CA1182409A - Plasmids constructed by gene manipulation, strains of escherichia coli carrying them, and process of tryptophan production using said strains - Google Patents

Plasmids constructed by gene manipulation, strains of escherichia coli carrying them, and process of tryptophan production using said strains

Info

Publication number
CA1182409A
CA1182409A CA000386858A CA386858A CA1182409A CA 1182409 A CA1182409 A CA 1182409A CA 000386858 A CA000386858 A CA 000386858A CA 386858 A CA386858 A CA 386858A CA 1182409 A CA1182409 A CA 1182409A
Authority
CA
Canada
Prior art keywords
tryptophan
strain
escherichia coli
strains
trp
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
CA000386858A
Other languages
French (fr)
Inventor
Tadayuki Imanaka
Shuichi Aiba
Hiroshi Tsunekawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanraku Ocean Co Ltd
Original Assignee
Sanraku Ocean Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanraku Ocean Co Ltd filed Critical Sanraku Ocean Co Ltd
Application granted granted Critical
Publication of CA1182409A publication Critical patent/CA1182409A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • C12N15/11DNA or RNA fragments; Modified forms thereof; Non-coding nucleic acids having a biological activity
    • C12N15/52Genes encoding for enzymes or proenzymes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • C12N15/63Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
    • C12N15/70Vectors or expression systems specially adapted for E. coli
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00Preparation of nitrogen-containing organic compounds
    • C12P13/04Alpha- or beta- amino acids
    • C12P13/22Tryptophan; Tyrosine; Phenylalanine; 3,4-Dihydroxyphenylalanine
    • C12P13/227Tryptophan

Landscapes

  • Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Biomedical Technology (AREA)
  • Biotechnology (AREA)
  • General Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Plant Pathology (AREA)
  • Biophysics (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Saccharide Compounds (AREA)

Abstract

Abstract of the Disclosure A recombinant plasmid having introduced thereinto a tryptophan operon which encodes an anthranilate synthase desensitized to feedback inhibition by tryptophan; a strain of Escherichia coli carrying said recombinant plasmid;
and a process for producing tryptophan using said strain of Escherichia coli.

Description

~ his i~ve~tion relatec; t;o a .recombinax:lt pla~d having a tryptophan ope:ron which e~codes anthranilate s;~thase ~Sase3 dese~sitized -to f eedback ir~hibition b~
tr~ptvphan9 a~d to a strain o~ ch~ichia coli b~vir:~g high ~r~ptoph~producing abilit,y as a re~ult o:E intro-duct~on thereanto of a ~corlb:inant plasmid obtai~d by gene marlipulationO It also pertai~s to a p~oc~8s for produci~g tr~p~op~2~ ef~ic~tly Wi~ a short p0r~0d o`
time by cultivati~; the g~raill of ~ coli i~ a 10 ~lutrienl; m~dium and reco~eri~s t~h~n :Erom ~h~ culture bI~ot~,.
ha~ be~rl we~l ~ow~ that ~lu~ c acid, l~r~ine9 etc.. ar~ produ~ed by :EerDle~ta~io~ ~echni~ues u~ing micro-orga~i~ms, i~ particular b~ u~ing artificiall~ mutatcd 15 ~licroo:~;a~m st:r~ins o~ high prQduct~ it;y" Co~lrentional ~Eerme~tation methods, how~ver~ do ~ot g:ive rise to high productivi~y ~ID f ~ a~ t~ ophan, a }dnà o~ ~no acid i9 concarrled, ~o f ermen~tio~ m~3thod that satis~
eco~omic f oasibili~ ha~ yet been esta~lish~d o~ ael ~n-2Q du~trial basia. Orl the other harld9 the rec~a~ ~dvance~o~ genetic en~ eeri~g ha~e e~abled us~ ubsta~ces ~uch a~ i~suli~ or growth 3:Lox~aor~e to be ~od~ced b~
ïerme~tat 2~ chniqu~s usin~; s~rain~ o i~to ~Jhich ~enes of hi~;her ~rLLmals or pl8~ h~e be~r 25 i~troduc ed .
W~ e ~ow suce.eeded i~ produci~g tr,~ypto~?haz:
ly b~ ~a~s~ ; a ~t~ o~
with a recom~ pla~mid co~structed b~y gen~ ipula~io~

that imparts tryptophan-s~nthesizi~g activity to said strai~ and by cultivati~g the t;rans~ormed strain.
Thus, one characteristic of this inventioD is to provide a recombinant plasmLd having a tryptophan operon of ~ coli which encodes ASase desen~
sitized to tryptophan inhibition, said plasmid being able to replicate in a strain of Es~herichie coli~
Another feature of the in~ention pertains -to a strain of ~ co~i transformed with said plasmid, said ~ coli strain havi~g ASase desensitized to feedback inhibitlon by try~topha~ and being a de~icie~t m~tant of tr~ptophan repressor a~d tr~ptophanase.
S~ill a~o~her ~eature of the inve~tion is to provide a process for producing tr~ptophan, which comprises cultivating the above trans~ormed ~scherichia coli strai~
in a nutrient medi~ particularly in a ~utrient medium containing anthra~ilic acid supp~emented, if desired3 ~ith a tetracycline~type antibiotic~ and separating and recovering L-tI~tophan from the cultur~ broth in a man~er l~own ~ se~.
The present i~verltiorl is described in detail here-inb~l ow .
The recombinan t p`lasmid in this i~vention ca~ be obtained in t;he f ollowin~; manner.
~'he Iirst enzyme in the tr~-ptophan synthesizin~;
system in a microorganism is ~Sase. .A6ase i5 USllally subJect to :Eeedback inhibition by t~yptopha~. Some of mioroorganis~ strains wbich are r esistan-t to 5-~ethyl~

~ 3 --DLrtryptophan~ an analog of t~tophan, have ASase that is insensitive to feedback in~.bi-tlon by t~yptophan, Accordingly, if such strains ~ cultivated, tryptopha~
can be produced in lc~rge quanti.~ies.
~hus, Escheric ia co]i W~llO ~ (pSC101-tr~), i.e. an Escherichia coli strain carryin~ a plasmid, havi~g a tryptophan operon introduced thereinto~ is physically or chemica~ly mutated by a k~own muta-ting means such as W irradia~ion or treatment with N-methyl ~'-ni~ro-N-nitrosoguanidine, ethyl methanesulfonate, etc, ~rom the muta~ts obtained$ those which are resistant to 5-methyl-nL-tryptophan and hc1~e ASase insensiti.ve to tryptophan inhibition are selectedO Plasmids extracted from these selected strai~s (e.g~pS~l0~_-trp~I15) haviog a tryptophs~
~peron xesistan's to feedbac'~ inhibition by ~ryptophan~
Recombi~ant plasmids having a -tryptophan operon as used in this in~ention, such as p~C101-trp~ can be ob~
tained by recombining a ~no~m tryptophan operon with a vector such as a plasmid. for Escherichia coli.by the method 2t) described in Gene, VolO 1, pages 141 to 152 ~1977~ or by the modi~ied methodsO
It has been asce.rtained -that the :Eollowing strai~s can be used as hos-ts into which the recombinant plasmid pro~r-lded by -this inve~tion can be in-troduced by 25 ~transI ormationO
~scherichia coli W3110 ~ (AEl for short), _~__ __ ~scherichia coli W3110 ~ E~_m~Z ~Xam for ~____ _ short ~, ;Esche:r hi coli W3110 ~ ~ ~L (Tna f OI` short ) O
Escherlc'[li~ coli (E~ocOli) iS a stra~n which is non-ly~ogenic for lambda (';. ) and does ~ot have a 5 fert~lity factor F ~F ). It is ~ mut~nt ~ATCC 27325 derived :Fr~m a parent stxai~1 ~E. coli Kl29 which is lysoge~ic ~o~ lsmbds and has a fertility factor F~ rl:hus, accordin~ to this invention, all E. coli str~ins derived from E,. coli K12 are eligible as hosts of the plasmid of the m vent ion . When it is desired to produce tryptophan, the use of an Eo coli strain which has the followi~g three p.roperties, i.e.~ tryptophan operon deletion mutation ~trpA:E;l), ~r~ptophan repressor defici~eIIt mut~tioII (trpR) __ _ ar~d tr~ptophanase deficient mutation ~), thQt iS9 15 ~ coll W3110 ~ tnaA is most preferred.
~ he properties which the host E~ coli cells should ha~e are described below~
~~
'rhe tryptophan operon of ~O coli linl~s a tonB
gene on -the chromo~ome~ Since tonB is necessary for the adsorption o~ a phage Tl to Eo coli., m~lta5ion of tonB
results in a ~allure o~ phage '~1 adsorptionO Accordingly, the O coli becomes resistant to 5he phage Tl by the mutation o~ ton:B, ~en double mutants~ tryptophan requirement and re~istance to pha~e Tl ~Tr.p ~ Tlr~ are obtained by ultra violet irradiation~ it is seen that in mos-t of these mutants, DN~ segments extendlng from the tonB to the t ~

tryptophan operon are par-tly o:r to-tally de]eted from the chromosome. The mutagenic trea~men-t and the method o~
deter~ination in~olved iD the :foregoing are described in detail, for example~ in ~enletics, VolO 49~ p~ge~
2~7-278 (1964)~
trpRam27~ trpR (tr~tophan repressor de~icient ~utation) Tryptophan repressor mu-t~nts are preliminarily selected for their resistance to -tryp-tophan analogs (such as 5-~ethyl-DL-tryptophan, or 6-methyl-DL-tryptophan).
q`he analog-resistant strains may possibly include (13 those which ~re derepressed mutants9 (2) those which are ~sensitive to feedback inhibition by tryptophan 7 and (3) those which cannot take the analogs into their cells because of changes in membrane structureO
Thus7 i~ tr~yptophan s~nthase is constitutively synthesiæed in the analog-resi~tant strains when culti-v~ted in a medium containing tryptophan (with wild strains tryptopha~ synthase is scarcely syrlthesized under these conditions because of repression), these str~ins are determined as derepressed mutantsO As -to whether the derepression is due to the repressor mut~tion or the operator mutation~ the analog-resistant strain is sub-jected to transduction by a ph~ge PIKC (a generalized transducing phage of ~ coli) to examine whether the genotype of this p~rticular analog-resistant mutation is linked to the thr(threonine-auxotrophic) gene or to ~(-tr~ptophsn-au~otrophic) geneO lf it is linked with thr gene, it can be ascertained that repres~or mutation has taken placeO Such a strai:n can be used in this in-ve~tion~
Incidentally~ ~27 is tryptophan repressor 5 nonsense mut~tion, and ~ is tryptophan repressor missense mutation. ~or details~ reference m~y be h~d9 ~or example, to J. Mol~ Biol., Vol 44, page~ 185-193 (1969), and Genetics, Vol. 52, pages 130~--1316 (1965)o A wild type of Eo coli strain c~n grow b~
uti~ izing tryptophan as ~ sole c~rbon source becaus~ of tryptophanase ~ctivity (tryptoph~n ~ indole+ pyruvic ~cid + NH3), whereas a tryptophan~e-deficient mut~nt of E.
coli c~nnot~ By utilizing this physiclo~ic~l tr~it, the ~5 tryptophanase~de~icient mutant c~n be separated. For ex~mple, a _~ coli 6trai~ is sub~ected to mu-ta~enic treat-m~ts eith~r ~y ultraviolet irr~diatio~ N-methyl-N'-nitro-N~nitrosoguanidine (NTG) or ethyl msth~esulfon~te (E~lS~ to form colo~ies on a minim~l ~gar mediwm cont~i~ing 20 gluoose as a carbon ~ource~ The colo~ies were tr~nsferred GlltQ 8 minimal ~gE~r medium contaill~ng tryptophan as a sole carbon ~ource ~ ~hus ,, those str~ which ~srow when th~
carbon source is glucose but c~nnot grow on tr~ptophaD
~re s~lected.. The tr~ptophan~se aotivity is determined 25 b;y ~dding ~r~ indol~2 reagent to the culture broth obtained by cultiv~ting the sforesaid strain in I.~brothO When red color specl;E ic to indole is not Iormed upon the ~3adition ~a color reaction on indole), the tryptoph~n~s~

7 _ is regarded as deficient.
In this regard~ reference may be had to, for example~ J. Bacteriologyt Vol~ &99 pages 680-686 (1965).
E~ coli W3110 ~ tnaA strain can be obtained by using the aforesaid methods i~ combination.
Specifically, this can be accomplished by the following procedureO
(1) Subject E. eoli W3110 ~ strain ~cystein-auxotroph) to -trpR mutation, (2) ~ransduce a ~ strairl with the PIKC
lysate prep~red on E. coli W3110 ~ strain to obtain W3110 ~ strain9 and
(3) Subjsct the resultin~ strain in (2) to t _ mutation.
The tryptophan synth~se (TSase) and anthranilate synthasc (A~ase) activities of a strain obt~ined by trans-~ormation with the plasmid pro-vided by this i~vention~
such as pSC101-trpdI5 or pSC101-trp-I15 are shown in ~able 1~ inhibition of ASa~e activity b~ tryptophan, in ~able 2; a~d the productivi-ty ot tryptcphan, in Table 30 The characteristics of -the Eo coli strains in this in~
vention will be urther descr1bed~

~ o o o o o o d~ .~
.~ ~3 ~
~~a ~
cq ~ ~ ~ ~ C ~D
a)E~ ,~ ~ ~ ~ ~JO
~ ~l ~ ~ ~
~ --r~3 r~ ~ tU ~ O
~; I r~ r~
----~
tn 0a~ ~C~co~ ~ ~
CQ ~ o ~ o ~ ~ c ~q 0 ~ ~ 0 ~ o ~
tQ r~ ~ O O
.~ ~l ~
~ --~
^
~1 U~ ~1 U~ r~
H H H H H H
E~
.~1~ ~ .
I I ~ rJ r~ I
O O O O ~ C) r-~l r~l r~ ~-~ r~
V C~ C~ ~ V
~ ~ ~ c3 u~ CQ
E~
.
a~
h Ul ~ .
____~

_ 9 _ The unit of the activities given in Table 1 is U~mg of pro-t~n~ The activities were measured usin~ 8 cell-disrupted solution (by sorlication; crude enzyme solution) obt~ined in a me~ium A to be described here-5 inbelow. ASase activity was measured in the absence (~Trp) and/or presence (+Trp)(().2mM) o:E -tryptop~an.
The TSase and ASase activitieæ are higher with Ram or Tna StrainB which are tryp-tophan repressor-, flsa . ~
de~icient than A:El straill. A~e is not inhibi-ted by 10 tryptophan in either ca~e.

_ 10 --able 2. Inhibition oî ASa~e acti~ity by tryptophan _ ~ . .___ Trp 50/0 in-Stra ill Trp ~mM ) ~ /0 ) hib it ion (mM ) ____~ ~
AEl (pSClOl_trp I5) 1~1 100 13.1 ___ __ In Ta~le 2, Trp 50% inhibition der~otes the conc~ntrat~o~ o~ trypt~?hal~ ~t which tryptopha~ ix~hibit~
5 by 5G~/o the ASass aetivity in the absence of tryptophar~c With regard to the inhibition oî A~3a~ actilrity by tryptopharl, no significant diî:~erence i~ see~ betwesn pSC101-trp - I5 ~nd pSC101- trp Il50 This suggests that the pl~smid pro~ d by the pre~;ent ir~veirlt iorl are not 10 alwa~s specif ic O
The 1~, col:~ cells trarlsform~d with the pla3mid i~ this i~vention, for exa~nple~ ~na(p~l(:l-trp-I15) str~in e~itiv~ to feed~ac:k inhibitiori by ~ryp~ophan t tryptophan repr~ssor is m~l~unction~g9 ar~d tr;srpt~ha~se 15 activitie~ are mi~sing~ Only tho~ :E. coli strains which ~eet the~e r~qu;~ments ac¢umulate t~;yptQphan oGnsider-a~bl;yO ~he ob jective OI high tryptophan production c~nnot be achieved, if ~ny one of these reguire~ents is lacking~
This is clearly seen from Table 3 below.
T~ble 3: Productivity of tryptophan (48_hour cultivation) ~ _ __ _ Repres- In- Trypto- Tryptophar ~traIn plasmid sio~ hibi-tion pha~ase (~g/m~) _ ___ ___ __ __ AEl pSC101-trp + + + 7 pSC101-trp I15 ~ _ + 11 Ram p5C101-trp ~ ~ 7 pSC101-trpoI15 _ _ ~ 7o Tha pSC101-trp _ + _ pSC101-trp,I15 _ _ _ 360 ~ __ __ __ ~
For accu~ulation of tryptophan i~ high con-ce~tratio~s~ both the removal of repression by tryptophan ~nd resistanc~ to feedback inhibition by tryptophan are es~enti~ nd the deficiency of tryptoph~nase is also neces~aryO The productivity of Tn~(pSClOl~trp~I15) is hi~her than that shown by a chro~o30~al dou~le mutant (repre~sio~ , inhi~ltion ) of _, coli [iOeO, 183 ~g/m~:
J. ~`er~ent. Technol., vol~ 43, page~ 302-306 (1965~].
T~is is believed to reflect ~he gene dosage effect of the plasmid on th~ amount of the ~in~l product~
E. coli W3110 ~ tnaA. ~pSC101-trp~
I15) mention~d above was deposited on October 28~ 19~0 i~
American ~yp~ Culture Collection (a d~posit number: ATCC
3~74~)~
~he medium ~or cultivating microorganisms i~
this invention may be ~ny natural or synthetic nutrient _ 12 -medium containing carbon sources, nitrogen sources, in-organic materials, etcO which may, as reguired, by supplemented with the drugs used in the preparation of the microorga~isms u~ed, and/or anthranilic acid. The carbon and nitrogen sources used in -the cultur~ mediu~
may ~e a~y kinds which the microorganisms can utilize.
~he carbon sources are, for examplel carbohydrate~ such as gluco~e, glycerol9 fructose, sucrose~ maltose, mannose, starch, starch hydrolyzate and molasses~ ~xamples of the nitrogen sources include ammonia, inorganic and organic ammo~ium salts such 85 ammonium chloride, ammonium sulfate, ammonium carbonate, ammonium phosphate a~d a~o~ium acetate, and natural o~ganic nitrogen sources such as meat extract, yeast extract, corn steep liguor7 casein hydrolyzateS defatted soybaan residue or the digested product thereof. Man~ of natural organic nitrogen sources can serve both as the nitrogen and carbon sources~
Examples o~ the inorganic material~ include ~ 6r}~ potassium monohydrogen phospha-te (K ~P0~
---c potassium dih~dro~en phosphate (KH ~04~, magnesium ~ul~ate, sodium chloride, ferrous sulfate, calcium chloride, zinc ¢hloride, copper sulfate, manganese chloride, cobalt chloride, ammonium ~olybdate, and boric acid~
Whe~ the created microorganism has resista~ce to an antibiotic may be added to the culture m~dium to prevent antibiotic cvntamina-tion ~he addition of anthranilic acid, a precursor of tryptophan, is also useful for enhancement of tryptophan production.
~ - The cultivation is c~rri~d out;under aerobic conditions by shaking or submerg~d culture under aeration and stirxing. The culti~ation temperature is usu~lly 20 to 50C, preferably 35 to 45G. Desirably, the pH
of the culture medium is maint~ined nearly neutral, iOe~
about 6 to 7. 87 during the cultivation~ l'he cultivation period is usually ~rom 1 to 3 days~
'~ryptophan accumulated in the cul-ture mediu~
may be separated and recovered by conventional methods, ~or example, by using an ion exchange resin~
~ he following Examples illustrate the prese~t invention without any intention of limiting the invention thereby. Before proceeding to these Examples, the con-struction of pSClOl~trp is described.
~e~
pSC101 (tetracycli~e resisbant, ~cr a~d copy number per chrsmoso~e7 5-10) was used as a vector7 a~d a specialized ~ran~ducing phage ~ ~ wa~ used as do~or o~ tr~ptoph~n operon in E. coli~
(1) Treatment with res-triction endonuclease, EcoRI
-,~t~ Q=~ D~A (about 0.1 ~g) and pSC101 plas~id D~ (about lo9 ~g~ were digested ~or 1 hour at 37C ln the following re~ction soluti~n~ The~, the mixtur~
wa~ heat~d at 65~C for 5 minutes to inac-ti~te EcoRI.
~ coRI reaction solution ~50 ~ in to~al):-Tris-HCl (pH 7~4~ 90 mM
MgC12 10 m~-l DNA 2 ~g EcoRI 2 units EcoRI is commercially ~vail~ble f~m Miles ~abor~tories Inc.~ ~ethesda R~s~arch I,~boratories Inc.
etc~
~2) Treatment with T4-DN~ ligase The T4-D~A ligase trea-tment was carrie~ out at
4~C for 18 hours usi.ng a }igase solutio~ o~tained by adding the ~ollowing reagent~ to the a~or~said EcoRI
reaction solution, and adjusting the amount o~ the mixture to 100 ~ h~ ligase is also availa~le.
~E~
50 mM MgC12 10 100 mM d}thio~ry~hritol 10 11 0~5 ~M adeno$ine tri~
phosph~te (ATP) 10 Watcr ~ ~
T~ A ligase 0~2 u~it ~3) ~ran3~0rmatio~ of E~ coli ~- coli a60~ rk ~ mk 1 Trp strain waa culti-~ted at 37C in 20 ml of ~roth (~or co~positions.
per liter~pepto~e 10 g, yeast extr~c~ 5 g~ NaCl 5 ~
pE 7) ~o an op~ical de~slty ~OD660~ of 0047 The cells were collected, washed with 20 ml of 100 mM MgCl~, ~uspended in 10 ml of 100 mM C~C12, and allowed to stand i~ an ice bath for 20 minutes~ The cells were re-collected by centri~ugation, and again suspended in 1 ml of 100 mM CaC12. In an ice b~-th, 200 ~L~ of this cell suspension was mixed with 100 u~ of the a~ore~aid T4-D~A
ligas~ reaction solution~ and the mixture was allowed to stand ~or 30 minutes~ ~he mixture was then treated at 4~C for 2 minutes, and again allowed to s-tand in an ice bath for 20 minutes. 2.7 ml o:E the I.-broth was ~dded, and the bacteria were cultiva-ted a-t 37C for 2 hours~ The culture broth was spread on a cult~e medium A of the fol-~0 lowing composition containing 15 g~ agar ana 10 ~gJml o~tetracycl m e (~c), and a trans~ormed str~in ~er and ~rp was selected~
~ith regard to -the aforesaid E. coli C600, the symbol rk denotes the property of the bacterium to di~tîn~
guish its ow~ D~A molecules (the bases on DNA are specifi~
cally m~thyl~ted~ from foreign DNA molecules (which differ from its own DN~ molecules in the site of methylation), restricting the entr~ of foreign D~A. ~he symbol m~ de-notes the property of the bacterium -to modif~ the foreign DNA to innate DNA molecules in the site of methylation.
~husg rk and m~ show tha-t these properties are absent~
Gulture medium A (Vogel and Bonner minimal medium, pH 7~ contain~d per liter.
K~IP04 10 g NaNH~EP0~4~I20 3-5 g r1~S04 ~ 7~2 0 . 2 g Citric acid~H20 2 g Glucose 2,5 g Casamino acids 0~5 g (4) Extraction o.~ p~C101-trp plasmid ~NA
The TcrTrp trans~orman-t was cultivated at 37C
i~ 100 ~1 o~ the I~broth to an optical density (OD660) of 0.8~ The cells were collected, and suspended in 1 ml of Tris~sucrose [Tris-HCl pH 8 (50 ~M)~ sucrose (2~/o wt/vol)].
I~ an ice bath, Oa~ ml of lysozyme (5 mg/~l) was added, and the mixture was allowed to stand for 5 minutes~ Then, 0.4 ml of Na2EDTA (250 mM, pH 3) was added, a~d the mix-ture was allowed to st~nd for 5 minut~s. Further, 0.5 ml of 5M NaCl and 0.2 ml of l~o (w~v) sodium dodecylsulfate ~SD~) were successively added. The mixture was stirred and then allowed to stand over~ight in an ice bath. The mixture wa3 then cen~rifuged at 4C for 30 minutes (30,000x g~. The resulti~g supernatant liguid was ad-justed to a volume of 5 ml using 50 mM Na2EDTA (pH 8~, and 407 g of CsCl and 1~8 mg of ethidium bromide were added to adjust the de~sity of the mixture to 1.57 g~ml. The resulti~g sample was subjected to CsCl-ethidium bromide density gradient centrifugation us~ a~ RP65 rotor (made by Hitachi Works ~tdo) at 38,000 rpm ~or ~0 hours. hfter th~ centrifugation, fractions containing plasmid DNA wer~
collected, and ~thid;L~ bromide was e:~iFacted from them using butanol and dialyzed against T:E buffer ~Tris~HCl 10 mM 7 ~la 2EDqlA O ~ 1 m~l 9 p~ 8 ) .
The -theory o:E the above densi-ty gradient cen-tri~uga-tion is as follows~
Plasmid D~A (covalently closed circular DNA) a~d chxomosomal DNA (li~ear D~A; although they are _ l7 _ circular in the cells, Ihey change to linear in the course of extrac-tion because of their high molecular weight) differ from each other in the form of molecules. Ethidium bro~ide intercalates between bases of DNA to a greater exten-t in -the linear DNA molecules than in the cir-cular. Consequently, a difference in density arises be-tween the plasmid and the chromosomal DNAs. The plasmid DNA is separated by utilizing this density difference.
pSC101-trp extracted by the above method had a molecular weight oE about 16.5 x 106 daltons. It was digested with restriction endonucleaseJ EcoRI and subjected to electrophoresis on an agarose gel.
Two DNA fragments were noted, one corresponding to the fragment ~10.8 x 106 daltons) containing tryptophan operon and the other to the original vector plasmid, pSC101 (5.7 x 10 daltons).
Example 1 A plasmid having a tryptophan operon insensitive to feedback inhibition by tryptophan was separated in the following manner.
~1) Separation of strains resistant to 5-methyl-DL-tryptophan ~5MT) 5M~, an analog of tryptophan, as does tryptophan, represses transcription of a tryptophan operon to a messenger RNA (mRNA) and inhibits the activity of anthranilate synthase (ASase). A wild strain cannot grow in the presence of 5MT because of no production of o~

tryptophan. But if tryptophan operon is derepressed by tryptophan repressor ~utation~ etc. or the activity of ASase is not mhibited as a result of mutation, this str~in synthesizes a minimal amount of tryptophan and can grow (5MTr).
~ . coli W3110 ~ (whole tryptophan operon on chromosome was deleted, and therefore, Trp , design-ated as ~AEl] ) was tra~sformed with DNA of pSC101-trp to obtain a transformant ~1 (pSC101-trp~ whvse phenotype:
(~c~rp~). The AEl(pSC101-trp) s~rain was treated with NTG (200 ~g~m~), and the cells were spread on an agar medium A (medium A added by 15 g~ of ~gar) co~tai~ing 200 ~g/m~- of 5~, and cultivated overnight at 37C~ By this method, ab~ut seventy 5M~r strai~s were separated 15 independently.
(2) Separation of strains resistant to ~eedback inhibition Seventy 5M~r strains were cultivated each at 37C for 16 hours in 100 ~4 of the culture medium A. The cells were collected, washed with 0.~/0 NaCl, and suspended in 5 m~ of 100 ~M tris-I~Cl (pX 7.8)~ The cells were then so~icated by a~ ultrasonic generator (Model 42~0, Kaijo Denki Co., 10 KHz) to disrupt the cells7 ~nd centrifuged at 18~000 rpm for 30 minutes by using a rotor ~Sorval SS~34). '~he ~upern~t~nt liquid was obtained as a crude enzyme solution~
The .ASase ~ctivity of the crude enzyme solution was assayed and the ~ctivity of ~Sase in the presence of 0.2 ~M o~ tryptophan was checked. It was found that the activity of ASase in two strains (I5 and I15) was not inhibited by 0~2 mM of tryphophan and these strai~ had resistance to feedback i~hibi-t ion ~
(3) Praparation o~ a plasmid h~ving a trypto-phan operon desensitiæed to ~eedback inhibition Plasmids pSC101-trp I5 and pSC101-trp I15 wer~
extracted~ respectively by the same method as described iO here maboveO 'rhe pSC101-trp-I5 and pSC101-trp I15 were treated, respect ively with EcoRI 9 a~d ~ubjacted to agarose gel electrophoresisv Two bands corresponding to 10.8x 106 and 5.7x 106 daltons were noted.
It was confirmed ~rom the following fact t~at resistance to the ~eedback inhibition was ascribable to the plasmid mutation. Specifically, AEl strain, ~. coli W3110 ~ ~3~ (tryptophan operon deletion, tryptopha~ xepressor de~icient, ~esi~nated a~ [Ram]), ~ coli W3110 ~ tnaA (tryptophan operon deletion, 20 tryptopha~ repressor deficient~ tryptophansse deficient, desi~ated as ~'~na]) were tra~sformed with the pSC101-trp~I5 or pS&101--trpoI15s respecti~ely. U5ing the trans~ormants carrying pSC101--trp- I5 or pSC101-trp~I15, crude enæyme solutions were prepared a~ described here-inabove, and the activity of ASase was measured. In allcase~ the ~c tivity of ASase was insensitive to trypto-phan Accordi~ly, the resistance to ~eedback inhibition was attributable to the mutation of tryptoph~n opero~

20 ~
of pSC101-trp.I5 or pSC101-trp~Il50 A loop of the Tna(pSClOl-trp~l15) strain obtained by transforming Tna strain wit:h pSC101-trp I15 ~ s in-oculated into L-broth having the following composition (per liter~ and containi~g 20 ~g/m~ o~ tetracycline, and precultivated a-t 37C for 9 to 15 hours. Thenl 0.5 m~ (o~ 5%) of the pre-cul-ture was inoculated in 100 m~ of medium B having the followin~ composition (per liter) in a 500 m~ flask, and cultivated at 37C. The pH of the culture medium was adjusted to 7 with 2N NaOH every 3 to 5 hours. After the cultivation for 48 houxs~ trypto-phan (360 ~g/m~) was assayed by the Xanthydrol ~ethod.
~-b Bacto-tryptone 10 g Yeast ex~ract 5 ~
~aCl 5 g pH 7 Culture medium B
KH ~0~ 3 ~
K ~ 04 7 g NH4C1 3 g M~S0~7H~0 0.2 g pH 7 Glucose 30 g Casamino acids 1 g ~5 ~
The Tna strain (pSC101~-t~I15) was .inoculated in medium B supplemented with an-thra~ilic acid and Casamino acids as shown in the following table, and cultivated at 37 C ~or 48 hours. ~he pH of the culture mediu~ was adJusted to 7 with 2N NaOH. Tryptophan produced is shown in the following ta~le.
When the amount of anthranilic ~ci~ added ini-tially was 500 mg/e, it was consumed completely in about 24 hours. When the amount was 800 mg/~, anthranilic acid was consumed completely in about 48 hours. Whan the con-cen-t~ation of anthra~ilic acid was much higher, it was inhibitory to the bacterial g~owth~ ~he cultivatio~ time reguired was 63 hours when the concen-tration of' anthranilic acid was 1,000 mg~, a~d ~ore than 63 hours if the con-ce~tration was 1~500 mg~ he anthranilic acid consumed was converted almost completely to tryptophan.

_~
Amount o~ tryptophan accumulated (m~e) Anthranilic Cas~mino ___________ acid acids 48 hours 63 hours (~g/~) (%) later l~ter __~
500 0.2 1140 11~5 ~00 0~2 1626 1557 800 o L~ 1 L~07 1404 1000 0.4 1233 L575 1500 0.4 1233 1614 ____ ~

15 ~
Tna~pSC101-trp.I15) strain was precultivated at 37C for 9 to 15 hours in L~broth supplemented wi-th 20 y.gf~ of tetracycline" 100 m~ of the preculture broth was inoculated in a ~ar fermentor (2 ~;.Model MD-250;

- 2~ -arubishi Go., Tokyo) containing 1.5 ~ of a culture ~edium having the ~ollowing composition (per liter), and cultivated at ~7C, The cultu.re medium was stirrsd at 500 rpm, and air was supplied at a rate of 1 v.v~m. ~Le pH of the medium was adjusted to 7 with 1'~% N~-I40H.
A~thranilic acid as a substrate was added at a const~nt rate of 50 ~g/~/hr after 8 h~ur~ from the s-tarting of the cultivationO ~he cultivation was carried out for ~8 hours. ~he amount of tryptophan accumul~ted was 5~6 10 g/.eO
T ~re ~
KH ~O~ 3 ~
K2HPO4 7 g NH4C1 3 g MgSO407H20 0.2 g ~eso4 7H20 o. 01 g Anthranilic acid 005 g Glucose 50 g Casamino acids 10 ~
29 Tetracycline O~Ol g pH 7 One liter of -the resulti~g cul~ure broth was centrifuged, and the supernat~nt liquid obtained was pas~ed throu~h a chromatographic column packed with 900 ~ o~ activated carbon to cause adsorption of trypto-~5 phan. ~he column was washed with water and eluted with
5~/O etha~ol c~olution conta}~ing o.70/o of ammonia to sepa-rate trypt~phan~ ~he eluate was concantrated under reduced pressure to xemove ~mmonia and eth~nol~

The resulting agueous solutio~ Qf -tryptop:han was adjusteà to ~ p:~l of 4~5, and passed through a column (10 x 40 cm) of Dowex 50x8 (Na form) (a tradename for a product of Dow Chemical Co. ~ buîI ered with a t)O lM citrate 5 ~olu~ion ~pH 3.4)~
~ hen, 4.5 ~ of a O~lM citrate bufîer tpH 5.0) was passed through the column, and the colum~ was elut~d with a 50% a9ueous solut io~ of ethanol conta in ing 0O 2~/o ~mmonia to sep~rate tryptophan. ~h~ eluate was concen-~0 trated to dryness under reduced pres~ure to ~ive crudetryptoph~n as a crystalline powder. ~ne crude tryptophan powder was dissolved in a small amount Of 5C% hot ethaDol, decolorized with a small amo~t of activated carbon, and cooled to gi~T~ 3O5 g of tryptophan as white scale-like 15 crystals~
t ~h~ result~ shown i~ thase l~amples demonstrate that tryptophan ca~ be obtained efîiciently within shorter periods o~ time by using Eo coli strains tr~nsIormed with recombina~t plasmids constructed by the gene manuipu~:a~or 2:) techni~ues i~ vitro than by using conve2ltionRl mut~nts o~ ;E. coli. Moreovar, by transformillg E. coli strains with recombinan t plasmids of larg~r copy numbers or by increasirlg their resis-tance to feedb~ck inhibition9 ths praduction of brylptopha~ will be rnors eff icient.

Claims (6)

WHAT WE CLAIM IS:
1. A recombinant plasmid having introduced there-into a tryptophan operon which encodes an anthranilate syn-thase desensitized to feedback inhibition by tryptophan, said plasmid being able to replicate in a strain of Escherichia coli.
2. A strain of Escherichia coli carrying a re-combinant plasmid and being a deficient mutant of tryptophan repressor and tryptophanase, said recombinant plasmid having a tryptophan operon which encodes an an-thranilate synthase desensitized to feedback inhibition by tryptophan.
3. The strain of Escherichia coli of claim 2 which is Escherichia coli W3110 trpAE1 trpR tnaA (pSC101-trp.
I15) (ATCC 31743).
4. A process for producing tryptophan, which com-prises: cultivation in a nutrient medium of a strain of Escherichia coli carrying a recombinant plasmid and be-ing a deficient mutant of tryptophan repressor and tryptophanase, said recombinant plasmid having a trypto-phan operon which encodes an anthranilate synthase de-sensitized to feedback inhibition by tryptophan, and separation and recovery of tryptophan from the culture broth.
5. The process of claim 4 wherein the nutrient medium contains anthranilic acid.
6. The process of claim 4 wherein the nutrient medium contains tetracycline.
CA000386858A 1980-11-05 1981-09-29 Plasmids constructed by gene manipulation, strains of escherichia coli carrying them, and process of tryptophan production using said strains Expired CA1182409A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP154,706/80 1980-11-05
JP55154706A JPS5780398A (en) 1980-11-05 1980-11-05 Plasmid produced by genetic manipulation, coliform bacillus having the same and preparation of tryptophan with said bacillus

Publications (1)

Publication Number Publication Date
CA1182409A true CA1182409A (en) 1985-02-12

Family

ID=15590169

Family Applications (1)

Application Number Title Priority Date Filing Date
CA000386858A Expired CA1182409A (en) 1980-11-05 1981-09-29 Plasmids constructed by gene manipulation, strains of escherichia coli carrying them, and process of tryptophan production using said strains

Country Status (3)

Country Link
JP (1) JPS5780398A (en)
AU (1) AU549686B2 (en)
CA (1) CA1182409A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6180373B1 (en) 1992-09-28 2001-01-30 Consortium f{umlaut over (u)}r elektrochemische Industrie GmbH Microorganisms for the production of tryptophan and process for the preparation thereof
EP1715056A1 (en) 2005-04-23 2006-10-25 Degussa AG Process for the production of L-amino acids using improved Enterobacteriaceae strains
DE102007051024A1 (en) 2007-03-05 2008-09-11 Evonik Degussa Gmbh Process for the preparation of L-amino acids using strains of the family Enterobacteriaceae
EP1975241A1 (en) 2007-03-29 2008-10-01 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
EP2036979A1 (en) 2007-09-15 2009-03-18 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
EP2055785A1 (en) 2007-11-02 2009-05-06 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
EP2060636A1 (en) 2007-11-14 2009-05-20 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
DE102008040352A1 (en) 2008-07-11 2010-01-14 Evonik Degussa Gmbh Process for the preparation of L-tryptophan using improved strains of the family Enterobacteriaceae
DE102008044768A1 (en) 2008-08-28 2010-03-04 Evonik Degussa Gmbh Process for the preparation of organochemical compounds using improved strains of the family Enterobacteriaceae
EP2628792A1 (en) 2012-02-17 2013-08-21 Evonik Industries AG Cell with reduced ppGppase activity
WO2014117992A1 (en) 2013-01-30 2014-08-07 Evonik Industries Ag Microorganism and method for production of amino acids by fermentation
EP3385275A1 (en) 2017-04-07 2018-10-10 Evonik Degussa GmbH Method for producing aromatic l-amino acids using improved strains of the enterobacteriaceae family
US11053526B2 (en) 2018-08-09 2021-07-06 Evonik Operations Gmbh Process for preparing L amino acids using improved strains of the enterobacteriaceae family

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA811368B (en) * 1980-03-24 1982-04-28 Genentech Inc Bacterial polypedtide expression employing tryptophan promoter-operator
JPH074257B2 (en) * 1983-06-17 1995-01-25 三菱油化株式会社 Novel plasmid
JPS6043392A (en) * 1983-08-20 1985-03-07 Showa Denko Kk Preparation of l-tryptophan
EP0190921A3 (en) * 1985-02-04 1988-01-13 Engenics, Inc. Method for the overproduction of amino acids
EP0293207A3 (en) * 1987-05-29 1989-11-02 The Standard Oil Company Eschericia coli carrying recombinant plasmid for the production of tryptophan
JPH0722510B2 (en) * 1988-05-09 1995-03-15 三井東圧化学株式会社 Gene encoding thermostable tryptophan synthase and its use
US6118047A (en) 1993-08-25 2000-09-12 Dekalb Genetic Corporation Anthranilate synthase gene and method of use thereof for conferring tryptophan overproduction
BR112015026210B1 (en) * 2013-04-16 2022-11-29 Cj Cheiljedang Corporation RECOMBINANT MICROORGANISM HAVING IMPROVED L-TRYPTOPHAN PRODUCTIVITY AND METHOD FOR PRODUCING L-TRYPTOPHAN

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4371614A (en) * 1980-08-22 1983-02-01 Ajinomoto Co., Inc. E.Coli bacteria carrying recombinant plasmids and their use in the fermentative production of L-tryptophan

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6180373B1 (en) 1992-09-28 2001-01-30 Consortium f{umlaut over (u)}r elektrochemische Industrie GmbH Microorganisms for the production of tryptophan and process for the preparation thereof
EP1715056A1 (en) 2005-04-23 2006-10-25 Degussa AG Process for the production of L-amino acids using improved Enterobacteriaceae strains
DE102007051024A1 (en) 2007-03-05 2008-09-11 Evonik Degussa Gmbh Process for the preparation of L-amino acids using strains of the family Enterobacteriaceae
EP1975241A1 (en) 2007-03-29 2008-10-01 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
EP2036979A1 (en) 2007-09-15 2009-03-18 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
DE102007044134A1 (en) 2007-09-15 2009-03-19 Evonik Degussa Gmbh Process for the preparation of L-amino acids using improved strains of the family Enterobacteriaceae
EP2055785A1 (en) 2007-11-02 2009-05-06 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
EP2060636A1 (en) 2007-11-14 2009-05-20 Evonik Degussa GmbH Method for manufacturing L-amino acids using improved strains of the enterobacteriaceae family
DE102008040352A1 (en) 2008-07-11 2010-01-14 Evonik Degussa Gmbh Process for the preparation of L-tryptophan using improved strains of the family Enterobacteriaceae
EP2147972A1 (en) 2008-07-11 2010-01-27 Evonik Degussa GmbH Method for manufacturing L-tryptophane using improved strains of the enterobacteriaceae family
DE102008044768A1 (en) 2008-08-28 2010-03-04 Evonik Degussa Gmbh Process for the preparation of organochemical compounds using improved strains of the family Enterobacteriaceae
EP2163613A2 (en) 2008-08-28 2010-03-17 Evonik Degussa GmbH Method for manufacturing organic chemical compounds using improved strains of the enterobacteriaceae family
EP2628792A1 (en) 2012-02-17 2013-08-21 Evonik Industries AG Cell with reduced ppGppase activity
WO2014117992A1 (en) 2013-01-30 2014-08-07 Evonik Industries Ag Microorganism and method for production of amino acids by fermentation
EP3385275A1 (en) 2017-04-07 2018-10-10 Evonik Degussa GmbH Method for producing aromatic l-amino acids using improved strains of the enterobacteriaceae family
US11053526B2 (en) 2018-08-09 2021-07-06 Evonik Operations Gmbh Process for preparing L amino acids using improved strains of the enterobacteriaceae family

Also Published As

Publication number Publication date
AU549686B2 (en) 1986-02-06
JPH0226955B2 (en) 1990-06-13
JPS5780398A (en) 1982-05-19
AU7464481A (en) 1982-05-13

Similar Documents

Publication Publication Date Title
CA1182409A (en) Plasmids constructed by gene manipulation, strains of escherichia coli carrying them, and process of tryptophan production using said strains
KR900004426B1 (en) Process for producing l-tyrosine
JPH024276B2 (en)
FR2484448A1 (en) PROCESS FOR PRODUCING L-ARGININE BY FERMENTATION
JPS61202694A (en) Production of l-glutamine by fermentation method
KR970001238B1 (en) Process for l-tryptophan
JPS6321479B2 (en)
US4683205A (en) Method for transforming microorganisms
EP0123903B1 (en) Method for producing l-aspartic acid
KR100954052B1 (en) Microorganisms of corynebacterium having an inactivated gene encoding abc-transpoter and processes for the preparation of 5'-inosinic acid using the same
JPH0351400B2 (en)
US4598046A (en) Mutant strain of Escherichia coli and its use for the preparation of glutathione
JPH0142672B2 (en)
JPH06277067A (en) Gene dna coding acetohydroxy acid isomeroreductase
EP0180192A1 (en) Novel plasmids
KR100576341B1 (en) Microorganisms of Corynebacterium having an enactivated gene encoding 5'-nucleotidase and processes for the preparation of 5'-inosinic acid using the same
KR100547585B1 (en) Microorganisms of Corynebacterium and Preparation Method of 5'-inosinic Acid Using the Same
KR100964078B1 (en) Corynebacterium ammoniagenes having enhanced 5'-inosinic acid productivity and method of producing 5'-inosinic acid using the same
JPH059063B2 (en)
KR100937326B1 (en) Microorganisms of corynebacterium having an inactivated gene encoding oxidoreductase and processes for the preparation of 5'-inosinic acid using the same
KR100547586B1 (en) Recombinant Escherichia spp. microorganisms in which the uShA gene is inactivated and 5'-guanylic acid synthase using the same
KR101049023B1 (en) Corynebacterium ammoniagenes with 5'-inosinic acid production capacity and method for producing 5'-inosine acid using the same
JPH062052B2 (en) Genetically modified Escherichia coli and method for producing L-phenylalanine using the same
JPS6047692A (en) Production of l-threonine by fermentation
JPS63185372A (en) Breeding of microorganish

Legal Events

Date Code Title Description
MKEX Expiry