U.S. patent number 3,926,723 [Application Number 05/495,609] was granted by the patent office on 1975-12-16 for method of controllably releasing glucose to a cell culture medium.
This patent grant is currently assigned to Massachusetts Institute of Technology. Invention is credited to Howard Green, James G. Rheinwald.
United States Patent |
3,926,723 |
Green , et al. |
December 16, 1975 |
Method of controllably releasing glucose to a cell culture
medium
Abstract
A cell culture medium is disclosed which contains secondary
sources of glucose comprising glucose-containing oligosaccharides
or polysaccharides and hydrolytic enzymes (glucosidases) to
liberate free glucose. Starch, for example, can be added to a
culture medium to provide the controlled release of glucose when a
serum supplement such as fetal calf serum, which contains the
hydrolytic enzymes amylase and maltase, is used. Amylase breaks the
starch down into glucose and maltose, and maltase converts the
remaining maltose to glucose. The rate of glucose release can be
controlled by regulating the amount of glucosidase activity present
in the medium.
Inventors: |
Green; Howard (Brookline,
MA), Rheinwald; James G. (Cambridge, MA) |
Assignee: |
Massachusetts Institute of
Technology (Cambridge, MA)
|
Family
ID: |
23969285 |
Appl.
No.: |
05/495,609 |
Filed: |
August 8, 1974 |
Current U.S.
Class: |
435/392 |
Current CPC
Class: |
C12N
5/0018 (20130101); C12N 2500/34 (20130101) |
Current International
Class: |
C12N
5/00 (20060101); C12K 009/00 (); C12B 003/08 () |
Field of
Search: |
;195/1.7,1.8,104,31R,100,101,66R,115 |
References Cited
[Referenced By]
U.S. Patent Documents
Other References
Chem. Abstracts 76:137424(e). .
Chem. Abstracts 48:4080h. .
Parker, Methods of Tissue Culture, 3 ed., Harper & Row, 1961,
pp. 215-217..
|
Primary Examiner: Monacell; A. Louis
Assistant Examiner: Wiseman; Thomas G.
Attorney, Agent or Firm: Smith, Jr.; Arthur A. Santa; Martin
M. Brook; David E.
Government Interests
The invention herein described was made in the course of work
performed with a grant from the Department of Health, Education and
Welfare.
Claims
What is claimed is:
1. In the method of culturing mammalian cells in a culture medium
which supplies nutrients including glucose to said mammalian
cells:
The improvement of maintaining the glucose concentration in said
culture medium at a desired concentration by providing sustained
release of glucose at a controlled rate by including in the culture
medium a compound containing an enzymatically-releasable glucosyl
moiety and an enzyme activity capable of releasing glucose from
said glucosyl-containing compound, said glucosyl-containing
compound being present in an amount sufficient to provide sustained
release of glucose and said enzyme activity being present at a
level sufficient to maintain the glucose at the desired
concentration.
2. The improvement of claim 1 wherein said enzyme activity is
supplied by the presence in said culture medium of at least one
hydrolytic enzyme.
3. The improvement of claim 2 wherein said hydrolytic enzyme
comprises a glucosidase.
4. The improvement of claim 3 wherein said glucosyl-containing
compound comprises an oligosaccharide.
5. The improvement of claim 4 wherein said oligosaccharide
comprises maltose and said glucosidase comprises maltase.
6. The improvement of claim 3 wherein said glucosyl-containing
compound comprises a polysaccharide.
7. The improvement of claim 6 wherein said polysaccharide comprises
starch and said glucosidase comprises amylase and maltase.
8. The improvement of claim 6 wherein said polysaccharide comprises
glycogen and said glucosidase comprises amylase and maltase.
9. The improvement of claim 1 wherein said enzyme activity is
supplied to said culture medium by adding serum thereto.
10. The improvement of claim 9 wherein said serum comprises fetal
calf serum.
11. The improvement of claim 5 wherein maltase is supplied to said
culture medium by adding serum thereto.
12. The improvement of claim 11 wherein said serum comprises fetal
calf serum.
13. The improvement of claim 7 wherein amylase and maltase are
supplied to said culture medium by adding fetal calf serum
thereto.
14. The improvement of claim 1 wherein said enzyme activity is
included in an amount sufficient to maintain a glucose
concentration in said culture medium of from about 1 to about 100
micrograms per milliliter of medium.
15. The improvement of claim 4 wherein said glucosidase is included
in an amount sufficient to maintain a glucose concentration in said
culture medium of from about 1 to about 100 micrograms per
milliliter of medium.
16. The improvement of claim 6 wherein said glucosidase is included
in an amount sufficient to maintain a glucose concentration in said
culture medium of from about 1 to about 100 micrograms per
milliliter of medium.
17. The improvement of claim 9 wherein sufficient serum is added to
maintain a glucose concentration in said culture medium of from
about 1 to about 100 micrograms per milliliter.
18. The improvement of claim 9 wherein the enzyme activity in the
serum added to said culture medium is reduced by heating the serum
to an elevated temperature prior to its addition to the culture
medium.
19. The improvement of claim 18 wherein said enzyme activity is
supplied by the presence in said serum of at least one hydrolytic
enzyme.
20. The improvement of claim 19 wherein said hydrolytic enzyme
comprises a glucosidase.
21. The improvement of claim 20 wherein said serum comprises fetal
calf serum.
22. In the method of growing mammalian cell cultures wherein serum
containing glucasidase activity is added to a mammalian cell
culture medium to release glucose from glucosyl-containing compound
to maintain a desired glucose concentration:
the improvement of regulating the glucose concentration in said
culture medium by regulating the glucosidase activity of the serum
prior to its addition to the culture medium.
23. The improvement of claim 22 wherein the glucosidase activity in
said serum is reduced by heating said serum.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention is in the field of biology, and more specifically in
the field of cell biology.
2. Description of the Prior Art
Mammalian cells are typically grown in a culture medium to which a
serum supplement is added. There are several well known culture
media including Eagle's medium, the Dulbecco-Vogt modification of
Eagle's medium, and Ham's medium. In general, these are synthetic
formulations designed to provide sources of amino acids, vitamins,
glucose, etc. to the growing cells. The serum supplement is added
to provide certain proteins to the culture, and typical serum
supplements include calf serum, fetal calf serum, and horse
serum.
It has heretofore been common to provide relatively high
concentrations of glucose, e.g., greater than about 1 mg/ml, in
culture media to provide a source of carbon and energy to the
growing cells. Utilization by mammalian cell cultures of sugars
other than glucose has, however, been studied extensively. See, for
example, Harris, M. and Kutsky, P. B., J. Cell Comp. Physiol., 42,
449 (1953); Eagle, H., Barban, S., Levy, M., and Schulz, H. O., J.
Biol, Chem., 233, 551 (1958); Bailey, J. M., Gey, G. O., and Gey,
M. K., J. Biol. Chem., 234, 1042 (1959); Baugh, C. L. and Tytell,
A. A., Life Sciences, 6, 371 (1967); Martineau, R. Kohlbacher, M.,
Shaw, S. N., and Amos, H., Proc. Nat. Acad, Sci. USA, 69, 3407
(1972); Kalckar, H. M. and Ullrey, D., Proc. Nat. Acad. Sci. USA,
70, 2502 (1973); and Paul, J., In Cells and Tissues in Culture,
Vol. 1, Willmer, E. N., ed., Academic Press, New York, 239 (1965).
From such studies, it has been determined that mannose and fructose
are metabolised rapidly, but galactose is utilized more slowly and
produces less lactate. See Eagle, H. Barban, S., Levy, M. and
Schulze, H. O., J. Biol. Chem., 233, 551 (1958). In spite of these
extensive studies, glucose is still the sugar mostly widely used in
mammalian cell cultures, although it has been noted that cell
growth could take place on maltose or glycogen after their
hydrolysis by enzymes of embryo extract or serum. See Harris, M.
and Kutsky, P. B., J. Cell Comp. Physiol., 42, 449 (1953).
The use of glucose in culture media does cause some problems,
however. The most serious of these is that the glucose is consumed
rapidly. Since cells cannot survive when their glucose supply has
been exhausted, frequent refeeding to replenish the supply is
necessary. Further, high concentrations of glucose are not used
efficiently by growing cells because the cells ferment more glucose
than they can oxidize. This results in an accumulation of lactic
acid, a fermentation product, in the medium which produces a
concomitant drop in pH which is deleterious to cell growth. See
Ceccarini, C. and Eagle, H., Proc. Nat. Acad. Sci. USA, 68, 229
(1971).
SUMMARY OF THE INVENTION
In one embodiment, the invention comprises the use of secondary
sources of glucose in cell culture media, particularly those
intended for mammalian cells. Suitable secondary sources of glucose
include either a glucose-containing oligosaccharide or
polysaccharide and a glucosidase, or enzyme capable of releasing
glucose from the glucose-containing compounds. Suitable glucosidase
activity can be provided by choosing serum supplement containing
the desired hydrolytic enzyme or enzymes. Alternatively, commercial
preparations of a glucosidase can be added to the culture
medium.
The rate of glucose release to the culture medium can be controlled
by adjusting the glucosidase activity present. For example, the
rate can be reduced by partially inactivating the glucosidase
activity in the serum supplement by heating the serum to an
elevated temperature prior to its addition to the culture medium.
Alternatively, different amounts or types of hydrolytic enzymes, or
serum supplements containing hydrolytic enzymes, can be added to
culture media to adjust the glucosidase activity to the desired
level for any specific oligosaccharide or polysaccharide.
One suitable secondary source of glucose is starch together with
the hydrolytic enzymes amylase and maltase. The amylase breaks
starch down to predominantly maltose units and the maltase
completes the hydrolysis to glucose. Another secondary source is
the sugar maltose which is hydrolyzed by the enzyme maltase. Thus,
glucose is released by both systems.
Providing glucose to culture media from secondary sources offers
significant advantages over the direct addition of glucose. A
primary advantage is that any desired rate of glucose release to
the cell culture medium can be achieved for extended periods of
time. Low concentrations of glucose cannot be maintained by direct
addition because the growing cells consume the glucose so rapidly.
In the new system, glucose continues to be available to the cells
at a time when it would have been exhausted if supplied to the
medium directly.
Supplying constant but relatively low levels of glucose to the cell
culture from secondary sources also helps to maintain the pH of the
culture medium within a beneficial range. This is primarily because
little or no lactic acid is formed, since the growing cells
metabolize completely the glucose liberated from the secondary
source. Thus, the cells can be grown to a higher density and
maintained healthier for longer periods of time than in media to
which glucose is added directly, and frequent refeeding of cultures
to supply glucose is eliminated.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 illustrates graphically the growth rate of established
mammalian cell lines at various glucose concentrations.
FIG. 2 illustrates graphically the efficiency of cell utilization
of glucose at different concentrations;
FIG. 3 illustrates graphically the release of glucose from the
secondary source starch using fetal calf serum which contains
amylase and maltase;
FIG. 4 illustrates graphically the inactivation of serum enzymes
with heat;
FIG. 5 illustrates graphically certain conditions resulting from
the growth of V79 cells in various culture media containing
glucose, starch, plus amylase or maltose plus maltase;
FIG. 6 illustrates graphically the growth of V79 cells on maltose
in a culture medium containing serum with maltase inactivated by
heat.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The provision of secondary glucose sources in culture media is
useful in most cell cultures and is particularly useful in
mammalian cell cultures. Such mammalian cells as 3T3 and 3T6 (mouse
embryonic fibroblast lines), SVPy3T3-11, a 3T3 line doubly
transformed by polyoma and SV40, human diploid fibroblasts, V79, (a
line derived from Chinese hamster embryonic lung fibroblasts), and
HeLa (human carcinona); as well as other mammalian cell lines can
be grown in media containing secondary glucose sources.
Secondary glucose sources can be added to a wide variety of cell
culture media. Some of the better known and widely used media
include Eagle's medium, the Dulbecco-Vogt modification of Eagles's
medium, and Ham's medium. It should be clear, however, that other
media known to those skilled in the art can be provided with
secondary glucose sources as described herein.
Suitable secondary sources of glucose can be a glucose-containing
oligosaccharide or polysaccharide together with appropriate
glucosidase activity. The release of glucose can be illustrated for
the oligosaccharide maltose used in combination with the enzyme
maltase as follows: ##SPC1##
Similarly, the release of glucose from the polysaccharide starch by
the enzymes amylase and maltase can be illustrated as follows:
##SPC2##
Amylase hydrolyzes starch to glucose and maltose, and the maltose
is hydrolyzed into glucose by the enzyme maltase. It is preferable,
therefore, to include both amylase and maltase in a culture medium
if starch is the secondary source of glucose.
All glucose-containing oligosaccharides or polysaccharides which
can be broken down to release glucose by an appropriate glucosidase
are suitable secondary sources. Examples of oligosaccharides
containing glucose include, but are not limited to, maltose,
sucrose, lactose, and raffinose. Suitable examples of
glucose-containing polysaccharides include, but are not limited to
glycogen and starch. Other compounds containing glucosyl moiety
which can be released may also be useful. These include, for
example, synthetically prepared glucosides.
Secondary sources of glucose are particularly useful in cultures
where it is desired to maintain a relatively constant but low
concentration of glucose. Whereas most previous systems used
glucose at the physiological range (1 mg/ml) or higher, it has been
demonstrated that much lower concentrations can be used to achieve
beneficial results. FIG. 1 illustrates how the doubling time of a
number of established mammalian cell lines in the Dulbecco-Vogt
modification of Eagle's medium supplemented with 10% dialyzed calf
serum or fetal calf serum depends on the glucose concentration of
the medium. These determinations were carried out by inoculating 32
mm petri dishes with 10.sup.3 or 10.sup.4 cells in 2.0 ml of medium
and counting the number of cells per culture at daily intervals.
The doubling times taken from the exponential portion of the growth
curves are independent of glucose concentration at the
physiological range (1 mg/ml) or higher. Below 300 .mu.g/ml the
growth rates decline; but even at 1 .mu.g/ml, a glucose
concentration 1,000 fold lower than physiological, two of the lines
grow with a doubling time of less than 50 hours without any initial
delay attributable to adaptation. At still lower glucose
concentrations, cell number does not increase and there is
noticeable cell death and detachment. From these experiments, it
can be seen that the preferred glucose concentration in a mammalian
cell medium is from about one microgram to about 100 micrograms per
milliliter of medium. Mass cultures can be grown indefinitely
(>20 generations) at these glucose concentrations if the cell
number is kept low and the cultures transferred before the glucose
is consumed.
The efficiency of glucose utilization is also improved by using
lower glucose concentrations. This is illustrated in FIG. 2 which
shows the number of cells grown per unit of glucose consumed at
varying glucose concentrations. Cultures with different initial
glucose concentrations were formed by inoculating petri dishes
containing 2.0 ml of Dulbecco-Vogt modification of Eagle's medium
and 10% dialyzed calf serum with 10.sup.4 cells which were allowed
to grow to maximal cell density. This density was attained when all
the glucose was consumed. These cultures were not refed. Ordinate
values were derived from the ratio, ##EQU1## At 1-3 mg/ml, the
number of cells produced is 5-20 fold greater than at the
physiological concentration of about 1 mg/ml. At all glucose
concentrations, the maximum cell number in fetal calf serum is
20-40% higher than in calf serum.
Doubling times and maximal cell density in low glucose
concentrations were estimated for FIGS. 1 and 2 as follows.
Subconfluent, growing cultures in medium containing 4.5 mg/ml
glucose and 10% calf serum were removed with isotonic EDTA and
trypsin, diluted into glucose-free medium for counting, then
centrifuged and resuspended in fresh glucose-free medium. 10.sup.3
or 10.sup.4 cells were plated in duplicate 32 mm dishes containing
2.1 ml of medium with 10% dialyzed calf serum and different glucose
concentrations. Beginning two to four days later, cultures were
trypsinized and the cells were counted daily until the cultures
failed to increase in cell number and began to degenerate due to
glucose starvation.
One method of conveniently adding the appropriate glucosidase to a
culture medium is to select a serum supplement which contains the
desired hydrolytic enzyme activity. As is known, different types of
serum contain differing types and amounts of enzyme activity. For
example, calf serum has been found to have three-fold greater
activity of .alpha.-amylase than fetal calf serum, whereas horse
serum has less than 10% of the activity of fetal calf serum.
Because of these differences, a convenient method of controlling
the amount of any particular glucosidase activity in the culture is
to select a serum containing the particular enzyme activity desired
and to add the serum in an amount sufficient to provide the desired
level of activity. Alternatively, another convenient method for
reducing the rate of hydrolysis is to use heat to inactivate part
of the enzymatic-activity. A serum having too high an activity, for
example, can be heated to an elevated temperature and cooled prior
to its addition to the culture medium to provide the desired
activity level.
The invention is further illustrated by the following examples:
EXAMPLE 1
Digestion of Starch and Liberation of Glucose by Enzymes of Fetal
Calf Serum under Cell Culture Conditions
A 10% stock solution of starch was prepared by dissolving 5 grams
of soluble starch, B grade (Calbiochem) in 50 ml of glass distilled
water by heating for about 30 minutes in a boiling water bath, and
then autoclaving for 15 minutes at 25 psi.
One part of the stock starch solution was introduced into 20 parts
of serum-free, Dulbecco-Vogt modification of Eagle's medium. The
medium was maintained at 37.degree.C. for over 20 days, after which
time there was no detectable decline in the amount of starch and no
liberation of glucose.
The same procedure was followed except substituting medium
containing 10% fetal calf serum. This time, starch disappeared with
a half-life of about 35 minutes and was near the limit of detection
4 hours later. Glucose appeared in the medium, but less rapidly,
since molecules containing fewer than 8 saccharide units give no
color in the starch-iodine reaction, but must be further hydrolyzed
to yield glucose. The glucose concentration in the medium reached
25 .mu.g/ml within an hour, a concentration fully able to support
cell growth. The concentration rose to 100 .mu.g/ml by four hours,
and continued to rise until, by about 10 days, a maximum of about
50% of the starch was converted to glucose.
Glucose and starch determinations were done as follows. The glucose
oxidase reaction, coupled with the oxidation of a chromogen
("Glucostat special", Worthington Biochemical Corp.) gives a
yellow-brown color with maximum absorption at 400 nm. 0.6 ml of
diluted unknowns, standards and a glucose-free blank were
deproteinized by the successive additions of 0.3 ml of 2%
ZnSO.sub.4.7H.sub.2 O and 0.3 ml 0.46% NaOH and centrifuged at
4,000 g for 10 min. Equal volumes of the supernatant and glucostat
reagent were mixed and incubated at 37.degree.C.; the reaction was
stopped by the addition of two drops of 4.0 N HCl. The length of
incubation with the glucostat reagent was adjusted to make the
absorption of the standard solutions proportional to their glucose
concentration in the range of interest. The assay was accurate over
a range of 1 .mu.g/ml to 5 mg/ml.
A modification of the iodine method of Smith and Roe (1949) was
used. Iodine reagent was prepared by adding 18 mg iodine dissolved
in 1 ml ethanol, to 320 ml of 3.5 mM KI. Concentrated HCl was added
to a concentration of 0.01 N. The reagent was stored in a brown
bottle and was prepared fresh every other day. Starch solutions
were diluted from 1:1 to 1:40 in iodine reagent so as to give
absorption proportional to starch concentration over a range of 20
.mu.g-5 mg perml. The color is stable for several hours at
dilutions of 1:20 or 1:40 of sample to reagent, but fades rapidly
at 1:1 dilution.
The results of this Example are shown graphically in FIG. 3.
EXAMPLE 2
Inactivation of Serum Enzymes Liberating Glucose from Starch and
from Maltose
Glucose-free, fetal calf serum, which contains amylase and maltase,
was heated in a water bath under various conditions and then tested
for its ability to release glucose from starch. The serum was
dialyzed at 4.degree.C. for 24 hours against three changes of 20
volumes of isotonic phosphate buffered salt solution (pH 7.3) and
finally for 10-18 hrs. against 5 volumes of glucose-free F12 medium
(Ham, 1965). This serum supported growth as well as undialyzed
serum, but glucose-free Dulbecco-Vogt medium could not substitute
for Ham's medium in the final dialysis without reduction in growth
rate and cloning efficiency. The level of glucose in the dialyzed
serum was below the limit of detection by the glucose oxidase assay
(1 .mu.g/ml). The serum was sterilized by filtration before
use.
FIG. 4 shows that the ability to release glucose from starch was
virtually completely lost after heating at 65.degree.C. for 90 min.
The maltase activity was more resistant; its inactivation required
30 min. at 70.degree.C. In the absence of serum, the glucose
oxidase assay of a 5 mg/ml maltose solution gave a value of 4
.mu.g/ml of glucose equivalent; this may represent contaminating
glucose.
EXAMPLE 3
Growth of V79 Cells on Starch or Maltose as Secondary Glucose
Sources
V79 cells (5.times.10.sup.3) were inoculated into 32 mm petri
dishes containing 2.0 ml of glucose-free Dulbecco-Vogt modification
of Eagle's medium. 4.5 mg/ml of either starch, maltose or glucose
were added.
The V79 cells grew on glucose liberated from starch or maltose by
the enzymes of fetal calf serum with virtually no initial period of
glucose starvation as shown in the upper panel of FIG. 5. The
growth curves of V79 cells in starch, maltose or glucose were
virtually identical, the doubling time being about 12 hours.
The middle panel of FIG. 5 shows that cells grown in free glucose
consumed nearly 90% of the added glucose in ten days. Glucose
liberated from maltose or starch by the serum was not appreciably
consumed by the cells for the first three days, but thereafter the
increased cell number reduced the glucose concentration to very low
levels, production and consumption presumably continuing
concurrently.
The bottom panel of FIG. 5 shows how the pH of the medium was
affected by the source of glucose in the culture. When the high
concentration of free glucose was present from the outset, the pH
eventually dropped below 6.6. In cultures containing secondary
glucose sources, the pH fell very little; the final values were 7.0
for maltose and 7.1 for starch, scarcely lower than the starting
value. From this data, it is clear that at the lower glucose levels
maintained by sustained release from starch or maltose, more
efficient glucose utilization results in much less acid
production.
EXAMPLE 5
Growth of V79 Cells on Reduced Initial Concentrations of Glucose
and Maltose
The procedure of Example 4 was followed except that an initial
concentration of glucose of 500 .mu.g/ml was used, and a low
initial concentration of maltase activity was established by using
a fetal calf serum supplement consisting of 9 parts heat
inactivated serum (70.degree., 30 minutes) and one part unheated
serum. Under these conditions, the growth rate in added glucose was
a little more rapid than in maltose as shown in the upper panel of
FIG. 6. By the fourth day, however, the glucose was no longer
detectable in the medium; cell number did not increase further, and
two days later began to decline, due to cell death and detachment.
The maltose-grown cells reached a higher saturation density and
remained healthy in appearance; free glucose could be detected in
the medium throughout the experiment as shown in the bottom panel
of FIG. 6.
EXAMPLE 6
Growth of V79 Cells on Glucose Released From Glycogen by Amylase in
Fetal Calf Serum
V79 cells (10.sup.4) were inoculated into culture media prepared as
in Example 3 but substituting glycogen for starch. Each day the
cultures were examined by microscope and it was observed that the
cells grew at the same rate and to the same density as a culture
containing glucose, but the medium did not become acidic.
* * * * *