Journal of Biotechnology 117 (2005) 277–286
Effects of amino acid additions on
ammonium stressed CHO cells
Peifeng Chen a , Sarah W. Harcum a,b,∗
a
Department of Chemical Engineering, Clemson University, Clemson, SC 29634-0905, USA
b Department of Bioengineering, Clemson University, Clemson, SC 29634-0905, USA
Received 24 September 2004; received in revised form 3 February 2005; accepted 9 February 2005
Abstract
Ammonium is a toxic and inhibitory byproduct of mammalian cell metabolism. At the end of a typical recombinant protein
production campaign, the ammonium concentration can be as high as 10 mM, mainly due to glutamine metabolism. Intracellular
pH (pHi ) levels are sensitive to ammonium, which negatively impacts both cell growth and recombinant protein productivity.
Ammonium also negatively affects the recombinant protein glycosylation profile, thus altering quality. Many strategies have
been adopted to reduce ammonium accumulation, with limited results. This study investigated the addition of amino acids to
the growth media for Chinese hamster ovary (CHO) cell cultures as a means of mitigating the negative effects of ammonium.
Threonine, proline, and glycine additions improved CHO cell growth and recombinant protein levels. Further, the threonine,
proline, and glycine additions positively impacted important metabolic parameters, including glucose consumption, lactate
production, glutamine utilization, and final ammonium levels. Additionally, threonine, proline, and glycine increased the level
of ␣(2,3)-linked sialic acid, galactose-(1,4)-N-acetylglucosamine, and ␣(2,6)-linked sialic acid residues on the recombinant
tissue plasminogen activator (t-PA). Thus, threonine, proline, and glycine can be used to mitigate some of the toxic effects of
ammonium on cell growth, recombinant protein productivity, and protein quality.
© 2005 Elsevier B.V. All rights reserved.
Keywords: Amino acids; Tissue plasminogen activator; Ammonia/ammonium; Chinese hamster ovary cells; Glycosylation
1. Introduction
Glutamine, a major nutrient in mammalian cell culture, is usually present at concentrations between 1 and
∗ Corresponding author. Tel.: +1 864 656 6865;
fax: +1 864 656 0567.
E-mail address: harcum@clemson.edu (S.W. Harcum).
0168-1656/$ – see front matter © 2005 Elsevier B.V. All rights reserved.
doi:10.1016/j.jbiotec.2005.02.003
7 mM. Glutamine metabolism and glutamine chemical decomposition are the primary sources of ammonium buildup in media and cell cytoplasm. Other media sources of ammonium include catabolism of some
amino acids and fetal calf serum (McLimans et al.,
1991). Ammonium concentrations can reach 10 mM at
the end of a typical batch or fed-batch culture (Ozturk
et al., 1992). Ammonium readily diffuses across the
278
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
cell membrane, perturbing the intracellular pH (pHi )
and electrochemical gradients. Glutamine metabolism
decreases pHi , while glutamine decomposition and
ammonium-additions increase pHi (Schneider et al.,
1996).
The effects of ammonium or ammonia on cell
growth, productivity, and glycosylation have been investigated. Specifically, elevated ammonium significantly inhibits cell growth and final cell densities
(Gawlitzek et al., 1999; Hassell et al., 1991; McQueen
and Bailey, 1991; Schneider et al., 1997; Singh et al.,
1994; Yang and Butler, 2000b), and ammonium decreases recombinant protein productivity (Canning and
Fields, 1983; Ito and McLimans, 1981; Reuveny et
al., 1986). Tissue plasminogen activator (t-PA) production has been observed to be reduced under elevated
ammonium conditions (Hansen and Emborg, 1994).
Also, it has been observed that elevated ammonium
levels result in lower terminal sialylation of all the glycans, lower tetraantennary and tetrasialylated oligosaccharide structures, and higher molecular heterogeneity (Andersen and Goochee, 1995; Borys et al., 1994;
Gawlitzek et al., 1998; Thorens and Vassalli, 1986;
Yang and Butler, 2000, 2002). These changes to the recombinant protein typically result in a less efficacious
drug.
Many strategies have been developed to overcome
the toxic ammonium effects in mammalian cell culture. Some methods have attempted to reduce the
production of ammonia from glutamine. For example, the substitution of glutamine for glutamate has
been investigated; however, cell growth was lower
with glutamate (Capiaumont et al., 1995; Hassell et
al., 1991). Others have attempted to remove ammonium from the media by electrokinetic techniques
(Gawlitzek et al., 1995); gas-permeable, hydrophobic
porous membranes (Schneider, 1995); immobilized adsorbents (Jeong and Wang, 1992); and co-culturing
with the cells that metabolize ammonia (Liu and Chang,
2003). However, no readily available, widely applicable method has been developed.
Amino acids exist as zwitterions at physiological pH; thus, amino acids have the potential to act
as buffers of pHi (Bavister and McKiernan, 1993;
Gardner and Lane, 1997). Edwards et al. (1998) reported non-essential amino acids and glutamine had
the greatest capacity to buffer pHi for early mouse
preimplantation embryos. deZengotita et al. (2002)
demonstrated that the amino acids glycine, threonine, and glycine betaine could protect hybridoma
and CHO cells from elevated carbon dioxide and
osmolality.
The objective of this study was to develop a method
to easily mitigate the negative effects of ammonium.
Various amino acids were supplied to CHO cell cultures under ammonium stress. The effects of the amino
acid additions on CHO cell growth, recombinant protein productivity, and glycosylation were examined.
It was determined that some amino acids could mitigate the negative effect of ammonium, especially cell
growth rates and productivity.
2. Materials and methods
CHO cells (CRL-9606) were obtained from American Type Culture Collection (ATCC). This cell line
constitutively expresses t-PA. All chemical reagents
were purchased from Sigma (St. Louis, MO) unless
otherwise specified. CHO cells were cultured in a
basal media containing IS CHO-VTM (Irvine Scientific, Santa Ana, CA) with 0.1% fetal bovine serum (Invitrogen), 200 nM methotrexate, and 7 mM glutamine
(Irvine Scientific, Santa Ana, CA). CHO cells were
cultured in 1-L spinner flasks in humidified incubators at 37 ◦ C and 5% CO2 . NH4 Cl was used to simulate elevated ammonium levels. NH4 Cl and amino
acids stock solution were prepared in Milli-Q water. The control spinner flask contained the basal media. The negative control contained the basal media
supplemented with 10 mM NH4 Cl. The amino acid
supplement spinner flasks contained the basal media
plus 20 mM of the appropriate amino acid and 10 mM
NH4 Cl. Milli-Q water was used to normalize culture
volumes; this equalized basal media components and
minimized the osmolality difference due to NH4 Cl and
amino acids additions. NH4 Cl, amino acids, and water
were added to the fresh media prior to the addition of
cells. Each set of spinner flasks was inoculated from a
common seed culture. The amino acid-supplemented
cultures were run in duplicates. Cell densities and viabilities were determined by the Trypan blue exclusion
method. Harvested cells were centrifuged at 1000 rpm
for 5 min at 4 ◦ C. The supernatant and pellets were
saved at −20 and −80 ◦ C, respectively, for later analysis.
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
The glucose concentrations were measured by One
Touch glucose meter (Life Scan, Milapitas, CA). Glutamine concentrations were measured by a glutamine
assay kit (Sigma, MI), as per kit instructions. Lactate
concentration was measured with a lactate assay kit
(R-biopharm, Germany), as per kit instructions. Ammonium and amino acids were analyzed with a Dionex
D-300 amino acid analyzer and a Dionex 2000i ion exchange chromatography system with a dual wavelength
detector (440 and 570 nm). Supernatants (2.8 mL) were
mixed with 10% sulfosalicylic acid (1 mL) to precipitate the proteins prior to chromatography column. Samples were incubated at room temperature for 30 min and
filtered prior to injection.
The specific consumption rates of glucose and lactate for the metabolic parameters were calculated by
the general formula
q=
dY 1
dt X
(1)
where Y represents each metabolic parameter, t represents culture time, and X represents viable cell densities. This method assumes that each specific consumption rate is constant.
T-PA activity was measured by the Spectrolyse kit
(American Diagnostica), as per kit instructions. The
t-PA integrity was analyzed by Western blot. The Opti4CN kit was used (Bio-Rad). Rabbit anti-human recombinant t-PA (American Diagnostica) was used as
primary antibody. The secondary antibody was GARHRP (Bio-Rad). The DIG glycan differentiation kit
(Roche) was used to identify glycan structures on tPA. Equal volumes of culture supernatant (2 L) were
used for Western blots and DIG analysis.
3. Results
To determine the effects of supplemented amino
acids on cell growth for CHO cells exposed to elevated ammonium, various amino acids (alanine, aspartic acid, histidine, glycine, proline, serine, threonine, arginine, and lysine) were examined. These amino
acids were selected based on at least one of the following properties: (1) potential metabolic effects related to ammonia or glutamine; (2) high secretion or
consumption rates reported in other ammonia studies;
(3) various pI values to determine the effect of pI on
279
ammonium toxicity; (4) examples of essential or nonessential amino acids.
In order to determine the optimum amino acid concentrations to overcome ammonium toxicity, the ammonium inhibition for this cell line in the IS-CHOV media were first examined. The addition of 5 mM
ammonium to the media prior to inoculation did not
significantly inhibit the CHO cell growth rates (data
not shown). The addition of 20 mM or greater levels
of ammonium dramatically inhibited the CHO cells
growth rates, and exceeded most industrially observed
levels. Additionally, none of the amino acid additions
were able to counteract the ammonium toxicity where
20 mM ammonium was used. The addition of 10 mM
ammonium was observed to significantly inhibit the
cell growth rates, and this has been observed for t-PA
production and other proteins (Hansen and Emborg,
1994; Kurano et al., 1990; Schlaeger and Schumpp,
1989). Thus, the 10 mM ammonium level was selected
for further study. The amino acid addition concentration was also examined, and it was determined that
20 mM amino acids additions had the greatest impact
on the cell growth rates. Therefore, the set of conditions examined in detail used 10 mM ammonium and
20 mM amino acid additions.
Most of the amino acids examined did not improve
the cell growth rates, however, three amino acids (threonine, proline, and glycine) improved growth rates relative to the negative control cultures. The growth curves
for the three amino acids that improved growth rates
and an example of one amino acid (alanine) that did
not improve the growth rates are shown in Fig. 1. For
all amino acids examined, the control cultures had the
highest growth rates and final cell densities. The negative control cultures had significant lower growth rates
and final cell densities than the control culture. The
threonine, proline, glycine-supplemented cultures had
lower growth rates and final cell densities than the control cultures and significantly improved growth rates
than the negative controls (ANOVA, p ≤ 0.05). Specifically, threonine addition improved the final cell density by 15% compared to the negative control culture;
the proline addition improved the final cell density by
20%; the glycine addition improved the final cell density by 25%. However, the final cell densities for the
three amino acid-supplemented cultures were approximately 20% lower than the control cultures. The alanine and serine additions in this study were selected as
280
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
Fig. 1. CHO cell densities for amino acid supplemented cultures in the presence of elevated ammonium levels. Control (), duplicate amino
acid supplemented (䊉), (), and negative control () cultures. Error bars represent 95% confidence intervals.
two examples that did not improve the growth rates.
The alanine addition was observed to decrease cell
growth rates to levels below the negative control. This
inhibitory effect was proportional to the amount of alanine added to the media for concentrations between 5
and 20 mM. Serine also inhibited cell growth rates, but
not as severely as alanine (data not shown).
The glucose consumption rates and lactate production rates are indicators of cell health. The glucose
consumption rates of the control and negative control cultures were nearly 13 and 20 nmol/105 cells h,
respectively, as shown in Fig. 2. Glucose and lactate consumption rates for all conditions are shown in
Fig. 2. The negative control culture utilized more glucose per cell in order to mitigate the ammonium stress.
The lactate production rate for the control and negative control cultures were 8 and 12 nmol/105 cell h, respectively. High lactate production rates indicated the
cells were more wasteful with respect to carbon utilization. The glucose consumption rates for the threonine,
proline, and glycine treatments were between 13 and
17 nmol/105 cell h. The lactate consumption rates for
the threonine, proline, and glycine treatments were between 9 and 11 nmol/105 cell h. The alanine addition
increased glucose consumption rates and lactate production rates to 2.5-fold higher than the negative con-
Fig. 2. (A) Glucose consumption and lactate production rates for the
control, amino acid supplemented, and negative control cultures; (B)
ammonium and glutamine concentration at the end of the cultures
(61 h).
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
281
Table 1
Amino acid concentration in media for the basal media initially, control, negative control, and amino acid supplemented cultures at time 61 h
Amino acid (mM)
Alanine
Arginine
Aspartic acid
Cystine
Glycine
Histidine
Isoleucine
Leucine
Lysine
Methionine
Phenylalanine
Proline
Serine
Threonine
Tyrosine
Valine
Conditions
Basal media
Control
Negative control
Threonine
Proline
Glycine
Alanine
Serine
1.06
1.04
0.53
0.61
0.77
0.33
0.62
1.07
0.68
0.19
0.65
1.18
0.80
0.66
0.25
1.00
3.43
0.63
0.63
0.31
0.57
0.12
0.30
0.52
0.26
0
0.31
0
0.64
0.32
0.08
0.60
3.63
0.64
0.69
0.36
0.41
0.16
0.32
0.60
0.30
0
0.38
0
1.50
0.34
0
0.66
3.00
0.74
0.53
0.34
0.46
0.19
0.35
0.65
0.40
0
0.37
0
2.45
16.1
0.13
0.64
2.81
0.67
0.59
0.34
0.51
0.18
0.35
0.65
0.34
0
0.44
15.7
2.70
0.36
0.12
0.68
3.70
0.69
0.68
0.41
16.1
0.15
0.39
0.72
0.36
0
0.48
0
2.31
0.38
0.17
0.68
16.6
0.99
0.66
3.01
0.60
0.32
0.58
1.10
0.66
0.15
0.57
0
5.37
0.54
0.29
0.95
4.06
0.91
0.71
0.56
0.50
0.17
0.44
0.77
0.41
0.07
0.53
0
20.2
0.41
0.16
0.76
The amino acid concentrations corresponding to the supplemented amino acid are shown in italics.
trol. The serine addition also increased glucose consumption rates and lactate production rates to levels
above the negative control, although not as severely as
the alanine addition. These results indicated threonine,
proline, and glycine additions positively impacted carbon utilization under ammonium stress, while the alanine and serine additions negatively impacted carbon
utilization.
As noted previously, elevated ammonium levels
are commonly observed near the end of mammalian
cell cultures. The ammonium levels for the control
and negative control cultures at the end of the cultures (61 h) were 4.1 and 11.7 mM, respectively, as
shown in Fig. 2. End-of-culture ammonium levels for
all conditions are also shown in Fig. 2. The ammonium levels for proline, glycine, alanine, and serine
were approximately the same concentrations as the
original ammonium additions; however, the threoninesupplemented cultures had significantly lower ammonium levels. Glutamine can be used as a carbon and nitrogen source by cells in culture. The
glutamine concentrations for the control and negative control cultures at the end of the cultures were
0.8 and 2.1 mM, respectively (shown in Fig. 2).
The initial glutamine concentration in the media was
7 mM for all cultures. The glutamine concentrations
for all the amino acid-supplemented cultures were
slightly-to-moderately higher than the negative controls (Fig. 2).
Free amino acids in the media can be used by CHO
cells directly as protein and nucleotide precursors, as
well as carbon and nitrogen sources. The amino acid
concentrations at the end of all the cultures were determined for the control cultures and the amino acidsupplemented cultures (threonine, proline, glycine, alanine, and serine), and these data are shown in Table 1.
The amino acid concentrations for the basal media were
also determined. For the control and negative control
cultures at the end of the cultures, alanine and aspartic
acid concentrations were higher relative to the basal
media; thus, these amino acids are produced by the
cells and secreted. The amino acids arginine, cysteine,
glycine, histidine, isoleucine, leucine, lysine, methionine, phenylalanine, proline, threonine, tyrosine, and
valine were all consumed approximately equally by the
control and negative control cultures by the end of the
cultures. Only proline and methionine were completely
consumed by the control and negative control cultures.
The only major differences in amino acid consumption
between the control and negative-control cultures were
observed for serine and tyrosine. Serine was consumed
by the control cultures and generated by the negative
control cultures. Tyrosine was completely consumed
by the negative control cultures, whereas only approxi-
282
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
Fig. 3. Western blots of t-PA from proline-, glycine-, and threonine-supplemented cultures in the presence of elevated ammonium levels. Control
(C), amino acid (AA), negative control (N). Times corresponded to culture times.
mately two-thirds of the basal media concentration was
consumed by the control cultures.
In general, the alanine-supplemented culture had the
highest number of amino acids with significantly different amino acid concentrations at the end of the cultures
when compared to the controls and other amino acidsupplemented cultures. The serine-supplemented cultures were more similar to the alanine-supplemented
cultures in the end-of-culture amino acid profiles as
well as in not protecting the cell growth rate. The
amino acid concentrations of threonine-, proline-, and
glycine-supplemented cultures were very similar to
each other. The most striking difference between the
amino acid-supplemented cultures and the control cultures was the serine concentration at the end of the culture. The serine levels for the amino acid-supplemented
cultures were all significantly higher than the negative
control cultures, which also produced serine, whereas
the control cultures consumed serine.
T-PA has three potential N-linked glycosylation
sites. Two glycosylation variants of t-PA have been
identified, type I and type II. Type I t-PA is glycosylated at amino acid positions 117, 184, and 448 and
has a molecular weight of 68 kD. Type II t-PA is glycosylated at positions 117 and 448 and has a molecular
weight 65 kD. Western blots were used to assess the
effects of amino acid supplementation on the distribution of type I and II t-PA. In this study, both type I
and II t-PA were produced by the control, amino acidsupplemented, and negative control cultures, as shown
in Fig. 3.
The t-PA activity was determined for the control, amino acid-supplemented (threonine, proline, and
glycine only), and negative control cultures, as shown
in Fig. 4. The control cultures had the highest t-PA activities at the end of the cultures. The negative control
cultures had the lowest t-PA activities at the end of the
cultures. For the threonine cultures, the observed t-PA
activity was nearly identical to the control cultures. For
glycine and proline, the amino acids increased t-PA activities; however, only approximately to the average of
the control and negative control levels.
The effects of the amino acid supplementation on
the glycosylation profiles of t-PA were determined using lectins specific to oligosaccharide linkages commonly found on terminal glycan branches. T-PA samples from the amino acid-supplemented cultures with
improved growth were compared (threonine, proline,
and glycine) to the control and negative control cultures. The 49-h samples for the control, amino acidsupplemented, and negative control were compared.
The 49-h samples were selected for comparison since
the cells had reached late exponential phase, but were
not nutrient limited, such as for proline. Therefore, the
effect of nutrients on glycosylation were minimized.
Five lectins were used to assess glycosylation. As
expected, the Galanthus nivalis agglutinin (GNA) did
not detect highly terminal mannose in any samples; and
Peanut agglutinin (PNA) did not detect O-linked disaccharide galactose (1,3)-N-acetylgalactosamine in any
Fig. 4. Normalized t-PA activity for proline-, glycine-, and
threonine-supplemented cultures in the presence of elevated ammonium levels at the end of the cultures (61 h). Control (C), amino acid
(AA), negative control (N).
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
283
Fig. 5. Glycan differentiation of t-PA glycans for proline-, glycine-, and threonine-supplemented cultures in the presence of elevated ammonium
levels. (A) Sialic acid terminally linked ␣(2,3) to galactose. (B) (1,4)-N-acetylglucosamine linked to galactose. Control (C), amino acid (AA),
negative control (N).
samples. The Maackia amurensis agglutinin (MAA)
detected ␣(2,3) sialic acid linked to galactose for both
type I and II t-PA in all samples, as shown in Fig. 5. The
Datura stramonium agglutinin (DSA) detected (1,4)N-acetylglucosamine linked to galactose for both type I
and II t-PA in all samples, as shown in Fig. 5. The Sambucus nigra agglutinin (SNA), which detects ␣(2,6)
sialic acid linked to galactose, gave a faint signal for
both type I and II t-PA in all samples (data not shown).
This faint ␣(2,6) sialic acid signal was most likely due
to the O-linked glycan (Harris et al., 1991; Moloney and
Haltiwanger, 1999; Van den Steen et al., 1998) since
CHO cells do not express the ␣(2,6) sialytransferase
for N-linked glycans.
For the lectin blots, all the amino acid supplemented
cultures had intensity bands that were slightly higher
than the negative controls, but lower than the controls,
as shown in Fig. 5. The intensity differences could be
attributed to higher ␣(2,3) sialic acid, higher (1,4)N-acetylglucosamine, or higher ␣(2,6) sialic acid on
the O-linked glycan, respectively. The intensity differences could also be attributed to higher levels of t-PA.
Since lectin blots are only semi-quantitative, it was only
possible to estimate the intensity difference; however,
the differences in t-PA activity were less than the differences observed in the lectin blot band intensities. Thus,
the observed increase in glycosylation was attributed to
improved glycosylation and not just higher t-PA levels.
ammonium, as demonstrated by lower growth rates.
Normally, the main source of ammonium buildup is
attributed to glutamine metabolism. Specifically, glutamine is hydrolyzed to glutamate and ammonia. Glutamate is further hydrolyzed to ␣-ketoglutarate via glutamate dehydrogenase, which releases another ammonia molecule, as shown in Pathway 1 in Fig. 6. Alternatively, glutamate and pyruvate can react to form
alanine and ␣-ketoglutarate, as shown in Pathway 2
in Fig. 6. Alanine is hypothesized to be secreted into
the media as a mechanism to reduce ammonia toxicity
by redirecting the amine group from glutamate to alanine, instead of a free ammonia molecule (Hansen and
Emborg, 1994; Miller et al., 1988; Ozturk et al., 1992;
Schneider et al., 1996; Street et al., 1993) as shown in
Fig. 6. Thus, the addition of alanine to the media probably inhibited the reaction of glutamate and pyruvate
to alanine, therefore prevented the cells from secreting
alanine. In this study, compared with the concentration in basal media, alanine was found to be secreted
into the media at the end of the culture at high levels for the control, negative control, and other amino
acid supplemented cultures. These results strongly support the hypothesis that alanine secretion reduces ammonium stress via this mechanism. Additionally, the
alanine supplemented cultures had elevated glutamine
4. Discussion
The objective of this research project was to determine if amino acids could protect mammalian cell
growth, recombinant protein productivity, and glycosylation in the presence of elevated ammonium. Threonine, proline, and glycine had significant protective
impact. Most amino acids, such as alanine, serine,
and histidine, did not mitigate the negative effects of
Fig. 6. Schematic diagram of amino acid metabolism for alanine,
proline, glycine, and threonine, as related to ammonium.
284
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
levels, even when compared to the negative control. The
elevated glutamine levels were probably from a combination of lower consumption of glutamine from lower
growth rates and a reduction in the glutamine/pyruvate
to alanine/␣-ketoglutarate reaction.
High levels of serine were observed in the media
at the end of the cultures for the negative control and
other amino acid (non-serine) supplemented cultures;
however, the serine levels in the media at the end of
the cultures for the control cultures were lower than
the basal media. Elevated serine levels for the negative
control and amino acid supplemented cultures could
have been due to the reaction of pyruvate with ammonia to form serine. Additionally, this reaction in reverse
(serine to pyruvate and ammonia) could have been responsible for the slightly higher levels of ammonium
observed in the serine-supplemented cultures.
The threonine-, proline-, and glycine- supplemented
cultures had lower ammonium levels relative to the negative controls. Additionally, the ammonium levels in
the threonine-supplemented cultures were lower than
the amount of ammonium initially added to the media. Additionally, threonine protected the cells to the
greatest extent based on growth rates and t-PA activity.
The glutamine levels for the amino acid-supplemented
cultures were higher than the control cultures and
slightly higher than the negative control cultures. Interestingly, both the glucose consumption and lactate production rates for the threonine-, proline-, and glycinesupplemented cultures were between the levels observed for the control and negative control cultures.
In contrast, the glucose consumption and lactate production levels for the alanine and serine supplemented
cultures were both higher than the negative control cultures. These results indicate that the threonine, proline,
and glycine additions may have provided both alternative carbon and nitrogen sources, which contributed to
improved cell growth rates, productivity, and protein
quality.
The threonine, proline and glycine additions improved cell growth, t-PA productivity and glycosylation. Proline was slightly less effective than glycine
and threonine at improving cell growth rates and tPA productivity. The protection provided by proline
was probably related to glutamate synthesis, as shown
in Fig. 6. Specifically, proline was probably converted
to glutamate by the ATP-independent glutamate semialdehyde dehydrogenase. The proline addition allowed
the cells to synthesize ␣-ketoglutarate via glutamate,
which generates only a single ammonia molecule per
proline. In contrast, the consumption of glutamine to
␣-ketoglutarate via glutamate generates two ammonia
molecules per glutamine. Thus, proline metabolically
substituted for glutamine and allowed the cells to have
an active tricarboxylic (TCA) cycle with reduced ammonia production. This hypothesis is supported by the
relatively high level of glutamine still present at the end
of the proline supplemented culture (Fig. 2).
Threonine and glycine additions had similar effects on cell growth, t-PA productivity, and glycosylation. It is probable that glycine and threonine used
similar mechanisms to mitigate the ammonia stress.
Glycine and threonine metabolism are connected, in
that glycine is readily converted to threonine, as shown
in Fig. 6. The increased pyruvate levels due to the
glycine and threonine degradation mechanism may
have increased the flux through the TCA cycle, which
improved cell energetics. Specifically, threonine was
converted to pyruvate via a pathway initiated by threonine dehydrogenase. This reaction yielded ␣-aminob-ketobutyrate. The ␣-amino-b-ketobutyrate molecule
spontaneously degraded to aminoacetone, which was
converted to pyruvate. The glycine mechanism was
identical to threonine, except glycine was first converted to threonine by threonine aldolase. Thus, glycine
and threonine may mitigate ammonia stress by increased pyruvate levels, which are then metabolized
via the TCA cycle.
Another possible protective mechanism that can be
attributed to the amino acid supplements may be the
zwitterions property of these amino acids. Glycosylation reactions are very sensitive to the Golgi pH (Valley
et al., 1999). Ten mM ammonium has been observed
to raise the Golgi pH from the normal range (between
6.5 and 6.75) to 7.0 (Andersen and Goochee, 1995).
The pI values for threonine, proline, and glycine are
5.6, 6.3 and 5.97, respectively. Therefore, threonine,
proline, and glycine have the ability to balance the
Golgi pH due to zwitterionic properties. These results
can be indirectly confirmed by the effect of histidine
and arginine supplementation. These two basic amino
acids, with pI values of 7.59 and 10.76, respectively,
essentially prevented cell growth (data not shown). Although alanine has a pI of 6.02, it did not mitigate the
negative effects of ammonia. This was probably due
to its metabolic role in ammonia elimination. In this
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
study, alanine and serine did not protect the cells due
to metabolic constraints, where as threonine, proline,
and glycine probably mitigated the negative effects of
ammonia via a combination of pI buffering effects and
favorable metabolism.
5. Conclusions
Various amino acids were screened to determine if
the negative effects of ammonium stress on growth
rates, productivity, and protein quality could be mitigated. Only a few amino acids were able to counteract
the negative effects of ammonium on CHO cell growth
rates. Threonine, proline, and glycine were able to partially recover CHO cell growth rates, improve t-PA, and
improve glycosylation via metabolism and favorable
pI values. Amino acid metabolism and the zwitterionic properties of the amino acids were both important
properties for ammonium stress mitigation. For example, even with a favorable pI, alanine was unable to
overcome its metabolic constraints, whereas threonine
positively impacted metabolism and had a favorable
pI value. In conclusion, these research results indicate
that amino acid additions could be an effective and easy
method to protect CHO cells from elevated ammonium
stress.
Acknowledgements
The IS CHO-VTM media and l-glutamine were
kindly donated by Irvine Scientific. This work is partially supported by the National Science Foundation
under Grant No. 0303782.
References
Andersen, D.C., Goochee, C.F., 1995. The effect of ammonia on the
O-linked glycosylation of granulocyte-colony-stimulating factor
produced by Chinese-hamster ovary cells. Biotechnol. Bioeng.
47, 96–105.
Bavister, B.D., McKiernan, S.H., 1993. Regulation of hamster embryo development in vitro by amino acids. In: Bavister, B.D.
(Ed.), Preimplantation Embryo Development. Springer-Verlag,
New York, pp. 57–72.
Borys, M.C., Linzer, D.I.H., Papoutsakis, E.T., 1994. Ammonia affects the glycosylation pattern of recombinant mouse placental
285
lactogen-I by Chinese hamster ovary cells in a pH dependent
manner. Biotechnol. Bioeng. 43, 505–514.
Canning, W.M., Fields, B.N., 1983. Ammonium chloride prevents
lytic growth of reovirus and helps to establish persistent infection
in mouse L-cells. Science, 987–988.
Capiaumont, J., Legrand, C., Carbonell, D., Dousset, B., Belleville,
F., Nabet, P., 1995. Methods for reducing the ammonia in hybridoma cell-cultures. J. Biotechnol. 39, 49–58.
deZengotita, V.M., Abston, L.R., Schmelzer, A.E., Shaw, S., Miller,
W.M., 2002. Selected amino acids protect hybridoma and CHO
cells from elevated carbon dioxide and osmolality. Biotechnol.
Bioeng. 78, 741–752.
Edwards, L.J., Williams, D.A., Gardner, D.K., 1998. Intracellular pH
of the mouse preimplantation embryo: amino acids act as buffers
of intracellular pH. Hum. Reprod. 13, 3441–3448.
Gardner, D.K., Lane, M., 1997. Culture and selection of viable blastocysts: A feasible proposition for human IVF? Hum. Reprod.
Update 3, 367–382.
Gawlitzek, M., Conradt, H.S., Wagner, R., 1995. Effect of different cell culture conditions on the polypeptide integrity and Nglycosylation of a recombinant model glycoprotein. Biotechnol.
Bioeng. 46, 536–544.
Gawlitzek, M., Papac, D.I., Sliwkowski, M.B., Ryll, T., 1999. Incorporation of N-15 from ammonium into the N-linked oligosaccharides of an immunoadhesin glycoprotein expressed in Chinese
hamster ovary cells. Glycobiology 9, 125–131.
Gawlitzek, M., Valley, U., Wagner, R., 1998. Ammonium ion and
glucosamine dependent increases of oligosaccharide complexity
in recombinant glycoproteins secreted from cultivated BHK-21
cells. Biotechnol. Bioeng. 57, 518–528.
Hansen, H.A., Emborg, C., 1994. Influence of ammonium on
growth, metabolism, and productivity of a continuous suspension Chinese-hamster ovary cell-culture. Biotech. Prog. 10, 121–
124.
Harris, R.J., Leonard, C.K., Guzzetta, A.W., Spellman, M.W., 1991.
Tissue plasminogen-activator has an O-linked fucose attached to
threonine-61 in the epidermal growth-factor domain. Biochemistry 30, 2311–2314.
Hassell, T., Gleave, S., Butler, M., 1991. Growth-inhibition in
animal-cell culture – the effect of lactate and ammonia. Appl.
Biochem. Biotechnol. 30, 29–41.
Ito, M., McLimans, W.F., 1981. Ammonia inhibition of interferon
synthesis. Cell Biol. Int. Rep. 5, 661–666.
Jeong, Y.-H., Wang, S.S., 1992. In-situ removal of ammonium
ions from hybridoma cell culture media: selection of adsorbent.
Biotechnol. Technol. 6, 341–346.
Kurano, N., Leist, C., Messi, F., Kurano, S., Fiechter, A., 1990.
Growth-behavior of Chinese hamster ovary cells in a compact
loop bioreactor. 2. Effects of medium components and waste
products. J. Biotechnol. 15, 113–128.
Liu, Z.C., Chang, T.M.S., 2003. Coencapsulation of hepatocytes and
bone marrow stem cells: in vitro conversion of ammonia and in
vivo lowering of bilirubin in hyperbilirubemia Gunn rats. Int. J.
Artificial Organs 26, 491–497.
McLimans, W., Blumenson, L., Repasky, E., Ito, M., 1991. Ammonia loading in cell culture systems. Cell Biol. Int. Rep. 5, 653–
660.
286
P. Chen, S.W. Harcum / Journal of Biotechnology 117 (2005) 277–286
McQueen, A., Bailey, J.E., 1991. Growth-inhibition of hybridoma
cells by ammonium ion – correlation with effects on intracellular
pH. Bioproc. Eng. 6, 49–61.
Miller, W.M., Wilke, C.R., Blanch, H.W., 1988. Transient responses
of hybridoma cells to lactate and ammonia pulse and step changes
in continuous culture. Bioproc. Eng. 3, 113–122.
Moloney, D.J., Haltiwanger, R.S., 1999. The O-linked fucose glycosylation pathway: Identification and characterization of a uridine diphosphoglucose: fucose- 1,3-glucosyltransferase activity from Chinese hamster ovary cells. Glycobiology 9, 679–687.
Ozturk, S.S., Riley, M.R., Palsson, 1992. Effects of ammonia and
lactate on hybridoma growth, metabolism, and serum concentration. Biotech. Prog. 6, 121–128.
Reuveny, S., Velez, D., Macmillan, J.D., Miller, L., 1986. Factors affecting cell growth and monoclonal antibody production in stirred
reactors. J. Immunol. Methods 86, 53–59.
Schlaeger, E.-J., Schumpp, B., 1989. Studies on mammalian cell
growth in suspension culture. In: Spier, R.E.G.J.B., Stephenne,
J., Croopy, P.J. (Eds.), Advances in Animal Cell Biology, Technology for, Bioprocesses, Butterworths. Sevenoaks, Kent, UK,
pp. 386–396.
Schneider, M., 1995. Applications of hydrophobolic porous membranes in mammalian cell culture technology. Ph.D. Thesis
No. 1412, Ecole Polytechnique Federal de Lausanne (EPFL),
Switzerland.
Schneider, M., ElAlaoui, M., vonStockar, U., Marison, I.W., 1997.
Batch cultures of a hybridoma cell line performed with in situ
ammonia removal. Enzym. Microb. Technol. 20, 268–276.
Schneider, M., Marison, I.W., vonStockar, U., 1996. The importance of ammonia in mammalian cell culture. J. Biotechnol. 46,
161–185.
Singh, R.P., Alrubeai, M., Gregory, C.D., Emery, A.N., 1994. Celldeath in bioreactors – a role for apoptosis. Biotechnol. Bioeng.
44, 720–726.
Street, J.C., Delort, A.M., Braddock, P.S.H., Brindle, K.M., 1993.
A H-1 N-15 NMR-study of nitrogen-metabolism in culturedmammalian-cells. Biochem. J. 291, 485–492.
Thorens, B., Vassalli, P., 1986. Chloroquine and ammonium-chloride
prevent terminal glycosylation of immunoglobulins in plasmacells without affecting secretion. Nature 321, 618–620.
Valley, U., Nimtz, M., Conradt, H.S., Wagner, R., 1999. Incorporation of ammonium into intracellular UDP-activated Nacetylhexosamines and into carbohydrate structures in glycoproteins. Biotechnol. Bioeng. 64, 401–417.
Van den Steen, P., Rudd, P.M., Dwek, R.A., Opdenakker, G., 1998.
Concepts and principles of O-linked glycosylation. Crit. Rev.
Biochem. Mol. Biol. 33, 151–208.
Yang, M., Butler, M., 2000a. Effects of ammonia on CHO cell
growth, erythropoietin production, and glycosylation. Biotechnol. Bioeng. 68, 370–380.
Yang, M., Butler, M., 2000b. Effect of ammonia on the glycosylation
of human recombinant erythropoietin in culture. Biotech. Prog.
16, 751–759.
Yang, M., Butler, M., 2002. Effects of ammonia and glucosamine on
the heterogeneity of erythropoietin glycoforms. Biotech. Prog.
18, 129–138.