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Claims  |
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What is claimed is:
1. In a process for selectively cleaving a fusion protein produced from a
genetically engineered microorganism containing a foreign gene, the fusion
protein comprising native protein segment and foreign protein and the
cleavage selectively occurring between the native and foreign protein the
improvement comprising incorporating the tetrapeptide sequence
Pro-Xyz-Gly-Pro between the native and foreign protein, wherein Xyz can be
any natural amino acid and its carboxy end is attached to the amino end of
Gly, and reacting the fusion protein with a collagenase whereby said
Xyz-Gly bond is selectively cleaved, thereby producing a foreign protein
with the sequence Gly-Pro at its N-terminal end.
2. The process of claim 1 wherein the collagenase is E.C. 3.4.24.3.
(Clostridiopeptidase A).
3. The process of claim 1 further comprising subsequently selectively
cleaving said glycine residue from the N-terminal end of the produced
protein with an aminoacylproline aminopeptidase.
4. The process of claim 3 wherein the collagenase is E.C. 3.4.24.3, and the
aminoacylproline aminopeptidase is aminopeptidase P, E.C. 3.4.11.9.
5. The process of claim 3 further comprising selectively cleaving said
terminal Pro therefrom with a proline aminopeptidase.
6. The process of claim 5 wherein the proline aminopeptidase is E.C.
3.4.11.5.
7. The process of claim 5 wherein the cleavage of the glycine residue with
an aminoacylproline aminopeptidase and of the proline residue with proline
aminopeptidase is conducted in one step.
8. The process of claim 1 further comprising selectively cleaving said
Gly-Pro residue from the N-terminal end of the produced foreign protein
using postproline dipeptidylaminopeptidase.
9. The process of claim 1 wherein the foreign protein itself is terminated
by the sequence Uvw-Pro at its N-terminal end, and which further comprises
incorporating the amino acid Zxy on the carboxy end of the sequence
Pro-Xyz-Gly-Pro, wherein Zxy and Uvw independently each are any natural
amino acid except Pro, whereby after the selective collagenase reaction,
there is produced a protein with the sequence Gly-Pro-Zxy-Uvw-Pro at its
N-terminal end.
10. The process of claim 9 wherein the amino acid Zxy is Met.
11. The process of claim 9 further comprising, subsequently selectively
cleaving said Pro-Zxy-bond by treating the protein with postproline
dipeptidylaminopeptidase, thereby producing a protein having the sequence
Zxy-Uvw-Pro at its N-terminal end.
12. The process of claim 11 wherein the amino acid Zxy is Met.
13. The process of claim 11 further comprising selectively cleaving said
Zxy residue from the resultant protein by treating the latter with leucine
aminopeptidase.
14. The process of claim 13 wherein the amino acid Zxy is Met.
15. The process of claim 13 wherein the leucine aminopeptidase is E.C.
3.4.11.1.
16. The process of claim 15 wherein the amino acid Zxy is Met.
17. In a process for selectively cleaving a fusion protein produced from a
genetically engineered microorganism containing a foreign gene, the fusion
protein comprising native protein and foreign protein, the cleavage
selectively occurring between the native and foreign protein, and the
foreign protein being terminated at its N-terminal end by Pro, the
improvement comprising incorporating the tripeptide sequence Pro-Xyz-Gly
between the native and the foreign protein, wherein Xyz can be any natural
amino acid and its carboxy end is attached to the amino end of Gly, and
reacting the fusion protein with a collagenase whereby said Xyz-Gly bond
is selectively cleaved, thereby producing a foreign protein with the
sequence Gly-Pro at its N-terminal end.
18. The process of claim 17 wherein the collagenase is E.C. 3.4.24.3
(Clostridiopeptidase A).
19. The process of claim 17 further comprising subsequently selectively
cleaving said glycine residue from the N-terminal end of the produced
protein with an aminoacylproline aminopeptidase.
20. The process of claim 19 wherein the collagenase is E.C. 3.4.24.3, and
the aminoacylproline aminopeptidase is aminopeptidase P, E.C. 3.4.11.9.
21. In a process for selectively cleaving Met from a foreign protein
produced from a genetically engineered microorganism containing a foreign
gene using the direct synthesis method wherein first the codon for Met is
incorporated at the terminus of the foreign gene, whereby after culturing
the microorganism, a foreign protein is obtained having Met attached to
its N-terminal end, the improvement comprising first incorporating into
the foreign gene the codons for Met-Pro attached to the N-terminal end of
the subsequently produced foreign protein instead of only Met, whereby
after culturing the microorganism Met-Pro is attached to the N-terminal
end of the obtained foreign protein, and subsequently, selectively
enzymatically cleaving Met-Pro to produce the foreign protein per se by
treatment with postproline dipeptidylaminopeptidase.
22. In a process for selectively cleaving Met from a foreign protein
produced from a genetically engineered microorganism containing a foreign
gene using the direct synthesis method wherein first the codon for Met is
incorporated at the terminus of the foreign gene, whereby after culturing
the microorganism, a foreign protein is obtained having Met attached to
its N-terminal end, and wherein the foreign protein per se contains the
sequence Uvw-Pro- at its N-terminal end, the improvement comprising first
incorporating into the foreign gene the codons for Met-Pro-Zxy attached to
the N-terminal end of the subsequently produced foreign protein instead of
only Met, whereby after culturing the microorganism, Met-Pro-Zxy is
attached to the N-terminal end of the obtained foreign protein, Uvw and
Zxy being any natural amino acid except Pro, and subsequently, selectively
enzymatically cleaving Met-Pro from the N-terminal end by treatment with
postproline dipeptidylaminopeptidase thereby producing a foreign protein
having Zxy at its N-terminal end, and then selectively cleaving Zxy by
treatment with leucine aminopeptidase to produce the foreign protein per
se.
23. In a process for selectively cleaving Met from a foreign protein
produced from a genetically engineered microorganism containing a foreign
gene using the direct synthesis method wherein first the codon for Met is
incorporated at the terminus of the foreign gene, whereby after culturing
the microorganism, a foreign protein is obtained having Met attached to
its N-terminal end, the improvement comprising first incorporating into
the foreign gene the codons for Met-Pro attached to the N-terminal end of
the subsequently produced foreign protein instead of only Met, whereby
after culturing the microorganism, Met-Pro- is attached to the N-terminal
end of the obtained foreign protein, and subsequently, selectively
enzymatically cleaving Met from the N-terminal end by treatment with
amino-acylproline aminopeptidase thereby producing a foreign protein
having Pro at its N-terminal end, and then selectively cleaving Pro by
treatment with proline aminopeptidase to produce the foreign protein per
se. |
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Claims  |
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Description  |
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BACKGROUND OF THE INVENTION
The present invention relates to a process for specifically cleaving
proteins such as fusion proteins derived from genetically engineered
microorganisms.
In the synthesis of foreign proteins (e.g., mammal proteohormones) by
genetically modified microorganisms, the foreign gene which codes for the
desired protein sequence is incorporated into a structural gene of the
microorganism. Concomitantly, the regulation sites on the microbial
structural gene remain functional; thus, protein biosynthesis can occur in
the usual way from the microbial starting codon for methionine to the stop
codon on the foreign gene.
As a result of this protein manufacture, a fusion protein is obtained as
the primary product. It contains at the amino terminal end, a more or less
long sequence of the microbial indigenous protein, in the special case of
the so-called "direct synthesis" only the starting amino acid methionine,
and the carboxy terminal end, the desired foreign protein. For its
subsequent use, the foreign protein must first be processed by a specific
cleavage from this fusion protein. The only method known for this cleavage
at the present time is a reaction with cyanogen bromide which leads to a
cleavage of the peptide sequence at the carboxy end of methionine residues
(S. B. Needleman, "Protein Sequence Determination", Springer Publishers,
1970, N.Y.). Accordingly, it is necessary for this purpose that the
foreign gene, at the 5'-end of the codegenic strand, contain an additional
codon for methionine, whereby a methionine residue is disposed between the
N-terminal native protein sequence and the foreign protein of the fusion
protein. This method, however, fails if other methionine residues are
present in the desired foreign protein per se. Additionally, the cleavage
with cyanogen bromide has the disadvantage of evoking secondary reactions
at various other amino acids.
SUMMARY OF THE INVENTION
Accordingly, it is an object of this invention to provide a new process for
cleaving a foreign protein from the native protein sequence of a fusion
protein, which process is free from the foregoing disadvantages.
Upon further study of the specification and appended claims, further
objects and advantages of this invention will become apparent to those
skilled in the art.
It has now been found that it is possible to process such a foreign protein
without the usual secondary reactions, even in the presence of methionine
residues, by a selective enzymatic hydrolysis, if there is in the fusion
protein, at the amino-terminal end of the foreign protein sequence, a
tetrapeptide of the general formula Pro-Xyz-Gly-Pro-(amino-terminal end of
foreign protein), wherein Xyz is any desired amino acid. The overall
cleavage is effected by first selectively cleaving the Xyz-Gly bond with a
collagenase (E.C. 3.4.24.3., Clostridiopeptidase A) then removing the
glycine residue with an aminoacylproline aminopeptidase (aminopeptidase-P,
E.C. 3.4.11.9.) and removing the proline residue with a proline
aminopeptidase (E.C. 3.4.11.5). Instead of both enzymes also the PPDA can
be used.
The process of this invention, therefore, comprises the specific enzymatic
cleavage of a fusion protein obtained by genetic engineering, the protein
carrying at the linkage point of the native protein sequence and the
foreign protein a collagenase-specific tetrapeptide sequence of the
formula Pro-Xyz-Gly-Pro, wherein the enzymes collagenase, aminoacylproline
aminopeptidase and proline aminopeptidase or PPDA respectively are
utilized for the enzymatic cleavage.
This invention also relates to several variations of the process whereby
other enzymatic cleavages are utilized to sever the protein sequence
dependent on the genetic technological processing (fusion protein or
direct synthesis) respectively on the N-terminal sequence of the desired
foreign protein (proline in position 1 or 2).
DETAILED DISCUSSION
Herein, Xyz refers to all naturally occurring amino acids contained in the
genetic code.
The collagenase required for the enzymatic cleavage of the desired protein
from the fusion protein must be extensively free of other proteases. The
enzyme is produced, for example, by Clostridium histolyticum and can be
obtained by a fermentation thereof in fully conventional manner according
to fully conventional methods. The collagenase is also available
commercially in purified form. To block the proteases which are usually
still present in small amounts in most preparations, a protease inhibitor,
e.g., diisopropyl fluorophosphate, N-ethylmaleinimide,
phenylmethylsulfonylfluoride, can be added during the incubation with the
fusion protein. Collagenase itself is not inhibited by this inhibitor.
During the collagenase reaction, the desired foreign protein extended by
the sequence Gly-Pro at the amino terminal is produced. This modified
foreign protein (as well as the subsequently obtained protein per se) can
be separated from the reaction mixture using fully conventional methods
and considerations. The methods to be used for this purpose are, as usual,
dependent on the specific properties of the compound, determined
essentially by the desired foreign protein (e.g., proinsulin, insulin A-
or B-chain, ACTH, STH). See, e.g., the examples.
The cleavage of the glycine and the proline residues using the two specific
aminopeptidases can be achieved in two separate sequential hydrolysis
batches or, as in most cases, by a combined incubation with both enzymes.
Aminopeptidase-P can be isolated from an Escherichia coli strain, for
example, strain B, e.g., as described in Biochem. and Biophys. Res. Comm.
32: 658-663 (1968) by ammonium sulfate fractionation, acetone
precipitation, and chromatography on calcium phosphate, DEAE cellulose and
"Sephadex G-200". The proline aminopeptidase likewise can be isolated from
an Escherichia coli strain, e.g., from the strain K 12. This proline
aminopeptidase is obtained in an adequately pure form after ammonium
sulfate fractionation and conduction of two chromatographs on DEAE
cellulose. It must be free of less specific aminopeptidases [J. Biol.
Chem. 234: 1740-1746 (1959); ibid. 237: 2207-2212 (1962)].
The cleavage reactions with the enzymes are conducted by dissolving the
fusion protein, e.g., in a suitable buffer such as tris buffer or
phosphate buffer (e.g., especially at a pH of 6-9), depending on the
solubility properties of the particular fusion protein involved. The
specific enzyme(s) is added to the solution and incubation ensues at a
temperature and time optimized, e.g., by routine, conventional
experiments, generally 25.degree.-40.degree. C., for 0.5-10 hours.
It has furthermore been found that the dipeptide sequence Gly-Pro, which
after the cleavage of the Xyz-Gly bond of the N-terminal tetrapeptide
sequence of the fusion protein with a cellagenase, is still present at the
amino-terminal end of the foreign protein sequence, can be split off in
one step with a postproline dipeptidylaminopetidase. Such a postproline
dipeptidylaminopeptidase is readily accessible according to literature
disclosures [Biochem. Biophys. Acta 485: 391 (1977)]. Use of postproline
dipeptidylaminopeptidase (PPDA) can be conducted as follows. The protein,
e.g., the foreign protein cleaved from the fusion protein is dissolved in
a suitable buffer, such as, for example, tris buffer or phosphate buffer
(wherein the pH is especially advantageously in the range of 7-8),
depending on the solubility properties of the protein, and incubated with
PPDA at 30.degree.-40.degree. C., preferably around 37.degree. C. The
reaction time is extensively determined by the dissolved protein, in the
majority of cases 3-5 hours are sufficient.
The advantages in the use of this enzyme reside in the higher activity of
this dipeptidylaminopeptidase and in the convenient working-up procedure
for the end product. This high activity, which permits a very economical
use of the process, remains preserved even after binding of the enzymes on
a polymeric support, whereby the process is substantially simplified.
Since the splitting-off of the two amino acids takes place in one step,
the final product, in the case of an incomplete cleavage, need not be
separated from two by-products (the starting compound and the starting
compound shortened by one amino acid) during the final purifying step.
Only the starting compound is involved.
Moreover, this variation of the process can be generalized since by means
of this process it is possible to cleave from a protein not only Gly-Pro,
but also all other amino-terminally bound dipeptide sequences Yzx-Pro.
Postproline dipeptidylaminopeptidase is not specific with respect to the
amino acid located in front of proline. Therefore this enzyme can also be
utilized in the known so-called "direct synthesis" for converting the
primary fusion protein, which contains an additional methionine residue as
the start codon for protein biosynthesis into the desired foreign protein.
In this case, a codon for proline must be attached at the 5' end of the
proteincoding nucleotide sequence. In this case, the foreign protein
prolonged by Met-Pro at the amino terminal is then obtained as the primary
product from which the terminal Met-Pro sequence can readily be split off
with postproline dipeptidylaminopeptidase. However, this variation of the
process cannot be employed if the desired foreign protein sequence starts
at the N-terminal end with proline or with aminoacylproline.
Herein Xyz independently can be any naturally occurring amino acid
contained in the genetic code. In the following, Uvw and Zxy is any such
naturally occurring amino acid except for proline.
An apparent limitation of this variation is that when the desired foreign
proteins contain at the N-terminal yet another proline as the second amino
acid, as is the case for the human growth hormone or for the cattle
prolactin, then PDDA would continue digestion to a protein shorter by the
proline-containing dipeptide. However, it has now been found that even
foreign proteins having proline as the second N-terminal amino acid can be
obtained from fusion proteins by means of this invention, if an additional
amino acid Zxy, which can be any desired amino acid in the genetic code
except for proline, is inserted between the otherwise coded sequence,
e.g., the tetrapeptide sequence Pro-Xyz-Gly-Pro, and the desired foreign
protein. After, for example, the collagenase cleavage of the Xyz-Gly bond
of the pentapeptide sequence Pro-Xyz-Gly-Pro-Zxy, it is then possible to
split off the dipeptide Gly-Pro with the enzyme PPDA without attacking the
proline-containing foreign protein.
Thereafter, the remaining amino acid Zxy is split off by an enzymatic
method using leucine aminopeptidase [LAP, E.C. 3.4.11.1),
.alpha.-aminoacylpeptide hydrolase]. With this enzyme, it is also possible
to split off N-terminal methionine from foreign proteins containing after
the "direct synthesis" the sequence Met-Uvw-Pro, wherein Uvw is any
desired amino acid except for proline. Heretofore, the only available
method was the mentioned one with cyanogen bromide by S. B. Needleman
which proceeds with secondary reactions and is limited to proteins which
do not contain other methionine residues in the desired foreign protein.
In general, this proceeds with secondary reactions. In general, this
enzyme can be used to cleave the sequence Zxy-Uvw-Pro at the Zxy-Uvw bond,
providing Zxy is an N-terminal group.
Accordingly, by the introduction of the additional amino acid Zxy, such as,
for example, leucine or glycine, between the collagenase-specific sequence
and the foreign protein sequence, the advantages of the high enzyme
activity of PPDA and the easier purification of the cleavage products can
be expanded to obtaining desired foreign proteins having an N-terminal
sequence Uvw-Pro.
In this case, yet another codon for the amino acid Zxy must be introduced
between the collagenase-specific nucleic acid sequence and the
foreign-protein-coding nucleic acid sequence. If the desired protein has
an N-terminal proline residue the process of this invention can be used in
analogous manner. If the case of a fusion protein this N-terminal proline
residue is already the last residue of the collagenase specific sequence
Pro-Xyz-Gly-Pro and the collagenase and the aminoacylpyroline
aminopeptidase must be used; while in the case of the direct synthesis a
Met-Pro-protein is obtained from which the methionine residue can be
removed with the aminoacylprolin aminopeptidase. All of the mentioned
coding operations can be effected by fully conventional genetic
engineering techniques. See, for example, Progress in Molecular and
Subcellular Biology, Vol. 6, 1978, Springer, Berlin (Editor Fred E. Hahn)
and A. D. Riggs et al. Am.J.Hum.Gen. 31(1979), 531-538, which disclosure
is incorporated by reference herein.
The foreign protein, N-terminally extended by an amino acid, can be
dissolved in a suitable buffer, such as, for example, tris buffer or
phosphate buffer (pH 8-10, preferably 8.6) in order to activate the LAP.
The protein is customarily combined with 1-5 millimoles per liter of
MnCl.sub.2. After the LAP is added to the protein solution, it is
incubated at 35.degree.-40.degree., preferably at 40.degree. C. The
reaction period depends heavily on the N-terminal amino acid to be split
off and can range between a few minutes and several hours. Details, as
with all of the reactions involved herein, can be determined by routine,
conventional experiments and considerations.
The desired foreign protein finally present in the free form can be
isolated in its pure form according to the fully conventional methods of
protein purification. The methods used in this connection are primarily
determined by the properties of the foreign protein (e.g., proinsulin,
insulin A- or B-chain, ACTH, STH), and the properties of the compounds to
be separated therefrom.
The following examples show that the enzyme postproline
dipeptidylaminopeptidase accepts as a substrate not only model peptides,
but also higher-molecular weight proteins. In these examples, the specific
enzymes employed are those specific ones mentioned above in each case.
Without further elaboration, it is believed that one skilled in the art
can, using the preceding description, utilize the present invention to its
fullest extent. The following preferred specific embodiments are,
therefore, to be construed as merely illustrative, and not limitative of
the remainder of the disclosure in any way whatsoever.
In the following examples all temperatures are set forth uncorrected in
degrees Celsius; unless otherwise indicated, all parts and percentages are
by weight.
EXAMPLE 1
140 mg of Z-Gly-Pro-Leu-Gly-Pro-insulin-A-chain (50 .mu.mol) is dissolved
in 10 ml of 0.05 mol/l of tris buffer (pH 7.2) containing 0.1 mol/l of
calcium acetate and, to prevent hydrolysis at an undesirable location by
contamination of the collagenase by other proteases, 0.1 mmol/l of
diisopropyl fluorophosphates, and is combined with 10 mg of collagenase.
After 60 minutes at 28.degree. the reaction is stopped by adding ethanol.
After precipitated enzyme has been filtered off, the alcohol is
exhaustively evaporated under vacuum, and the solution is desalted by
chromatography on "Sephadex G-15" with 0.01 mol/l of ammonium bicarbonate
as the eluent. The eluate is concentrated under vacuum to a small volume
and freeze-dried. Yield: 110 mg of Gly-Pro-insulin-A-chain. By means of
end group determination (DNP method), glycine can be proven to be the
N-terminal amino acid. The thus-obtained product is used directly for the
further reaction.
EXAMPLE 2
Separate Cleavage of the First Two N-Terminal Amino Acids
50 mg of Gly-Pro-insulin-A-chain is dissolved in 1 ml of 0.1 mol/l of tris
buffer (pH 8.5) containing 0.5 mmol/l of MnCl.sub.2. To this is added 2
.mu.g of aminopeptidase-P and the mixture is incubated for 1 hour at
37.degree.. By brief heating to 60.degree. the mixture is inactivated,
and, without further purification, 20 .mu.g of proline aminopeptidase is
added. After 24 hours at 37.degree. the high-molecular proteins are
removed by precipitation with alcohol and filtration. The filtrate is
concentrated under vacuum, taken up in 0.01 mol/l of ammonium bicarbonate
buffer (pH 9), and desalted by chromatography on "Sephadex G-25." The
insulin-A-chain fraction is introduced directly to an AE cellulose column
and chromatographed with an ammonium bicarbonate gradient (0.01-0.1 mol/l,
pH 9). By concentration and freeze-drying of the insulin-A-chain fraction,
40 mg of insulin-A-chain is obtained.
Amino acid analysis:
__________________________________________________________________________
Asp Thr
Ser
Glu
Gly
Cys Val
Ile
Leu
Tyr
__________________________________________________________________________
Calculated
2.00
1.00
2.00
4.00
1.00
4.00 1.00
2.00
2.00
2.00
Found 1.98
0.92
1.64
3.79
1.02
not 0.98
1.99
2.04
1.86
determined
__________________________________________________________________________
EXAMPLE 3
Combined Cleavage of the First Two N-Terminal Amino Acids
As in Example 2, 50 mg of Gly-Pro-insulin-A-chain is dissolved in 1 ml of
tris buffer. Then, 2 .mu.g of aminopeptidase-P and 20 .mu.g of proline
aminopeptidase are added thereto. After a reaction time of 18 hours at
37.degree. the mixture is precipitated with alcohol and worked up as
described in Example 2.
Yield: 30 mg of insulin-A-chain.
EXAMPLE 4
200 mg of Z-Gly-Pro-Leu-Gly-Pro-insulin-B-chain is reacted as set forth in
Example 1.
Yield: 150 mg of Gly-Pro-insulin-B-chain which can be further processed
without any purification.
EXAMPLE 5
100 mg of Gly-Pro-insulin-B-chain produced according to Example 4 is
dissolved in 5 ml of tris buffer and incubated as described in Example 2
in succession with aminopeptidase-P and proline aminopeptidase, desalted
on "Sephadex G-25" and purified by chromatography.
Yield: 70 mg of insulin-B-chain.
Amino acid analysis:
__________________________________________________________________________
Asp Thr
Ser
Glu
Gly
Pro
Cys
Phe
Val
Leu
Ala
Tyr
His
Lys
Arg
__________________________________________________________________________
Calculated
1.00
1.00
1.00
3.00
3.00
1.00
2.00
3.00
3.00
4.00
2.00
2.00
2.00
1.00
1.
Found 0.95
0.92
0.83
3.12
3.02
0.98
1.75
2.98
3.10
3.96
2.04
1.89
1.94
1.06
0.
__________________________________________________________________________
EXAMPLE 6
15 mg of Z-Gly-Pro-Gly-Gly-Pro-Ala-Met-Glu-His-Phe-Arg-Trp-Gly is reacted
as described in Example 1.
Yield: 10 mg of Gly-Pro-Ala-Met-Glu-His-Phe-Arg-Trp-Gly.
EXAMPLE 7
10 mg of Gly-Pro-Ala-Met-Glu-His-Phe-Arg-Trp-Gly prepared according to
Example 6 is reacted as in Example 3 with both aminopeptidase-P and
proline aminopeptidase. For purifying purposes, the mixture, after
precipitation of the enzymes with ethanol, is concentrated to a small
volume and chromatographed over carboxymethylcellulose with an ammonium
acetate gradient (0.01-0.2 mol/l).
Yield: 7 mg of Ala-Met-Glu-His-Phe-Arg-Trp-Gly,
Amino acid analysis:
______________________________________
Glu Gly Phe Ala Met His Arg Trp
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Calculated
1.00 1.00 1.00 1.00 1.00 1.00 1.00 1.
Found 1.03 1.01 0.98 1.02 0.81 0.93 0.97 n.
______________________________________
EXAMPLE 8
50 mg of Gly-Pro-Ala is incubated with 700 .mu.g of postproline
dipeptidylaminopeptidase (designated PPDA hereinbelow) in 2 ml of tris
buffer (20 mmol/l, pH 7.8) for 3 hours at 37.degree.. The cleavage batch
is combined with 1 ml of ethanol to remove the enzyme, and the
thus-precipitated enzyme is filtered off. The filtrate is taken up, after
concentration, in NH.sub.4 HCO.sub.3 buffer (0.01 mol/l, pH 7.4) and, to
separate the mixture, chromatographed over a cellulose column. After
combining the corresponding fractions, the mixture is concentrated under
vacuum and twice freeze-dried.
Yield: 13 mg of alanine (70%).
EXAMPLE 9
75 mg of Gly-Pro-Ser-Tyr-.beta. NA is incubated with 700 .mu.g of enzyme as
described in Example 1. To separate the mixture, the thus-formed
Ser-Tyr-.beta. NA is extracted with ethyl acetate and, after
concentration, reprecipitated twice from methanol/ether.
Yield: 43 mg (74%) of Ser-Tyr-.beta. NA, m.p. .about.205.degree.
(decomposition).
EXAMPLE 10
50 mg of Gly-Pro-insulin-A-chain-tetra-S-sulfonate (cattle) is dissolved in
2 ml of tris buffer (0.1 mol/l, pH 8.0) and combined with 100 .mu.g of
PPDA. After 4 hours at 37.degree., the mixture is chromatographed over
"Sephadex G50" with 0.01 mol/l of NH.sub.4 HCO.sub.3 (pH 7.5) as the
eluent. After combining the corresponding fractions, the mixture is
concentrated to a small volume and twice freeze-dried.
Yield: 43 mg of insulin-A-chain.
The product can be degraded with leucine aminopeptidase, in contrast to the
starting compound.
Amino acid analysis
__________________________________________________________________________
Asp Ser
Gln
Gly
Cys
Val
Ala
Ile
Leu
Tyr
Pro
__________________________________________________________________________
Calculated
2.00
2.00
4.00
1.00
4.00
2.00
1.00
1.00
2.00
2.00
0.00
Found 1.97
1.70
4.02
1.05
n.b.
1.99
0.97
1.04
2.08
1.78
0.04
__________________________________________________________________________
EXAMPLE 11
20 mg of prolactin hexa-S-sulfonate is dissolved in 5 ml of tris buffer
(0.5 mol/l, pH 7.2) and combined with 0.1 mol/l of calcium acetate and 0.1
mmol/l of diisopropyl fluorophosphate as well as with 5 mg of collagenase.
After 30 minutes at 30.degree. the reaction is stopped by the addition of
ethanol. After concentration under vacuum, the mixture is taken up in 0.02
mol/l of tris buffer, pH 7.8, and chromatographed over a "Sephadex G75"
column with the same buffer as the eluent. The combined fractions are
desalted by dialysis against demineralized water and, after freeze-drying,
taken up in 4 ml of tris buffer (0.1 mol/l, pH 7.9) and incubated with 5
.mu.g of PPDA for 2 hours at 37.degree.. The mixture is again
chromatographed over "Sephadex G75", the corresponding fractions are
combined, dialyzed, and freeze-dried.
Yield: 10 mg of desoctapeptide-prolactin-penta-S-sulfonate.
In contrast to the starting compound, Gly can be determined as the
N-terminal amino acid. Furthermore, the final product can be degraded with
LAP, as contrasted to the intermediate compound.
EXAMPLE 12
150 mg of Met-Pro-Ser-Tyr-.beta. NA is reacted with 1 mg of postproline
dipeptidylaminopeptidase as described in Example 2 and worked up.
Yield: 80 mg (70%) of Ser-Tyr-.beta. NA, m.p. .about.208.degree.
(decomposition).
EXAMPLE 13
500 mg of Met-Gly-Pro-amide is incubated with 1 mg of activated leucine
aminopeptidase in 20 ml of tris buffer (30 mmol/l of tris.HCl, 2 mmol/l of
MnCl.sub.2, pH 8.6) for 30 minutes at 40.degree.. Gly-Pro-amide is
extracted under cooling with ethyl acetate and, after concentration under
vacuum, reprecipitated twice from ethanol/petroleum ether.
Yield: 242 mg=72%, m.p. 209.degree.-210.degree. (decomposition).
[.alpha.].sub.D =194.4.degree. (c=1, H.sub.2 O)
EXAMPLE 14
100 mg. of cattle growth hormone is incubated with 25 .mu.g of activated
leucine aminopeptidase in 10 ml of tris buffer (30 mmol/l of tris.HCl, 2
mmol/l of MnCl.sub.2, pH 8.6) for 30 minutes at 40.degree.. The protein is
then precipitated with ethanol, taken up in 1 ml of a bicarbonate buffer
(10 mmol/l of NH.sub.4 HCO.sub.3, pH 7.5), and the mixture is separated at
40.degree. over a "Sephadex G50" column (100 cm.times.1 cm .phi.) with the
same bicarbonate buffer. The fractions containing the desalanyl.sup.1
-growth hormone are combined, concentrated, and freeze-dried. After
dansylation and acidic hydrolysis, phenylalanine is determined as the
terminal-positioned amino acid by thin-layer chromatography.
Yield: 84 mg=84%.
EXAMPLE 15
100 mg of Gly-Pro-Leu-Gly-Pro-amide is incubated with 1 mg of PPDA in 5 ml
of tris buffer (20 mmol/l of tris.HCl, pH 7.3) for 3 hours at 37.degree..
The thus-produced Leu-Gly-Pro-amide is extracted under cooling with ethyl
acetate. After concentration, the mixture is taken up in tris buffer (30
mmol/l of tris.HCl, 2 mmol/l of MnCl.sub.2, pH 8.6), combined with 0.1 mg
of activated leucine aminopeptidase, and incubated for 30 minutes at
40.degree.. The final product is extracted under cooling with ethyl
acetate and, after concentration under vacuum, precipitated twice from
ethanol/petroleum ether.
Yield: 18.3 mg=47%, m.p. 209.degree.-210.degree. (decomposition).
[.alpha.].sub.D =194.4.degree. (c=1, H.sub.2 O).
The preceding examples can be repeated with similar success by substituting
the generically and specifically described reactants and/or operating
conditions of this invention for those used in the preceding examples.
From the foregoing description, one skilled in the art can easily ascertain
the essential characteristics of this invention, and without departing
from the spirit and scope thereof, can make various changes and
modifications of the invention to adapt it to various usages and
conditions.
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