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Patent 2031810 Summary

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(12) Patent Application: (11) CA 2031810
(54) English Title: PROCESS FOR THE EXPRESSION OF FOREIGN GENES IN YEASTS
(54) French Title: PROCEDE D'EXPRESSIVITE DE GENES ETRANGERS DANS LES LEVURES
Status: Deemed Abandoned and Beyond the Period of Reinstatement - Pending Response to Notice of Disregarded Communication
Bibliographic Data
(51) International Patent Classification (IPC):
  • C12P 1/02 (2006.01)
  • C12N 9/10 (2006.01)
  • C12N 15/81 (2006.01)
(72) Inventors :
  • BROKER, MICHAEL (Germany)
  • GROTE, MATHIAS (Germany)
(73) Owners :
  • BEHRINGWERKE AKTIENGESELLSCHAFT
(71) Applicants :
  • BEHRINGWERKE AKTIENGESELLSCHAFT (Germany)
(74) Agent: SMART & BIGGAR LP
(74) Associate agent:
(45) Issued:
(22) Filed Date: 1990-12-07
(41) Open to Public Inspection: 1991-06-09
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
P 39 40 651.2 (Germany) 1989-12-08

Abstracts

English Abstract


- 1 -
Abstract of the Disclosure
A process for the expression of foreign genes in yeasts
The invention relates to the optimization of the expres-
sion of foreign genes, especially recombinant factor
XIIIa (rFXIIIa) in yeasts. The optimization was essen-
tially carried out by use of a hybrid Gal UAS /CycI
promoter, deletion of the 5' non-translated region and
truncation of the 3' non-translated region of the FXIIIa
cDNA, selection of specific yeast strains and a par-
ticularly suitable growth medium composed of whey or whey
hydroly ate. Quantities achievable in this way are
? 100 mg/l FXIIIa in shake cultures and ? 500 mg/l in
fermentation after scale-up.


Claims

Note: Claims are shown in the official language in which they were submitted.


- 17 -
THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for the expression of foreign genes in yeasts
using a galactose-induciible promoter, which comprises
employing lactose hydroly sate, hydrolyzed whey powder or
using whey powder with the addition of .beta.-Galactosidase or
lactose-cleaving microorganisms.
2. The process as claimed in claim 1, wherein n partially
demineralized condensed cheese whey is employed.
3. The process as claimed in claim 1, wherein the Gal/CycI
hybrid promoter is employed.
4. The process as claimed in claim 1, wherein the Gal/CycI
hybrid promoter and the cDNA of the factor XIIIa gene
which has the 5' non-translated region deleted and the
3' non-translated region reduced from 419 to 120 base
pairs is employed.
5. The process as claimed in claim 4, wherein an expression
plasmid with the selection markers Leu2d, Ura3 and/or
Trpl is employed.
6. The process as claimed in claim 5, wherein the yeast
strain AH22, C13ALYS86 or 150-2B is employed.
7. A process for the expression of factor XIIIa in yeasts by
means of promoters of yeast genes involved in the degra-
dation of galactose.
8. The process as claimed in claim 7, wherein promoters of
the Gall or Gal10 gene or promoter-active parts thereof
are used.

- 18 -
9. The process for the expression of foreign genes in
yeasts as claimed in claim 1 and substantially as
described herein.

Description

Note: Descriptions are shown in the official language in which they were submitted.


2 ~
BEHRINGW~ TIE~3Gl~SE:Ll,SC~lA~r HOE 8g/B 046 - ~la 796
Dr. Lp~rd
D~scription
A process for the expression of forei~n ~enes Ln yea~t~
The invention relates to the optimization o~ the expreR-
~ion of foreign genes, especially reoombinant f~ctor
XIIIa [rFXIIIa) in yeas~ he optimization wa8 e~en-
tially carried out by use of a hybrid GaluAs /CycI
promoter, deletion of the 5' non-translated region and
truncation of the 3' non~transla~ed region of the FXIIIa
: cD~A, selection of specific yeast strains and a par-
ticularly sui~able growth medium compo~ed of whey or whey
hydrolyzate. Quantities achievable in thi~ way are
2 IOO mg/l FXIIIa in shake cultures and ~ 500 mg/l in
fermentation after scale up.
Clotting factor XIII (FXIII) forms the final member in
lS the coagulation cascade in the ~tural process of blood
clotting. FXIII was described as a ~erum factor for the
first time by Robbins in 1944. Robbins had observed that
fibrin clots from normal whole blood are in~oluble in
urea solution whereas clots from highly purified fibri-
: 20 nogen and thrombin are ~oluble.
. .
The molecular w~ight of FXIII from pla~ma is about
300 kd. The plasma protein i~ composed of subunit A of
about 80 Xd ~nd subunit b of about 75 kd and e~i~t3 as
a tetramer wi~h two a ~nd two b subunits t~2b2). Sub-
unit a tFXIIIa~ contain~ the enzymatic activity. FXIIIa
i activated by elevage of an ~nino-tenminal peptide
which is 4 kd in ~i~e by thrombin ~o ~ive FXII~a'. This
activated ~orm o~ FXIIIa act~ ln the presence of calcium
~ ions as a kran~glutamina~e and preduces cro~linked, via
`;1 30 intermolecular ~-glutamyl~~-ly~ine linkage~, fibrin
monomers to give fixmer clots.
The cDNA and the first instancas of expression of FXIIIa
'`" . :
.-~. . . :
:;.: . . .. . .
: :- . . . .

2~3~81~
in E. coli, animal cells and yaa3t~ iB described in
EP 0,236,~78. Th0 yield~ o~ active FXIIIa in yea~ts are,
however, rather low, at 150 ng/ml, in the process de~
cribed.
:
FXIIIa can be expre~Red in high yields in E. cDli (Amann
at al., Gene 69, 301-315 [1988]). However, ~oBt of the
FXIIIa synthesized in E. coli i~ in~oluble and thus not
- enzymatically active. A suitable alternati~e to hetexo-
logous e~pression in prokaryote~ i~ the synthe~i~ in
eukaryotic cells. Heterologou~ expression of biologically
- active FXI~Ia in CHO cell~ ha~ already been demon~trated
(Zettlmei~l und Rarge~, (19B9) r XIIth Consress of the
: International Society on Thrombos~ 8 and Haemo~tasis,
Tokyo). Nevertheless, the yields in this ca~e are inade-
lS quate to ensure cost-efficient production.
Yea~ts are suitable as host cells be ause, on the one
handl their genetics have been well characterized for
molecular biological operations/ cloning and expre~sion
vectors are available and~ ~s eukaryotes~ they poS8e66
the typical post-translational modifica~ion machanisms.
On the other hand~ as microorganisms, they have a rather
short generakion tLme ~nd there has been aufficiant
development of fermentation procasses for cult~ring
~ yeasts in high cell den~ity. It ha~ already been ~hown by
:: 25 way of example in European Patent Applic~tion
EP A2 0,236,978 that bioloyically actiYe FXIIIa can be
prepared in baker's yeast. Recombinant active F~IIla can
also be synthesized in the fi~sion yeast
: . Schizo~accharomyces pombe with the aid of molecular
biolo~ical techniques (Br~ker ~nd ~uml, F~BS Lett. 248,
105-110 [l9B9]). ~owever, the yield in the two examples
described il3 1 at 0.15 and 2 mg/l resp2ctivaly, no~ in a
:~ range which make~ preparation appear economic. Higher
yields are described in the EP Application A2 0,268,772.
Plasmids in which FXIIIa ~ynthesis i~ under the control
of the strong glycolytic TPI promotar result ~n a
synthesis rate of 10 mg/l. 50 mg/l are achieved usin~ the
~:.
.. . - ; :
;
.,
.

2031810
-- 3 --
ADHII promoter.
~ence the ob~ect was to improve the expres~ion of FXIIIa
so as to achieve values 2 100 mg/l. With such expre~sion
rates the genetically engineered prepar~ion of FXIIIa i8
more cost-effi~ien~ than cla~sical purification from
placentae.
We have found tha~ the use o~ a hybrid GaluAs /CycI
promoter, the deletion of the 5' non-tran~lated region
and a truncation of ~he 3~ non-tr?n~lated xegion of
FXIIIa cDNA in the expre~sion vector, the ~slection of
specific yeast strains and the U50 of a very suitable
growth medium containing glucose and galacto~e alone or
in combinati~n result in a high yield of F~IIIa. The
: hybrid Gal uAs~CycI promoter i8 derived from pENBLyex4
: 15 (Cesareni, G. und Murray, A.H. in Se~l~w, J.~. (ed.~
Genetic Engineering, Vol. 9, 135-154, Plenum Publi~hing
;~ Corporation, 1987).
. . ;, .
: Representative vector~ con~ain the FXIII cDN~ without the
5~ non-translated and 3~ non-translated cDNA region, the
latter preferably ~hortened from 419 base pairs (bp) to
only 120 bp. The synthesis of the specific vectors pMB307
and pMB330 is ~hown in the f igure and in the e~mples.
The fund~mental basic vector i~ the above ~entioned vector
pEMBLyex4 in whose polylinker the above mentioned
~runcated FXIIla cDNA has been ligated.
pEMBLyex4 is located episomally in yeast in a copy number
of abou~ 50/cell and carrie~ ~he 8e1QCtiOn markers Leu2d
; and ~ra3, so that complementation of yeast strains with
: the genotype leu2 and ura3 iB pos~ible; complementation
of Trpl ~trains al80 occurs on insertion of the Trpl g~ne
(see Example 2) in p~B307 to give p~B307T.
.~
Most ~uitable for p~B307 were the S. cerevi~iae strain~
AH22 and Cl.3A~YS8S, and for p~B307T the ~train 150-~B.
AH22 i~ described in A~ Hinnen et al. (Proc~ Natl. Acad.
~?'`:','
: ~,,':: :, ',' :, ' " ' , ' ''
'.' ' ~ ' ' ,
,~'' : '.
. ~, ,~, ,
::, . ' . .

2~31810
Sci. USA ~1978) 75, 1929-1933); C13~B~rS83 ha3 been
di~clo~ed in EP-Al-0, 327 " 797 " and 150-2B has been des-
cribed by C. Baldari et al. (EMB0 Journal, (1983), 6,
229-234L) .
The presence o~ glucsse in the mQdium repre~e~ ~he
induction of the Gal or Gal/u~s promo~ers by galacto~e.
Surprisin~ly, the ~ynthe~is r,ata increase~ v0ry greatly
when galacto~e i al~o pre~ent in the medium in addition
to glucose from the ~tart of the fermentation onwards.
Hydrolyzed whey powder i8 e~pecially ~uitable and,
moreover, is obtainable at low C08t by compar1son with
pure galacto~e. An alternative i~ whey powder with added
~-Galacto~idase or lactose-cleaving microorganisms.
~ccordingly, the invention relates ~o the uPe of hydro-
lyzed whey powder in conjunction with yea~t expressionplasmid~ under the control of a galactose-inducible
promoter (1), preferably the hybrid Gal uAs/CycI promoter
(2), and preferably the pEMBLyex4 vector framework into
which the FXIlIa cDNA from which the 5~ non-tran~lated
region has been deleted and the 3t non-tran~lated region
has been truncated hax been in~erted (3) is us~d.
Preferred 6trains for the expression are the ~trains AH22
t4) and C13ABYS86 (S) for Leu or Ura ~election and 150-2B
for ~rp selection (6).
The combination of the abovamentioned features (1), t2),
~3), (5) and (6) i~ particul~rly preferred ~or FXIIIa
expression optLmization. On implementation on the indu8-
trial scale in 100 1 or larger fermenters, F~IIIa con-
centrations 2 500 ~g~l were achieved with the ~bove-
mentioned proce~s.
The invention i8 ~urther described in the examples andthe patent cla.ims.
. ~ , . .
;" " '''
.':.~ ' :

203181~
-- 5 --
~xam~les:
The molecular biological techniques u~ed herain are
mainly based on ~aniatis et al.: Molecular Cloning. A
Laboratory Manual. Cold Spring Harbor Laboratory, Cold
Sprinq Harbor (1982) and, w:ith regard to the work on
yeasts, e~pecially on Rodri~lez et al.: Reco~binant DN~
Techniques. Addison Wesley Publishing Company, London
(1983~. The hosts used for the ~nthe~i~ of FXIII~ were
generally accessible laboratory strain~ of baker'~ y~ast
Saccharomyces cerevisiae which have one or more defects
; in bio~ynthetic enzymec. The~e defects are complemanted
: by the corresponding functioning genes on the vector~ in
each case. The yeast strains were transformed by the LiCl
method as has been optimized for the fission yeast
(Broker, ~., Biotechniques 5, 516-518 [~987]), with the
modification that the heat shock was carried out at 42C,
not at 46C. Single clones can be selected on YNB minimal
medi~m three to four days after the transformation with
~ plasmid DNA. ~he culturing of the tran~for~ant~ in liquid
- 20 culture to obtain FXlIIa was carried out as follows:
~ 50 ml of YNB medium in a 250 ~1 Erlenmeyer ~lask with
.~ baffles on the side were inoculated with a ~ingle colony
and shaken at 30C for two days. When a yeast ~trai~
whose totality of genstic defec~ was not complemented by
the vector was used, 0.02 0.04 mg/l of the appropriate
amino acid or of the base wa~ added to the medium. 10 ml
of ~uch a preculture were u~ed to inoculate 100 ml of
. complex YPD medium. The 108s of plasmid under the~e non-
~elective conditions varied with the plasmid and yeast
strain used. Cultures in which FXIIIa synthesi~ i8 under
.~ the control of the Gall or GaluAs /Cycl hybrid promoter
which can be regulated by ~alactose were mixed with 2%
galacto e 24 hour3 after the inoculation, in order to
induce the Gal pro~oterO
; 35 Baker's~ yea~t is able to grow on medium containing
: ~alacto~e as the ~ole carbon ~ource. Galactose is trans-
ported via a specific ~alactose permease into ths cell
~,. '''
:

203181~
-- 6 ~
and finally enters glycolysi~ as glucose l-pho~phate. The
following enzymes are involved in thi~: Galac~oki~ase
(Gall), D-Galactose-l-phoRpha~te uridyl~ran~ferase (Gal7)
and uridine-diphosphogIucos0 4-eRimerase ~allO~. The
genes of these emz~mes are clssely ad~acent and sub~act
to coordinated regulation. When the carbon source i8
changed from glycerol or glucose to galactoBe~ tr~n-
~cription of the~e genes ig enhanced 1000-~old. In the
absence of galactose, Gall, Gal7 and GallO are repre~sed
by the nega~ive regulator protein which i8 encoded b~ the
Gal80 gene. A po~itive regulator protein which is sncoded
by the Gal4 gene i~ required for the expre~sion o~ Gall,
Gal7 and GallO. There i~ con titutive synthesiR of amall
amount~ of Gal80 and Gal4 protein~. The Gal80 protein
binds to Gal4 protein and, in this way, inhibits
activation of the genes by the Gal4 protein. ~n inducer
(galactose or a derivative of this sugar~ presumably
binds to a site on Gal80 80 that the affinity of the
Gal80 protein $o the Gal4 protein i~ reduced and Gal4
becomes free. Gal4 now pre~umably binds with it~ amino-
terminal end to the 5~ region~ of Gal 1, Gal7 and GallO
and brings about the enhanced transcription of the gene~.
These distal DNA regula~ory elements of yea~t genes are
called upstream activating sequences (UASs).
xample 1: Synthesis of the plasmid pMB307
The ~tarting material i~ pFXIII 104 (~mann et al.,
~ehring Inst. Mitt. (1988), 82, 35-42; Fig. 1) and
p~MB~yex4; the plasmid pEMB~yax4 i~ ~n E. coli ~huttle
vector. ~he e~Eential relavant properties of tha vsctor
are that they can be selected in E. coli on the b~sis of
the ampicillin-resistance gene. In yeasts, ~alection
~akes place via the Ura3 or Leu2-d gene in leucine-
and/or uracil-auxotrophic ~train~. ~table replication in
yeasts i6 en6ured by the content of 2~ DN~. A particular
: 35 feature of the vector is the Gal~Cyc hybrid promoter.
~enes can be in~erted into the polylinker at the 3' end
of this element so that, in yeast~ with a recombinant
. `; ' . I
:, ` " , '
' ` , ' ' ~ '

203181~)
plasmid of thi~ type, expressi.on of ths forei~n gene i~
under the control of ~he ~al~Cyc promoter which can be
regulated. Efficient transcript:ion termination ie ensured
by an appropriate DNA unit whic:h i8 located at the 3' end
of the polylinker. The construc:tion of pMB307 i~ dep1cted
diagrammatically in Figure 1.
., .
A pla~mid with deletion of the 3~ non-tran~lated re~ion
beyond 120 bp did n~t achieve any ~urther increase in
expression.
10 Example 2: Synthesis of the plasmid pMB307T :
The plasmid pMB307 carries, as ~election marker~, the
:: genes Leu2-d and Ura3, which are usad to complement
: strains which have the genotype leu2 and ura3. Trans
formation with a modified p~B307 whi~h carrie~ the ~rpl
gene has the advantage that the pla~mid 1088 occurring in
~trains with the g~notype trpl in c~mplex media which
contain acid-hydrolyzed protein~ as nitro~en ~ource i8
very low. The amino acid tryptophan is easily decompo~ed
by acid a.nd i6 no longer present in ~uch media ~o that a
complex medium itself xepres~nts ~ selectiv~ m~dium with
respect to the Trpl marker.
The vector p~B307 was linearized with ~t~ nd the
StuI/EcoRI DNA fra~ment, which is 830 bp in size and
carries the Trpl gene, from the plasmid pGT2 (D~, S.,
Rellermann, E. and Hollenbsrg, C. J. ~teriol. 153,
1165-1167 ~1984)) was ligated in. The new pla~mid p~307T
i~ now able ~180 to comple~ant trpl str~in~. V~rious
~train~ wer~ tranafor~ed wi h pM~307r, and the ~IIIa
yield wa~ determined~ ~he ~train with the highe~t FXIII~
~ynthe~is rate ~mong the ~ested ~trains w~ 150-2B.
Exam~le 4~ 5ynthesi~ cf the pla~mid pMB330
,.
The FXI~Ia cDNA mentioned in EP 0,236,978 code~ in
position 88 (CTC) for ~he amino acid leucin~ hinose et
,"~ : ~ .. '''' ' '
.
.
:: ,. . .
. . .
;,': :. ~
~: , . .
.
~' ,

2~3~810
al. ~1986), Blochemistry 25, 6900-6906, by ~ontra~t,
found a TTC triplet which code~ for phenylal~nine in this
po~ition. The amino-acid ~equence of FXIIIa, which has
been determined by Takahashi et al. (1986), Proc. Natl.
Acad. Sci. USA 83, 8019-8023 likewise revealed a phenyl-
alanine at position ~8. It is thus possible that the
amino acid leucine deduced in p~iti~n 88, which i~
mentioned in EP 0,236,978, is a relatively rare allele by
comparison with phenylalanine. ~ FXIIXa expre~sion vector
(pMB330) which has exactly the same structure as the
plasmid pNB307 and differs only in that the CTC codon has
been replaced by a TTC codon, ~hat is to ~ay code~ for a
phenylalanine in position 88, wa~ tharefore constructed.
Example 5: Effect of various strains on the FXIIla
synthesis rate with the plasmid pMB307 or
: pMB307T
Plasmid pNB307 en6ures in S. cerevisiae 252 a ~XIIIa
sy~thesis of about 5 mg/l under the optimized culture
conditions. The yield of FXIIIa in the strain HD was
considerably less. This indicates not only tha~ a high
- FXIIIa synthesis r~te depends on the plasmid and medium
but also that cellular factors are also able t~ influence
the yield. 5everal strains were therefore separately
: transformed with the vector pMB307 and analyzed for their
capacity to Mynthesize PXIIIa in shake cultures. The
: result i~ summarized in Tab. l. It emerged that it i~
possible to achiev0 a wide variation in F~IIIa yields
with the individual strains. It w~s poasible to ~chieve
high FXIIIa ~ynthesis only in strains which reach ~ high
~ell density and in which pla~mld 10~8 i~ low. On the
other hand, a strain which grows well ~nd h~3 ~ low
plasmid 108s does no~ necessarily ensura a ~a~isfactory
yield of F;KIIIa. A~toniRhingly, the capacity do~8 not
correla~e with few auxotropic marker~ either; this is
becaus~ even stxains with three or aven five defects in
bios~nthetic enzymes achieve cDnsiderable yields of
5-7 mg/l FXIIIa. ~oteworthy amon~ ~he tested ~trains are
,~ . . . .
~:~ . ' . : . .

2~31810
g
the strains AH22 and C13A~YS86 with yields above 10 mg/l
FXIIIa. The plasmid pM~307 carries, as selection marker~,
the genes Leu2-d and Ura3, which are used to complament
strains which have the genotype leu2 and ura3. Tran~-
formation with a modified pMB307 which carrie~ the Trplgene has the advantage ~hat the plasmid 108~ occurring in
s$rains with the genotype trpl in complex media which
contain acid-hydrolyzed proteins as ni~rogen BOurCe ia
: very low. The amino acid tryptophan i8 ea~ily decompo~ed
by acid and is no longer present in euch media ~o thst a
; complex medium it~elf repre~ents a selecti~e medium with
re~pect to the Trpl marker.
The vector pMB307 was linearized with BstEII, and th~
StuI/EcoRI DNA fragment, which is 830 bp in ~ize and
caxries the Trpl gene, from the plasmid pGL2 (DasO S.,
Kellermann, E. and ~ollenberg, C. J. Bacteriol. 158,
1165-1167 tl984)) was ligated in. The new plasmid pMB307T
is now able also to complement trpl ~rain~. Various
strains were transformed with pMB307T, an~ the FXIIIa
yield was determined. The strain with the hishest FXlIIa
synthesi~ rate among the tested strains was 150-2B, with
8 mgtl PXIIIa.
.
:: Example_6: Effect of the medium on the F~IIIa yield in
pMB30~ tra~6formant~
.~
Starting from the yields which were achieved
using the plasmid pMB307 in shake culture~ in cu~toma~y
media, attempts were made to increase tha synthesis rate
by altering the componont~ o~ the media. The tran-
scrip~ion of the PXII~a-~pecific cD~A in yeast cells
which carry the plasmid p~B307 i9 regulated by the carbon
seurce. No P'XIIIa i~ produced in media which con~ain only
gluco~e. ~ests were also carried out to find whether the
timing of indu~tion of FX~IIa-~pecific ~ran~cription has
an effect on the FXIlIa yield and whether the ener~y
source glucose can be replaced during the gxowth phase by
other carbon asurces without reducing ths yields
.
, . .
' ' .:
.': ' ~ ' ' .
~' .. .

203181~
of FXIIIa.
Wh~n the glucose in the ~PD medium i8 replaced by maltose
or glycerol, and the rultures are fed with 2~ galacto~e
after 24 h, once again the yields are about 2.5 to
3 mg/l. ~y contrast, when glucose in the medium is
:. replaced by galactose from the ~tar~, ~he yield of F~IIIa
is only about 1 mg/l. This relativaly low yield 18 not
: attributable to reduced growth, because the cell number is
about SxlO~/ml which iB exactly a~ hlgh as in culture~
which contained only glucose or were f ed with galactose
. after 24 h. Presumably FXIIIa syn~he~is has an adverse
:. effect on cell metaboli~m ev n during the growth pha~e
and, in this way, Lmpairs FXIIIa ~ynthe6is during the
idiophase. This observat.ion is ~upported by the fac~ that
the yield of FXIIIa likewise does not exceed 1 mg/l in
: shake cultures in which FXIIIa synthesis is under the
- control of the strong but constitutive ADC promoter.
The yield of FXIIIa in yeasts can be increased to 4 mg/l
by not only inducing FXIIIa ~ynth~sis by adding galacto~e
after 24 h, when glucose is no longer present in the
medium, bu~ also adding ~alactose once again, after a
further 24 h and 48 h, in a final concentration of 2% in
:~ each case. When, at the ~tart of the fermentation, the
complex medium co~tains not only glucose but also galac-
tose in addition, and when feeding with galacto~e is
- carried out each day, the production rate even increas2s
above 5 mg/l~ This supply of the YPD medium with glucose
and galactose i callad YPDG medium hereina~ter. It
: appear~ that FXIIIa synthesis i~ not induced ~y galactose
:~ 30 as long as glucose is pre~ent in the medium. On ~he other
handl under these conditions, the metabolic ~ha~ge-over
after cons~ption of the gluco~e can take place imme
diately, and in the late qrowth phase galactose actq both
as energy ~ource and as inducer. Thu~, it was possible
with a suitable composition of the medium for the yield
of FXIIIa to be approximately doubled by compari~on with
~he cu~tomary standard m~dium.
: .
.. . .
:;' '
~; .

2~3~810
.. 11 --
Exdmple ?- Whey and whey hydrolyzate as ~ource of galac-
tose
~:'
Owing to the vector~ pMB307 snd pMB330, FXIIIa synthe~isi6 strictly repres~ed by glucose in the medium and i~
S induced by galactose. It i~ evident that as long as
glucose i3 present in the medium induction i8 prevented
even in the pre~2nce of galacto6e. Since galacto~ is a
c08tly sugar, attemp~ were made to bring about induction
not by pure galactose but by a reasonably priced medium
which contain~ galac~o~e among~t other thin~. Hydrolyzed
whey powder from Molkerei-Zentrale Wes~falsn ~ippe eG
(Munster) was te~ted for this purpo~e. Thi~ whey powder
contains, apart from protein, fat and mineral~, about 18
glucose, 13% galactose and about 23% lactose too.
20 g of hydroly~ed whey powder were stirred in 100 ml of
water, heated to 60C and thus dissolved. ~his prepara-
tion w~s centrifuged at 10,000 g for 30 minute~ and then
the supernatant was filtered ~terile. Thi~ solution was
dilu~ed either 1:1 wi~h sterile water (A) or 1:1 with
concentrated YPD (B~. The FXIIIa yield with ~. eerevisiae
C13A~YS86 tpMB307 or pMB3303 was only about 5 mg/l ~n
medium A. By contrast, up to more than 100 mg/l F~IIIa
was detected in medium B. I~ was thu~ po~ible to 8how
that whey powder, vf which an exce6s is produced in
dai~ying and which i8 thus very r~a~onably priced~ can be
employed, ater h~drolysi~ of the l~ctose content to
glucose and g~lactose~ as a suita~le ~ubstance for the
recomb~nant ~ynthe~i~ of FXlIIa. In fdCt, ~ubstances
which have not yet been identified result in n con-
siderably higher FXIIIa synthesis compared with culture~which have been i~duced with pure galacto~e. It wa~ al30
pos~ible to achiev~ the high FXIIIa yleld~ ~hen ~ par-
tially dsmineralized condensed cheese whey from De Melk-
industrie Veghel ~BA Veghel~ NL) wa~ employed. Another
sui~able source of ~alactose a~ an alternative ifi whey
powder which, untreated, contains lacto~Q but no galac~
tose. Thi~ lacto~e present in whey powder was hydrolyzed,
".. ~ . . . . . .
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2~'31~10
- 12 -
af~er the pswd~r had been suspRnded in YPD, to glucose
and aalactose with ~-Galacto3idase from E. coli. A
pr~paration of this type also brought about high F~IIIa
synthesis in yeasts. It was even possible to add ~-
Galactosidase from E. coli o:r Kluyveromyces lactis (infree form or immobilized) to 1he ye~st culture which had
been supplemented with whey powder uo that galacto~e wa~
liberated by cleavage only du:ring the farmentation.
Also suitable for ~XIIIa production in place of whey
hydrolysa~e a~ source of alacto~e is lackose hydroly-
s~te. Commercially available lactose hydrolysate (for
example Biolac GmbH, D-3221 Harbernsen or IMA GmbH,
D-6078 ZeppelinheLm) have a total sugar content of about
50%, with the glucose and galacto3e proportion being
about lsl and, besides the monosaccharide~, uncleaved
lactose also being pre~ent in concentrations of 5-15%.
Such lactose hydroly~ates can be sterilized by auto-
claving without the foxmation of caramelization products
which have an adverse effect on the fermentation of
recombinant yeasts. It has ben found that the gluco~e
present in whey hydrolysates and lactose hydroly5ates
- does not impair in any way the induction o$ FXIIIa
synthesis and the production of FXIIIa by S. cerevisiae
~pMB307~ or S. cere~isiae ~pMB330~. Thi3 wa~ ~n u~expec-
ted finding because gluco e i8 described in the litera-
ture as an inhibitox of the induction of the galacto~e
operon. Furthermore, spray-dried lactosa hy~rolysate can
also be employed, in place of commercial lacto~e hydro-
lysate ~olution~, after it has been ~terilized by
suitable method~, for the fermentation. The high yields
: of FXIIIa described here were achieved with tr~nsfor~ants
which contained either the plasmid pMB307 or p~330, and
thus it can be as3umed khat the hi~h ~ynthesi~ rate~ do
:~ not dapend on particular alleles. It may thus be expected
that a high yield is ensured with this optimized produc-
tion proress even with amino-acid replacements other than
leucine 88 by phenylalanine 88,
:,
` ;' '
?

2031810
- 13 -
FXIIIa concentrations 2 500 mg/l were achleved w~th the
abovementioned medium and ~o-called plasmids pMB307 or
pMB330 on conversion on the l()O-SOO 1 fermen~er scale.
The purified FXIIIa was identical according to all te~ted
criteria with FXIIIa from placentae.
. ,~, ,~ . . , .: ,

~031810
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203181~
16
Fi~ure legend:
Construction of pMB307
The FXIIIa-specific EcoRI/HindIII cDNA fragment was
ligated into the polylinker of pEMBLye~4. Compared with
S the FXIII~ cDNA already described (Amann et al., loc.
cit.) the internal EcoRI Bi~e and ~he 5hine-Dalgarno~like
sequence have been mu ated w:Lthout sltering the amlno-
acid 6equence. These features are repre~ented by ~quare
brackets.
DNA Rep. ~,eans filling in of protruding end~, Lig. means
ligation of the resulting con~truct.
pMB330 differs from pMB307 only by Phe88 ~TTC) in place
of Leu88 (CTC) within the FXIIIa ~equence.
: ' `
:, ;
,
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:.
-~

Representative Drawing

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Administrative Status

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Event History

Description Date
Inactive: IPC from MCD 2006-03-11
Inactive: IPC from MCD 2006-03-11
Time Limit for Reversal Expired 1993-06-07
Application Not Reinstated by Deadline 1993-06-07
Deemed Abandoned - Failure to Respond to Maintenance Fee Notice 1992-12-07
Inactive: Adhoc Request Documented 1992-12-07
Application Published (Open to Public Inspection) 1991-06-09

Abandonment History

Abandonment Date Reason Reinstatement Date
1992-12-07
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
BEHRINGWERKE AKTIENGESELLSCHAFT
Past Owners on Record
MATHIAS GROTE
MICHAEL BROKER
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Abstract 1991-06-09 1 24
Drawings 1991-06-09 1 18
Cover Page 1991-06-09 1 19
Claims 1991-06-09 2 48
Descriptions 1991-06-09 16 689