombinant pET- 28a GAD65 gene construct; lane 3-4: Restriction digestedre combinant pET-28a GAD65 construct. Effect of IPTG concentration on gene expression Different parameters like IPTG concentration, induction temperature and length of induction influences both the solubility and yield of the protein. For the expression vector pET-28a_GAD 65, the foreign protein expression was triggered by adding IPTG into the culture medium. The Fig. 4. showed overall growth pattern of recombinant clones on different concentrations of IPTG ranging from 0.1, 0.3, 0.5, 0.7, 1.0, 1.5, 2.0, 2.5, 3.0, 3.5, 4.0 µM. Although the maximum cell growth was observed at 0.3 to 0.5µ M IPTG. The optimum growth and maximum expression i.e. 530μg/mL of protein was seen at 2.0 µM IPTG at 30°C after 4 h of induction (Fig. 4.). The decrease in protein expression after 2 µM IPTG concentration is may be due to the fact that further increase in IPTG concentration acts as inhibitory for the bacterial cells. Lower IPTG concentration, lower temperature with longer induction time leads to the slower expression rate of the protein which allows better folding of the protein but reduces yield. The higher IPTG concentration with shorter induction time at low temperature may allow higher properly folded protein expression which leads to increased yields of protein (Tolia and Joshua- Tor, 2006). As the GAD 65 gene was cloned into pET-28a expression vector, it has lacI promoter which codes for repressor protein and a T7 promoter which is specific to only T7 RNA polymerase. The control of pET expression system is accomplished through the lac promoter and operator. Addition of IPTG displaces the repressor from the lac operator and induces the expression of T7 RNA polymerase which in turn transcribes the target gene cloned into the pET-28a bacterial expression vector system. By adjusting the concentration of IPTG, expression can be regulated from very low level expression up to the robust, fully induced expression levels commonly associated with pET vectors (German and Eduardo, 2014).
  • 6. Int. J. Biomol. Biomed. Jayanth et al 6 Fig. 4. Effect of IPTG concentrations on bacterial cell growth and GAD 65 protein expression. Effect of different temperature and time interval on gene expression The optimum temperature for E. coli growth is 37°C but induction for recombinant protein expression are carried out at low temperature to retain the solubility (folding) of the expressed protein. The recombinant clones showed maximum growth at 37°C as compared with the other temperatures. Although the cells grew well at 37°C but the protein expression was not maximum at this temperature. At 25°C with 4, 8, 12, 16, 18 h time interval the protein expression was 259, 391, 498, 250 and 245μg/mL respectively while at 30°C with same length of induction period, the GAD 65 protein expression was 537, 436, 319, 298 and 256 μg/mL respectively. Hence, E. coli cells induced at 30°C for 4 h and 25°C for 12 h at 2 μM IPTG concentration showed the highest GAD65 protein expression of 537 μg/mL and 498 μg/mL respectively (Fig. 5.). This may be due to slower expression rate at 25°C when compared to 30°C. The temperature is known to influence the expression of recombinant proteins in E. coli. When the temperature decreases, induction time increases because of reducing culture temperature usually leads to slower growth of bacteria and slower rate of protein production (Gong et al., 2009). The bacterial growth at 37°C causes some proteins to accumulate as inclusion bodies, while incubation at 30°C leads to soluble, active protein (Vera et al., 2007). Fig. 5. Effect of different induction temperatures and time intervals on GAD 65 protein expression. The error bars indicate the standard deviation. Expression and Purification of GAD 65 protein After the optimization of the different parameters, the histidine tag fused GAD 65 protein expressed in E. coli BL 21 cell was extracted and purified by metal affinity chromatography. The purification of protein is essential for any biochemical analysis, therapeutics or structural studies. The GAD 65 protein samples were passed through Ni-NTA agarose column and the optimum elution of GAD65 protein was obtained when 250 mM imidazole was used. Similar result was reported by Papouchado et al., (1997) where they expressed GAD 65 protein as a fusion protein with thioredoxin which helped in the purification of GAD 65 protein. The purified GAD 65 protein expressed in E. coli was confirmed by SDS-PAGE where 65 kDa GAD 65 protein band was observed (Fig. 6A.).
  • 7. Int. J. Biomol. Biomed. Jayanth et al 7 Similarly, Rohmah et al., (2013) reported 65 kDa GAD 65 protein band on SDS-PAGE. This may be due to the correct expression and proper folding of GAD65 protein in E coli. Further it was confirmed by western blotting using monoclonal antibody. The presence of single 65 kDA protein band on the PVDF membrane confirmed the expression of GAD 65 protein (Fig.6B.). This is in line with Papouchado et al., (1997) who expressed GAD 65 protein in E. coli. The expression and subsequent purification of recombinant proteins are widely employed in biochemical and molecular studies. A powerful purification method involves the use of peptide affinity tags, which are fused to the protein of interest and used to expedite protein purification via affinity chromatography (Bornhorst and Falke, 2000). Hence, immobilized metal-affinity chromatography (IMAC) can be used to purify recombinant proteins containing a short affinity tag consisting of polyhistidine residues, theoredoxin residues etc., and the Ni NTA passed protein could keep its function. Fig. 6. SDS-PAGE and western blot analysis of recombinant GAD 65 protein expressed in E. coli. (A) Lane M: Protein ladder; lane 1: Purified protein sample (B) Western blot analysis. Lane M: Protein ladder; lane 1-4: GAD 65 protein samples expressed in E. coli. In conclusion, the different parameters were standardized for the expression of GAD 65 protein in E. coli. The protein produced can be aimed at developing a diagnostic kit for the prediction of insulin-dependent diabetes mellitus (Type-1). Acknowledgements Authors are highly thankful to the Dr. Ake Lernmark, Sweden for providing the GAD 65 gene construct. References Alvarez ML, Done SC, Cardineau GA. 2013. Reverse vaccination and treatment of type 1 diabetes using plant produced auto antigens and anti- inflammatory cytokines. Journal of Clinical and Cell Immunology S2:007. DOI: 10.4172/2155-9899.S2-007. Assenberg R, Wan PT, Geisse S, Mayr LM. 2013. Advances in recombinant protein expression for use in pharmaceutical research. Current Opinion in Structural Biology 23, 393-402. Bornhorst JA, Falke JJ. 2000. Purification of proteins using polyhistidine affinity tags. Methods Enzymology 326, 245-254. Bradford MM. 1976. A rapid and sensitive method for quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. Analytical Biochemistry 72, 248-254.
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