WO1998045425A9 - DEVELOPMENT OF HIGH-ETHANOL RESISTANT $i(ESCHERICHIA COLI) - Google Patents

DEVELOPMENT OF HIGH-ETHANOL RESISTANT $i(ESCHERICHIA COLI)

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Publication number
WO1998045425A9
WO1998045425A9 PCT/US1998/006405 US9806405W WO9845425A9 WO 1998045425 A9 WO1998045425 A9 WO 1998045425A9 US 9806405 W US9806405 W US 9806405W WO 9845425 A9 WO9845425 A9 WO 9845425A9
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WO
WIPO (PCT)
Prior art keywords
ethanol
microorganism
ethanologenic
microorganisms
liquid medium
Prior art date
Application number
PCT/US1998/006405
Other languages
French (fr)
Other versions
WO1998045425A1 (en
Inventor
Lonnie O Ingram
Lorraine P Yomano
Sean W York
Original Assignee
Univ Florida
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Filing date
Publication date
Application filed by Univ Florida filed Critical Univ Florida
Priority to EP98914390A priority Critical patent/EP0973882A1/en
Priority to CA002286334A priority patent/CA2286334A1/en
Priority to AU68752/98A priority patent/AU6875298A/en
Priority to JP54287898A priority patent/JP2001518789A/en
Publication of WO1998045425A1 publication Critical patent/WO1998045425A1/en
Publication of WO1998045425A9 publication Critical patent/WO1998045425A9/en

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    • 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
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/36Adaptation or attenuation of cells
    • 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
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • C12N1/205Bacterial isolates
    • 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
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/065Ethanol, i.e. non-beverage with microorganisms other than yeasts
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/185Escherichia
    • C12R2001/19Escherichia coli
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • Escherichia coli KOll is much less ethanol tolerant.
  • bacteria have been developed that have the ability to convert the sugars from, for example, lignocellulose to ethanol, the problem remains that ethanol tolerance in these bacteria limits botn the rate of ethanol production and the final ethanol concentration which can be achieved m the fermentors .
  • This invention is based upon the discovery that novel mutants of Escherichia coli KOll exhibit the ability to grow and survive m etnanol concentrations beyond that m which the parent Escherichia coli KOll can survive.
  • the invention is also based upon the discovery of an improved ethanol selection process which alternates between selection for ethanol resistance m liquid medium and selection for rapid growth on solid medium containing a high level of chloramphenicol . This selection process resulted m novel strains of Escherichia coli KOll, as discussed above, which are useful for ethanol production.
  • mutants producing 20% more ethanol and completing fermentation more rapidly than the parental E. coli KOll strain, could be produced. Moreover, the mutants are capable of growth m up to 50 g/L ethanol while the parent is incapable of growth at 35 g/L ethanol . Finally, the mutants show dramatically enhanced survival exposure to 100 g/L ethanol as compared to the parent. These characteristics of the mutants means that the expense of ethanol production from lignocellulosic hydrolysates will decrease by achieving higher ethanol concentrations m shorter times and reducing the costs of nutrients, capital equipment, product recovery and waste disposal.
  • the invention comprises a method for the selection of ethanologenic microorganisms comprising contacting the microorganisms sequentially to a liquid medium and a solid medium, wherein said liquid medium is used to select for ethanol tolerance and said solid medium is used to select for ethanologenic microorganisms having the ability to grow and produce ethanol .
  • the invention comprises liquid media containing increasing concentrations of ethanol and solid media containing antibiotics and a fermentable sugar for use m the above selection process .
  • the invention comprises an ethanologenic microorganism having the ability to grow m ethanol concentrations of greater than 35 g/L.
  • the ethanologenic microorganism is selected from the group consisting of Erwima, Klebsiella, Xanthomonas , Zymomonas and Escherichia, specifically K. oxytoca and E. coli .
  • the E . coli bacterium is selected from the group comprising LY01, LY02 and LY03.
  • the invention comprises an ethanologenic mutant having the ability to produce at least 10% more ethanol than the parental bacteria, preferably Escheri chia coli KOll, under equivalent fermentation conditions.
  • Figure IB shows the ability of mutants to survive in 10% ethanol (w/w) relative to the parental Escherichia coli KOll.
  • Figure 2A shows the ability of mutants, relative to the parental Escherichia coli KOll, to grow in the presence of glucose and no ethanol .
  • Figure 2B shows the ability of the LY01 mutants to grow in varying concentrations of ethanol and constant glucose relative to the parental Escherichia coli KOll strain in 3.5% ethanol and constant glucose.
  • Figure 2C shows the ability of mutants, relative to the parental Escherichia coli KOll, to grow in the presence of xylose and no ethanol .
  • Figure 2D shows the ability of the LYOl mutants to grow in varying concentrations of ethanol and constant xylose relative to the parental Escheri chia coli KOll strain in 3.5% ethanol and constant xylose.
  • Figure 3A shows the osmotic tolerance of mutants to increasing concentrations of glucose relative to the parental Escherichia coli KOll.
  • Figure 3B shows the osmotic tolerance of mutants to increasing concentrations of xylose relative to the parental Escherichia coli KOll.
  • Figure 4A shows the ability of mutants to convert 14% glucose to ethanol relative to the parental Escherichia coli KOll.
  • Figure 4B shows the ability of mutants to convert 14% xylose to ethanol relative to the parental Escheri chia coli KOll.
  • Figure 5 shows a map of pLOI1531 and subclones .
  • the map is of insert DNA from KOll.
  • the vector is not shown.
  • Figure 6 is a map of pL0I1534 and subclones.
  • the invention relates to an ethanologenic mutant having improved ethanol tolerance.
  • the mutant can produce at least 10% more ethanol than the parental bacteria, (e.g. Escherichia coli KOll) when grown under equivalent conditions.
  • the mutant can grow in ethanol concentrations which exceed those of the parental microorganism.
  • a microorganism e.g., an ethanologenic microorganism
  • mutant of the subject invention can be produced by the process of (1) contacting the parental microorganism (e.g., an ethanologenic microorganism) with a first liquid medium comprising an aqueous solution comprising ethanol, selecting one or more microorganisms that survive; (2) contacting one or more microorganisms obtained from the preceding step with a solid growth medium for a sufficient period of time to permit growth.
  • This process can be repeated, such as two, three, four or more times to further improve ethanol tolerance. With each repeating step, the concentration of ethanol is incrementally increased.
  • the m ⁇ croorgan ⁇ sm(s) obtained from step (2) can be contacted (step (3)) with a second liquid medium comprising an aqueous solution comprising an amount of ethanol greater than present m said first liquid medium, selecting one or more microorganisms that survive; and (4) contacting one or more microorganisms obtained from the preceding step with a solid growth medium for a sufficient period of time to permit growth.
  • the microorganisms selected m such a manner have improved ethanol tolerance to the parental microorganisms .
  • the liquid and solid mediums can contain additional components, as necessary or desirable.
  • the solid medium can include nutrients, such as sources of carbon, sulfur and nitrogen suitable for growth of the parental microorganism.
  • suitable growth medium include Luna broth and Basal Salts Media.
  • the solid medium will contain a sugar, such as xylose and/or glucose. This is desirable to ensure that the microorganisms selected form this step can produce ethanol from the sugar source m good to excellent yields (such as possessing the same or better ethanol production ability as the parent microorganism) .
  • the medium can also include an antibiotic, e.g. chloramphenicol , tetracyclme, or ampicillm and a fermentable sugar.
  • the liquid media include an aqueous solution of ethanol.
  • the media can, optionally, contain nutrients as well, including a suitable carbon, sulfur and nitrogen source.
  • the liquid medium can also contain a buffer to control the pH of the medium.
  • the liquid media preferably contain sugar, such as xylose and/or glucose.
  • the first liquid medium, second liquid medium or both generally contain at least about 3.5% (by weight) ethanol.
  • the second and subsequent liquid media contain incrementally greater concentrations of ethanol.
  • the second liquid medium can contain at least about 4% (by weight) ethanol.
  • a third liquid medium (when present) can contain at least about 4.5% (by weight) ethanol.
  • the microorganisms which can be subjected to the above process can be prokaryotic or eukaryotic and include bacteria, yeasts and fungi.
  • the process is particularly suited for ethanologenic microorganisms (such as ethanologenic bacterium) which comprise one or more enzymes which convert a sugar (such as a pentose (e.g., xylose) or a hexose (e.g., glucose)) to ethanol.
  • suitable ethanologenic microorganisms comprise one or more nucleic acid molecules which encode alcohol dehydrogenase and pyruvate decarboxylase .
  • Ethanologenic bacteria comprising one or more nucleic acid molecules which encode alcohol dehydrogenase and pyruvate decarboxylase (as isolated from, for example, Zymomonas species, such as Zymomonas mobilis) are known. Also microorganisms that possess xylulokinase, transaldolase, transketolase and xylose isomerase are known (such as those expressed by enteric bacteria, such as Escherichia coli ) . Many microorganisms have the ability to convert both xylose and glucose to ethanol. Such organisms possess both sets of enzymes.
  • a Ipet refers to the integration of Z. obilis pdc and adhB genes into the chromosome
  • b pet refers to the presence of Z. mobilis pdc and adhB genes in plasmid pL0I555.
  • c pet refers to the presence of Z. mobilis pdc and adhB genes in the indicated plasmid.
  • Cm r is the an E. coli shuttle vector carrying the cat gene.
  • Ethanologenic microorganisms or host cells which can be employed for the insertion of enzymes which convert one or more sugars to ethanol, can be selected from bacteria, yeasts, fungi, or other cells. Suitable bacteria include Erwinia, Klebsiella, Xanthomonas,
  • Zymomonas such as Zymomonas mobilis
  • Escherichia Preferred species include K. oxytoca and E . coli .
  • gram-positlve bacteria such as members of the genera Bacillus, for example, B . pumilus , B . subtilis and B . coagulans , members of the genera Clost ⁇ dium, for example, Cl . acetobutylicum, Cl . aerotolerans , Cl . thermocellum, Cl . thermohydrosulfuricum and Cl . the mo s ac char olyti cum, members of the genera Cellulomanas like C.
  • Acceptable yeasts are of the species of Cryptococcus like Cr. albidus , Momlia, and Pichia stipi ti s and Pullularia pullulans .
  • the above microorganisms can be subjected to the selection process of the claimed invention as they occur m nature or after isolation or genetic manipulation, as m mutation or genetic engineering.
  • soil or fecal samples containing microorganisms can be subjected to the described process.
  • the ethanologenic properties of the mutated microorganism can be introduced or further improved by inserting one or more enzymes which convert a sugar to ethanol, as described m the above patents.
  • an isolated ethanologenic microorganism with good to excellent ethanol producing properties are subjected to the above process.
  • the temperature and pressure of the process are generally not critical but should be selected to ensure viability and growth of the microorganisms. Suitable temperatures can be between about 20° and about 60°C. Pressure will generally be atmospheric.
  • the pH should also be selected towards the ability of the microorganism to remain viable and grow. For example, the pH may generally be selected to be between about 4.5 and 8.0.
  • the tolerance of a microorganism (or members of the species) can be determined readily and frequently are related to the conditions of the microorganism's native environment. Guidance for selecting optimal conditions for growth can be obtained for example m Bergey ' s Manual of Bacteriology.
  • the retention time of each step of the process is also not generally critical.
  • the time m which the microorganisms are subjected to the ethanol -containing liquid medium is generally selected such that some, but not all, of the population has died.
  • the step can last between about 8 hours to two weeks . Frequently, several days can be sufficient. Where the step lasts for several days, it may be desirable to exchange or add fresh liquid medium with the same or greater concentration of ethanol to the microorganisms.
  • the time for permitting growth of the microorganism on the solid medium is not generally critical and is dependent upon the microorganism. Slow growing microorganisms will require longer retention times than fast growing microorganisms, as generally known m the art. The time is generally long enough to differentiate colonies which are growing better than other colonies. Frequently, several days are sufficient for a fast growing bacteria.
  • the mutants produced by the claimed process have greater ethanol tolerance than the parental microorganisms.
  • the microorganisms can have improved ability to produce ethanol, as well.
  • the genetic basis for the mutation can be identified. For example, the chromosome and/or the RNA transcripts produced by the mutant microorganism can be compared to the parent microorganism. This can be done through hybridization technology, as described generally m Sambrook, et al . and Ausubel, et al . Once the genetic basis of the improved mutant has been identified, the mutation can be repeated or an equivalent produced through genetic engineering.
  • a recombmantly produced equivalent can be made by deleting the gene, deleting the regulatory sequences of the gene or targeting a site-specifIC mutation to shift the reading frame or remove an active site of the gene, as described m Ausubel, et al . and Sambrook, et al .
  • the result is the inability of the microorganism to express an active gene product.
  • recombmantly produced equivalent can be made by substituting the native promoter with a stronger promoter of the gene, adding an enhancer or introducing more copies of the gene.
  • a recombmantly produced equivalent can be prepared by introducing the mutated sequence under the control of a promoter region recognized by the host cell.
  • mutants which do not express active cyclic 7AMP receptor protein, active biosynthetic alanme racemase or both have increased ethanol tolerance.
  • the invention includes microorganisms of increased ethanol tolerance wherein the microorganism does not express active cyclic 7AMP receptor protein, active biosynthetic alanme racemase or both. This can be achieved, for example, by such molecular biology techniques as site-specific mutagenesis and knocking out the gene, also known as "knock outs.” This can be accomplished, for example, by homologous recombination, described m Ausubel, et al . and Sambrook, et al .
  • Microorganisms which do not express active cyclic AMP receptor protein and/or active biosynthetic alanme racemase can be particularly suitable host cells for expressing enzymes (e.g., recombmantly) which convert a sugar to ethanol .
  • Suitable microorganisms for use the invention are as discussed above.
  • Preferred microorganisms are bacteria, particularly gram-negative bacteria (e.g., enteric bacteria) such as Escherichia coli , Erwinia chrysanthia and Klebsiella oxytoca .
  • Particularly preferred microorganisms include those described m the U.S. Patents and applications to Ingram, et al . and Picataggio, et al . , above.
  • the invention further relates to methods of using the ethanol tolerant microorganisms described herein.
  • Microorganisms which have increased ethanol tolerance can be ethanologenic or not ethanologenic .
  • Ethanologenic microorganisms can be used m methods of producing ethanol, employing processes generally known m the art. Examples of suitable ethanol -producing processes include those described m the above patents and application to Ingram, et al . and Picataggio, et al . , which have been incorporated by reference.
  • An improved process for producing ethanol is described m copendmg application U.S.S.N. 08/833,435, by Ingram, et al .
  • ethanologenic microorganisms are particularly useful for the production of ethanol from lignocellulosic waste.
  • Other processes for the use of ethanologenic microorganisms include the fermentation of sugar containing materials to foods and beverages.
  • ethanologenic microorganisms are employed in the manufacture of soy sauce, sake, beer and wine.
  • this invention can be employed to further improve the activities and ethanol tolerance of the microorganisms employed in these processes.
  • Microorganisms of the invention which are not ethanologenic or slightly ethanologenic are particularly useful as host cells for inserting nucleic acid molecules which encode one or more enzymes which catalyze one or more reactions in the glycolytic pathway, or other pathway which converts sugar to ethanol. That is, such microorganisms are particularly useful in the production of ethanologenic microorganisms through recombinant DNA technology.
  • E. coli KOll was used in these studies. This is an ethanol producing derivative of E. coli B in which the Zymomonas mobilis genes for ethanol production (pdc, adhB) have been integrated into the chromosome immediately upstream from chloramphenicol acyl transferase (ca t) (U.S. Patent No. 5,424,202). In this strain, resistance to chloramphenicol (600 mg liter ⁇ ) was used to select for high level expression of pdc and adhB . Cultures were grown m modified Luna broth containing per liter: 5 g NaCl , 5 g Yeast Extract, 10 g Tryptone, 40 or 600 mg chloramphenicol, and 20-140 g of fermentable carbohydrate.
  • KOll cultures were transferred daily by diluting 1:20 to 1:200 into 10 ml of fresh broth containing ethanol and glucose (50 g liter ⁇ ) m 18x150 mm culture tubes. Tubes were incubated for 24 h at 35°C without agitation. As cultures increased m density during subsequent transfers, ethanol concentrations were progressively increased to select for resistant mutants. Twice weekly, cultures were diluted and spread on solid medium to enrich for ethanol-resistant mutants which grew rapidly and retained high level expression of the Z. mobilis genes. Colonies on these plates were scraped • into fresh broth and diluted. The dilutions were then used as inocula in ethanol-containing broth. KOll was initially transferred into 3.5% ethanol.
  • the ethanol concentration in the broth was increased to 4.0%; after 13 days, the ethanol concentration was increased to 4.5%; after 14 days, the ethanol concentration was increased to 5.0%. Dilutions into higher concentrations of ethanol did not appear to yield mutants with further increases in ethanol resistance which were also capable of rapid growth.
  • KOll. Colonies were transferred to 3 ml of broth and the resulting suspension diluted 60-fold into 13x100 culture tubes containing 0%, 4.5%, and 5% ethanol. After incubation for 24 h at 35°C, cell growth was measured as O.D. 550nm .
  • Mutants were maintained on plates containing 1% isopropanol and stored at -75°C in 40% glycerol .
  • Inocula were grown for 16 h (Beall, D.S. et al . , "Parametric studies of ethanol production from xylose and other sugars by recombinant Escherichia coli . " Biotechnol . Bioeng . 38:296-303 (1991)) (30°C) without agitation in Luria broth containing glucose or xylose (50 g/L) . Cells were harvested by centrifugation (6000 x g, 5 min, ambient temperature) and added to initiate fermentation to provide 1.0 OD at 550 nm (approximately 330 mg liter "1 , dry cell weight) .
  • Genomic Library Chromosomal DNA was isolated from KOll essentially as described by Cutting, S.M. and Vander Horn, P.B., Genetic analysis, p. 37-74. In C.R. Harwood and S.M. Cutting (ed.), Molecular biological methods for Bacillus . John Wiley & sons Ltd., Chichester, England (1990) .
  • a genomic library of the parental strain, KOll was constructed by ligatmg Sau3AI partial digestion products (4-9 kbp fragments) into the BamHI site of pUC18 followed by transformation into DHS ⁇ .
  • the resulting library consisted of approximately 8,000 clones. After pooling these colonies, plasmids were isolated to produce a library. Standard procedures were used for the construction, isolation, transformation, and analysis of plasmids (Sambrook et al . , 1989) .
  • D-cycloserme was used to selectively kill cells capable of growing m 3.5% ethanol (w/w) while allowing non-growmg cells to survive. At this concentration of ethanol, mutants continue to grow while the parent remains viable without increasing m cell number.
  • LY02 and LY03 were transformed with the KOll plasmid library and allowed to grow overnight into colonies. Recombmant colonies of each mutant were harvested by scraping into Luria broth containing glucose (50 g liter 1 ) and 3.5% ethanol, inoculated to provide 0.1 O.D. at 550 n , and incubated at 35°C. After 1.5 hr, D-cycloserme (100 mg liter ) was added and the incubation continued for 4 hours. After 4 h, CFU/ml had dropped by over 95%. Clones harboring putative genes for decreased ethanol tolerance were isolated from these plates .
  • the QIAprep spin plasmid kit (Qiagen, Chatsworth, CA) was used for plasmid purification. Dideoxy sequencmg was performed using fluorescent primers [forward, 5 ' CACGACGTTGTAAAACGAC-3 ' (SEQ ID N0:1); reverse, 5 ' -ATAACAATTTCACACAGGA-3 ' (SEQ ID NO : 2 ) ] (LI -COR, Lincoln, NE) .
  • Extension reactions were performed with a Perkm Elmer GeneAmp PCR System 9600 (Norwalk, CT) using an Excel Sequencing Kit-LC (Epicentre Technologies, Madison, WI) (30 cycles; denaturation for 30 sec at 95°C, annealing for 30 sec at 60°C, and extension for 1 mm at 70°C) . Extension products were separated and read with a LI -COR DNA Sequencer model 4000L.
  • EXAMPLE 1 Isolation of Ethanol-tolerant Mutants of E. Coli KOll Using the materials and procedures outlined above, a total of 135 colonies were initially tested for growth m 4.5% (w/w) ethanol, a concentration at which the parental KOll failed to grow. Forty three colonies were turbid after 24 h incubation at 35°C and were saved for further testing.
  • Ethanol tolerance was also compared using other fermentable sugars which may be of interest for fuel ethanol production: lactose, arabmose, and mannose, galactose, sucrose and raffmose.
  • KOll growth was consistently above that of the mutants m the absence of ethanol.
  • KOll failed to grow m ethanol concentrations above 3% (w/w) while the mutants grew in 5% ethanol with all sugars tested.
  • LYOl, LY02 , LY03 , and LY04 were transferred daily on solid medium lacking alcohol for 30 days. Cells were then used to inoculate broth cultures containing ethanol as shown m Figures 2C and 2D. The resulting growth curves were identical to those initially determined.
  • the retention of osmotic tolerance to sugars is essential for the utility of ethanol-tolerant mutants of KOll.
  • tolerance to xylose and glucose are similar on a molar basis. With both sugars, KOll appeared more resistant to osmotic stress than the ethanol -resistant mutants, although this difference was not dramatic. No differences were observed m growth at 48°C, the maximum temperature for growth. Both KOll and the mutants grew slowly at this temperature .
  • Plasmid pLOI1531 contains a 3.6 kbp fragment of KOll DNA within the 67.4 mm-76.0 mm region of the E . coli chromosome (GenBank Accession Number U18997) . Subclones were prepared and sequenced to confirm gene arrangement m KOll and to identify the genes which are responsible for a decrease m ethanol tolerance ( Figure 5) . Only 2 open reading frames were present: crp and a large open reading frame of unidentified function (ORF 0696).
  • pL0I1534 contains a 7.39 kbp fragment of KOll DNA within the 89.2 mm -92.8 mm segment (Accession Number U00006 of the E. coli chromosome ( Figure 6) .
  • Deleted derivatives of this clone were also sequenced to confirm gene arrangement and revealed the presence of 3 complete and 2 partial open reading frames: dnaB ' , air, tyrB, napA (hobH) , and uvrA ' .
  • a comparison of deleted derivatives identified the air gene (biosynthetic alanme racemase) as being responsible for decreasing the ethanol tolerance of LY02.

Abstract

The invention relates to a novel selection process to identify novel mutants of Escherichia coli KO11, an ethanologenic bacterium, that exhibit the ability to grow and survive in ethanol concentrations beyond that in which the parent Escherichia coli KO11 can survive. The new approach, which alternates between selection for ethanol resistance and selection for rapid growth on solid medium containing a high level of chloramphenicol, resulted in strains which are potentially useful for ethanol production.

Description

DEVELOPMENT OF HIGH-ETHANOL RESISTANT ESCHERICHIA COLI
BACKGROUND OF THE INVENTION
The fermentation of waste paper and other lignocellulosic products, such as crop residues, into ethanol offers the opportunity to reduce environmental waste problems and reduce reliance on petroleum-based automotive fuels. Genetically engineered bacteria, such as Escherichia coli KOll (U.S Patent No. 5,000,000) and Klehsiella oxytoca P2 (U.S Patent No. 5,424,202), have been developed which convert both pentose and hexose sugars, produced by the hydrolysis of hemicellulose , into ethanol .
Relative to yeast, such as Saccharomyces , which is currently used for commercial ethanol production from cane syrup and from hydrolyzed corn starch, Escherichia coli KOll is much less ethanol tolerant. Thus, even though bacteria have been developed that have the ability to convert the sugars from, for example, lignocellulose to ethanol, the problem remains that ethanol tolerance in these bacteria limits botn the rate of ethanol production and the final ethanol concentration which can be achieved m the fermentors .
SUMMARY OF THE INVENTION
This invention is based upon the discovery that novel mutants of Escherichia coli KOll exhibit the ability to grow and survive m etnanol concentrations beyond that m which the parent Escherichia coli KOll can survive. The invention is also based upon the discovery of an improved ethanol selection process which alternates between selection for ethanol resistance m liquid medium and selection for rapid growth on solid medium containing a high level of chloramphenicol . This selection process resulted m novel strains of Escherichia coli KOll, as discussed above, which are useful for ethanol production.
It was discovered that, by using this new approach, mutants producing 20% more ethanol and completing fermentation more rapidly than the parental E. coli KOll strain, could be produced. Moreover, the mutants are capable of growth m up to 50 g/L ethanol while the parent is incapable of growth at 35 g/L ethanol . Finally, the mutants show dramatically enhanced survival exposure to 100 g/L ethanol as compared to the parent. These characteristics of the mutants means that the expense of ethanol production from lignocellulosic hydrolysates will decrease by achieving higher ethanol concentrations m shorter times and reducing the costs of nutrients, capital equipment, product recovery and waste disposal.
In one embodiment, the invention comprises a method for the selection of ethanologenic microorganisms comprising contacting the microorganisms sequentially to a liquid medium and a solid medium, wherein said liquid medium is used to select for ethanol tolerance and said solid medium is used to select for ethanologenic microorganisms having the ability to grow and produce ethanol .
In a preferred embodiment, the invention comprises liquid media containing increasing concentrations of ethanol and solid media containing antibiotics and a fermentable sugar for use m the above selection process .
In another embodiment the invention comprises an ethanologenic microorganism having the ability to grow m ethanol concentrations of greater than 35 g/L. In a preferred embodiment the ethanologenic microorganism is selected from the group consisting of Erwima, Klebsiella, Xanthomonas , Zymomonas and Escherichia, specifically K. oxytoca and E. coli . In a more preferred embodiment the E . coli bacterium is selected from the group comprising LY01, LY02 and LY03.
In still another embodiment the invention comprises an ethanologenic mutant having the ability to produce at least 10% more ethanol than the parental bacteria, preferably Escheri chia coli KOll, under equivalent fermentation conditions.
Furthermore, it has been discolvered that the mactivation of cyclic AMP receptor protein and/or active biosynthetic alamne racemase results m a microorganism with improved ethanol tolerance.
BRIEF DESCRIPTION OF THE DRAWINGS
The foregoing and other objects, features and advantages of the invention will be apparent from the following more particular description of preferred embodiments of the invention, as illustrated m the accompanying drawings m which like reference characters refer to the same parts throughout the different views. The drawings are not necessarily to scale, emphasis instead being placed upon illustrating the principles of the invention. Figure 1A shows the ability of mutants to grow in increasing concentrations of ethanol relative to the parental Escherichia coli KOll.
Figure IB shows the ability of mutants to survive in 10% ethanol (w/w) relative to the parental Escherichia coli KOll.
Figure 2A shows the ability of mutants, relative to the parental Escherichia coli KOll, to grow in the presence of glucose and no ethanol . Figure 2B shows the ability of the LY01 mutants to grow in varying concentrations of ethanol and constant glucose relative to the parental Escherichia coli KOll strain in 3.5% ethanol and constant glucose.
Figure 2C shows the ability of mutants, relative to the parental Escherichia coli KOll, to grow in the presence of xylose and no ethanol .
Figure 2D shows the ability of the LYOl mutants to grow in varying concentrations of ethanol and constant xylose relative to the parental Escheri chia coli KOll strain in 3.5% ethanol and constant xylose.
Figure 3A shows the osmotic tolerance of mutants to increasing concentrations of glucose relative to the parental Escherichia coli KOll.
Figure 3B shows the osmotic tolerance of mutants to increasing concentrations of xylose relative to the parental Escherichia coli KOll.
Figure 4A shows the ability of mutants to convert 14% glucose to ethanol relative to the parental Escherichia coli KOll. Figure 4B shows the ability of mutants to convert 14% xylose to ethanol relative to the parental Escheri chia coli KOll. Figure 5 shows a map of pLOI1531 and subclones .
The map is of insert DNA from KOll. The vector is not shown.
Figure 6 is a map of pL0I1534 and subclones.
DETAILED DESCRIPTION OF THE INVENTION
As described above, the invention relates to an ethanologenic mutant having improved ethanol tolerance. In one embodiment the mutant can produce at least 10% more ethanol than the parental bacteria, (e.g. Escherichia coli KOll) when grown under equivalent conditions. In another embodiment the mutant can grow in ethanol concentrations which exceed those of the parental microorganism.
A microorganism (e.g., an ethanologenic microorganism), or "mutant" of the subject invention can be produced by the process of (1) contacting the parental microorganism (e.g., an ethanologenic microorganism) with a first liquid medium comprising an aqueous solution comprising ethanol, selecting one or more microorganisms that survive; (2) contacting one or more microorganisms obtained from the preceding step with a solid growth medium for a sufficient period of time to permit growth. This process can be repeated, such as two, three, four or more times to further improve ethanol tolerance. With each repeating step, the concentration of ethanol is incrementally increased. Thus, the mιcroorganιsm(s) obtained from step (2) can be contacted (step (3)) with a second liquid medium comprising an aqueous solution comprising an amount of ethanol greater than present m said first liquid medium, selecting one or more microorganisms that survive; and (4) contacting one or more microorganisms obtained from the preceding step with a solid growth medium for a sufficient period of time to permit growth. The microorganisms selected m such a manner have improved ethanol tolerance to the parental microorganisms .
The liquid and solid mediums can contain additional components, as necessary or desirable. For example, the solid medium can include nutrients, such as sources of carbon, sulfur and nitrogen suitable for growth of the parental microorganism. Examples of suitable growth medium include Luna broth and Basal Salts Media. Generally, the solid medium will contain a sugar, such as xylose and/or glucose. This is desirable to ensure that the microorganisms selected form this step can produce ethanol from the sugar source m good to excellent yields (such as possessing the same or better ethanol production ability as the parent microorganism) . The medium can also include an antibiotic, e.g. chloramphenicol , tetracyclme, or ampicillm and a fermentable sugar.
The liquid media include an aqueous solution of ethanol. In addition, the media can, optionally, contain nutrients as well, including a suitable carbon, sulfur and nitrogen source. The liquid medium can also contain a buffer to control the pH of the medium. As m the solid media, the liquid media preferably contain sugar, such as xylose and/or glucose. The first liquid medium, second liquid medium or both generally contain at least about 3.5% (by weight) ethanol. The second and subsequent liquid media contain incrementally greater concentrations of ethanol. For example, the second liquid medium can contain at least about 4% (by weight) ethanol. A third liquid medium (when present) can contain at least about 4.5% (by weight) ethanol. The microorganisms which can be subjected to the above process can be prokaryotic or eukaryotic and include bacteria, yeasts and fungi. The process is particularly suited for ethanologenic microorganisms (such as ethanologenic bacterium) which comprise one or more enzymes which convert a sugar (such as a pentose (e.g., xylose) or a hexose (e.g., glucose)) to ethanol. Examples of suitable ethanologenic microorganisms comprise one or more nucleic acid molecules which encode alcohol dehydrogenase and pyruvate decarboxylase . Ethanologenic bacteria comprising one or more nucleic acid molecules which encode alcohol dehydrogenase and pyruvate decarboxylase (as isolated from, for example, Zymomonas species, such as Zymomonas mobilis) are known. Also microorganisms that possess xylulokinase, transaldolase, transketolase and xylose isomerase are known (such as those expressed by enteric bacteria, such as Escherichia coli ) . Many microorganisms have the ability to convert both xylose and glucose to ethanol. Such organisms possess both sets of enzymes. These organisms have been manufactured by recombinant DNA technology by inserting the nucleic acid molecules which encode one set (or operon) of these enzymes into a host cell which, preferably, expresses the second set (or operon) of these enzymes. Table 1 summarizes several enzymes which possess the ability to convert both pentose and hexose to ethanol in good to high yields. TABLE 1
Figure imgf000010_0001
a Ipet refers to the integration of Z. obilis pdc and adhB genes into the chromosome, b pet refers to the presence of Z. mobilis pdc and adhB genes in plasmid pL0I555. c pet refers to the presence of Z. mobilis pdc and adhB genes in the indicated plasmid. Cmr is the an E. coli shuttle vector carrying the cat gene.
A more detailed description of these and other related recombinant organisms, as well as the techniques and materials used in their preparation can be found in, for example, United States Patent Nos. 5,028,539 to Ingram et al . , 5,000,000 to Ingram et al . 5,424,202 to Ingram et al . , 5,487,989 to Fowler et al . , 5,482,846 to Ingram et al . , 5,554,520 to Fowler et a 1 . , 5,514,583 to Picataggio, et al . , copendmg applications having U.S.S.N 08/363,868 filed on December 27, 1994, U.S.S.N. 08/475,925 filed on June 7, 1995 and U.S.S.N. 08/218,914 filed on March 28, 1994 and standard texts such as, Ausubel et al . , Current Protocols m Molecular Biology, Wiley-Interscience, New York (1988) (hereinafter "Ausubel et al . " ) , Sambrook et al . , Molecular Cloning: A Laboratory Manual , Second and Third Edition, Cold Spring Harbor Laboratory Press (1989 and 1992)
(hereinafter "Sambrook et al . " ) and Bergey ' s Manual of Systematic Bacteriology, William & Wilkms Co., Baltimore (1984) (hereinafter "Bergey's Manual") the teachings of all of which are hereby incorporated by reference m their entirety.
Additional microorganisms having improved ethanologenic activity are described m copendmg application U.S.S.N. 08/834,901, to Ingram et al . , filed April 7, 1997, which is also incorporated herein by reference.
Ethanologenic microorganisms, or host cells which can be employed for the insertion of enzymes which convert one or more sugars to ethanol, can be selected from bacteria, yeasts, fungi, or other cells. Suitable bacteria include Erwinia, Klebsiella, Xanthomonas,
Zymomonas (such as Zymomonas mobilis) and Escherichia. Preferred species include K. oxytoca and E . coli . Also envisioned are gram-positlve bacteria, such as members of the genera Bacillus, for example, B . pumilus , B . subtilis and B . coagulans , members of the genera Clostπdium, for example, Cl . acetobutylicum, Cl . aerotolerans , Cl . thermocellum, Cl . thermohydrosulfuricum and Cl . the mo s ac char olyti cum, members of the genera Cellulomanas like C. uda and Butyrivibrio fibrisolvens . Acceptable yeasts, for example, are of the species of Cryptococcus like Cr. albidus , Momlia, and Pichia stipi ti s and Pullularia pullulans .
The above microorganisms can be subjected to the selection process of the claimed invention as they occur m nature or after isolation or genetic manipulation, as m mutation or genetic engineering. For example, soil or fecal samples containing microorganisms can be subjected to the described process. In such an embodiment, the ethanologenic properties of the mutated microorganism can be introduced or further improved by inserting one or more enzymes which convert a sugar to ethanol, as described m the above patents. Alternatively, an isolated ethanologenic microorganism with good to excellent ethanol producing properties (such as one or more of the above recombmant microorganisms) are subjected to the above process. The temperature and pressure of the process are generally not critical but should be selected to ensure viability and growth of the microorganisms. Suitable temperatures can be between about 20° and about 60°C. Pressure will generally be atmospheric. The pH should also be selected towards the ability of the microorganism to remain viable and grow. For example, the pH may generally be selected to be between about 4.5 and 8.0. The tolerance of a microorganism (or members of the species) can be determined readily and frequently are related to the conditions of the microorganism's native environment. Guidance for selecting optimal conditions for growth can be obtained for example m Bergey ' s Manual of Bacteriology.
The retention time of each step of the process is also not generally critical. The time m which the microorganisms are subjected to the ethanol -containing liquid medium is generally selected such that some, but not all, of the population has died. For example, the step can last between about 8 hours to two weeks . Frequently, several days can be sufficient. Where the step lasts for several days, it may be desirable to exchange or add fresh liquid medium with the same or greater concentration of ethanol to the microorganisms. Likewise, the time for permitting growth of the microorganism on the solid medium is not generally critical and is dependent upon the microorganism. Slow growing microorganisms will require longer retention times than fast growing microorganisms, as generally known m the art. The time is generally long enough to differentiate colonies which are growing better than other colonies. Frequently, several days are sufficient for a fast growing bacteria.
As set forth above, the mutants produced by the claimed process have greater ethanol tolerance than the parental microorganisms. In mutating ethanologenic microorganisms, the microorganisms can have improved ability to produce ethanol, as well. Once the mutants have been isolated, the genetic basis for the mutation can be identified. For example, the chromosome and/or the RNA transcripts produced by the mutant microorganism can be compared to the parent microorganism. This can be done through hybridization technology, as described generally m Sambrook, et al . and Ausubel, et al . Once the genetic basis of the improved mutant has been identified, the mutation can be repeated or an equivalent produced through genetic engineering. For example, where the mutation is based upon the mactivation of a gene or genes, then a recombmantly produced equivalent can be made by deleting the gene, deleting the regulatory sequences of the gene or targeting a site-specifIC mutation to shift the reading frame or remove an active site of the gene, as described m Ausubel, et al . and Sambrook, et al . In any event, the result is the inability of the microorganism to express an active gene product. Where the mutation is based upon the increased expression of a gene, then recombmantly produced equivalent can be made by substituting the native promoter with a stronger promoter of the gene, adding an enhancer or introducing more copies of the gene. In yet another embodiment, where the mutation is based upon an activity caused by a mutation m the coding region of a gene, a recombmantly produced equivalent can be prepared by introducing the mutated sequence under the control of a promoter region recognized by the host cell.
In the examples below, it has been discovered that mutants which do not express active cyclic 7AMP receptor protein, active biosynthetic alanme racemase or both have increased ethanol tolerance. Thus the invention includes microorganisms of increased ethanol tolerance wherein the microorganism does not express active cyclic 7AMP receptor protein, active biosynthetic alanme racemase or both. This can be achieved, for example, by such molecular biology techniques as site-specific mutagenesis and knocking out the gene, also known as "knock outs." This can be accomplished, for example, by homologous recombination, described m Ausubel, et al . and Sambrook, et al .
Microorganisms which do not express active cyclic AMP receptor protein and/or active biosynthetic alanme racemase can be particularly suitable host cells for expressing enzymes (e.g., recombmantly) which convert a sugar to ethanol . Suitable microorganisms for use the invention are as discussed above. Preferred microorganisms are bacteria, particularly gram-negative bacteria (e.g., enteric bacteria) such as Escherichia coli , Erwinia chrysanthia and Klebsiella oxytoca . Particularly preferred microorganisms include those described m the U.S. Patents and applications to Ingram, et al . and Picataggio, et al . , above.
The invention further relates to methods of using the ethanol tolerant microorganisms described herein. Microorganisms which have increased ethanol tolerance can be ethanologenic or not ethanologenic . Ethanologenic microorganisms can be used m methods of producing ethanol, employing processes generally known m the art. Examples of suitable ethanol -producing processes include those described m the above patents and application to Ingram, et al . and Picataggio, et al . , which have been incorporated by reference. An improved process for producing ethanol is described m copendmg application U.S.S.N. 08/833,435, by Ingram, et al . , filed April 7, 1997, which is also incorporated herein by reference These processes are particularly useful for the production of ethanol from lignocellulosic waste. Other processes for the use of ethanologenic microorganisms include the fermentation of sugar containing materials to foods and beverages. For example, ethanologenic microorganisms are employed in the manufacture of soy sauce, sake, beer and wine. As such, this invention can be employed to further improve the activities and ethanol tolerance of the microorganisms employed in these processes.
Microorganisms of the invention which are not ethanologenic or slightly ethanologenic are particularly useful as host cells for inserting nucleic acid molecules which encode one or more enzymes which catalyze one or more reactions in the glycolytic pathway, or other pathway which converts sugar to ethanol. That is, such microorganisms are particularly useful in the production of ethanologenic microorganisms through recombinant DNA technology.
The invention will now be illustrated by one or more non-limiting examples.
EXEMPLIFICATION Methods and Materials The methods and materials described below were used in carrying out the work described in the examples which follow. For convenience and ease of understanding, the methods and materials section is divided into subheadings as follows.
Bacterial Strains and Media
E. coli KOll was used in these studies. This is an ethanol producing derivative of E. coli B in which the Zymomonas mobilis genes for ethanol production (pdc, adhB) have been integrated into the chromosome immediately upstream from chloramphenicol acyl transferase (ca t) (U.S. Patent No. 5,424,202). In this strain, resistance to chloramphenicol (600 mg liter λ) was used to select for high level expression of pdc and adhB . Cultures were grown m modified Luna broth containing per liter: 5 g NaCl , 5 g Yeast Extract, 10 g Tryptone, 40 or 600 mg chloramphenicol, and 20-140 g of fermentable carbohydrate.
Stock cultures of alcohol -resistant mutants were maintained on solid medium containing glucose (20 g liter 1) , chloramphenicol (600 mg liter l) , isopropanol (10 g liter 1) , and agar (15 g liter x) . Ethanol was added to the broth on a weight basis to prepare a stock solution (100 g kg x) which was diluted as necessary. Broth containing ethanol was filter sterilized using Nalgene 50 mm, 0.45μm bottle top filters (SFCA) . E. coli DH5a was used as a host for the construction of pUC18 -based plasmids . This strain was grown m modified Luna broth without added carbohydrate. Ampicillm (50 mg liter1) was used for selection as appropriate.
Enrichment and Selection of E . coli KOll Mutants
KOll cultures were transferred daily by diluting 1:20 to 1:200 into 10 ml of fresh broth containing ethanol and glucose (50 g liter λ) m 18x150 mm culture tubes. Tubes were incubated for 24 h at 35°C without agitation. As cultures increased m density during subsequent transfers, ethanol concentrations were progressively increased to select for resistant mutants. Twice weekly, cultures were diluted and spread on solid medium to enrich for ethanol-resistant mutants which grew rapidly and retained high level expression of the Z. mobilis genes. Colonies on these plates were scraped into fresh broth and diluted. The dilutions were then used as inocula in ethanol-containing broth. KOll was initially transferred into 3.5% ethanol. After 5 days of sequential transfer, the ethanol concentration in the broth was increased to 4.0%; after 13 days, the ethanol concentration was increased to 4.5%; after 14 days, the ethanol concentration was increased to 5.0%. Dilutions into higher concentrations of ethanol did not appear to yield mutants with further increases in ethanol resistance which were also capable of rapid growth.
Cultures were diluted and spread on solid medium containing chloramphenicol to allow the isolation of mutants. Large raised colonies were individually tested for ethanol resistance in comparison to the parent,
KOll. Colonies were transferred to 3 ml of broth and the resulting suspension diluted 60-fold into 13x100 culture tubes containing 0%, 4.5%, and 5% ethanol. After incubation for 24 h at 35°C, cell growth was measured as O.D.550nm.
Mutants were maintained on plates containing 1% isopropanol and stored at -75°C in 40% glycerol .
Cell Survival in 10% (w/w) Ethanol
Survival of mutant strains was compared to KOll after dilution into 10% ethanol. Cell suspensions
(approximately 0.05 O.D. at 550 nm) were prepared in Luria broth containing glucose (50 g liter"1) by transferring cells from overnight plates. These were preheated to 35°C and diluted at time zero with an equal volume of preheated broth containing 20% ethanol.
Dilution into broth lacking ethanol served as a control. Serial dilutions were spread on solid medium at time zero (no ethanol only), after 0.5 min, and after 5 min. After overnight incubation at 30°C, colonies from appropriate dilutions were counted to determine relative survival as colony forming units (CFU) .
Fermentation Experiments
Inocula were grown for 16 h (Beall, D.S. et al . , "Parametric studies of ethanol production from xylose and other sugars by recombinant Escherichia coli . " Biotechnol . Bioeng . 38:296-303 (1991)) (30°C) without agitation in Luria broth containing glucose or xylose (50 g/L) . Cells were harvested by centrifugation (6000 x g, 5 min, ambient temperature) and added to initiate fermentation to provide 1.0 OD at 550 nm (approximately 330 mg liter"1, dry cell weight) . Batch fermentations were carried out at 35°C (100 rpm) in modified 500-ml Fleaker™ beakers containing 350 ml of Luria broth supplemented with glucose or xylose (140 g liter"1) . Sugar solutions were sterilized by autoclaving separately. Automatic addition of 2 N KOH was used to prevent acidification above pH 6. Samples were removed to measure cell mass and ethanol. Base consumption and pH were also recorded.
Genetic Methods and Construction of a Genomic Library Chromosomal DNA was isolated from KOll essentially as described by Cutting, S.M. and Vander Horn, P.B., Genetic analysis, p. 37-74. In C.R. Harwood and S.M. Cutting (ed.), Molecular biological methods for Bacillus . John Wiley & sons Ltd., Chichester, England (1990) . A genomic library of the parental strain, KOll, was constructed by ligatmg Sau3AI partial digestion products (4-9 kbp fragments) into the BamHI site of pUC18 followed by transformation into DHSα . The resulting library consisted of approximately 8,000 clones. After pooling these colonies, plasmids were isolated to produce a library. Standard procedures were used for the construction, isolation, transformation, and analysis of plasmids (Sambrook et al . , 1989) .
Isolation of Plasmids Containing Native DNA Fragments from KOll Which Decrease Ethanol Tolerance by Reverse Complementation
D-cycloserme was used to selectively kill cells capable of growing m 3.5% ethanol (w/w) while allowing non-growmg cells to survive. At this concentration of ethanol, mutants continue to grow while the parent remains viable without increasing m cell number. LY02 and LY03 were transformed with the KOll plasmid library and allowed to grow overnight into colonies. Recombmant colonies of each mutant were harvested by scraping into Luria broth containing glucose (50 g liter1) and 3.5% ethanol, inoculated to provide 0.1 O.D. at 550 n , and incubated at 35°C. After 1.5 hr, D-cycloserme (100 mg liter ) was added and the incubation continued for 4 hours. After 4 h, CFU/ml had dropped by over 95%. Clones harboring putative genes for decreased ethanol tolerance were isolated from these plates .
DNA Sequencing and Sequence Analysis
The QIAprep spin plasmid kit (Qiagen, Chatsworth, CA) was used for plasmid purification. Dideoxy sequencmg was performed using fluorescent primers [forward, 5 ' CACGACGTTGTAAAACGAC-3 ' (SEQ ID N0:1); reverse, 5 ' -ATAACAATTTCACACAGGA-3 ' (SEQ ID NO : 2 ) ] (LI -COR, Lincoln, NE) . Extension reactions were performed with a Perkm Elmer GeneAmp PCR System 9600 (Norwalk, CT) using an Excel Sequencing Kit-LC (Epicentre Technologies, Madison, WI) (30 cycles; denaturation for 30 sec at 95°C, annealing for 30 sec at 60°C, and extension for 1 mm at 70°C) . Extension products were separated and read with a LI -COR DNA Sequencer model 4000L.
Sequences were analyzed using the Wisconsin Genetics Computer Group (GCG) software package and the National Center for Biotechnology Information BLAST network service.
Analytical Procedures
Cell density was measured using a Bausch & Lomb Spectromc 70 spectrophotometer and converted to dry cell weight based on a standard curve for this organism. Ethanol was measured by gas chromatography with n-propanol as an internal standard (Beall et al . , 1991) using a Vaπan Star 3400 CX gas chromatograph.
EXAMPLE 1 - Isolation of Ethanol-tolerant Mutants of E. Coli KOll Using the materials and procedures outlined above, a total of 135 colonies were initially tested for growth m 4.5% (w/w) ethanol, a concentration at which the parental KOll failed to grow. Forty three colonies were turbid after 24 h incubation at 35°C and were saved for further testing.
Stability of the ethanol resistance trait was examined by retestmg clones which had been stored frozen at -75°C and clones which had been maintained on solid medium lacking ethanol.
EXAMPLE 2 - Testing Mutants of E . Coli KOll for Ethanol Tolerance
As shown m Figure 1A, after 24 h, the mutants were much more resistant to ethanol than the parent KOll. Figure 2B, Figure 2D, and Table 1A and IB compare initial growth upon dilution into media containing various concentrations of ethanol . In the absence of ethanol, KOll appeared to grow slightly better than the mutants both with glucose and with xylose as the fermentable sugar as shown m Figures 2A and 2C. However, KOll was unable to grow m 3.5% (w/w) ethanol while all mutants grew m ethanol concentrations of up to 5% (w/w) . Ethanol tolerance was also compared using other fermentable sugars which may be of interest for fuel ethanol production: lactose, arabmose, and mannose, galactose, sucrose and raffmose. KOll growth was consistently above that of the mutants m the absence of ethanol. However, KOll failed to grow m ethanol concentrations above 3% (w/w) while the mutants grew in 5% ethanol with all sugars tested.
Next, cell survival during exposure to 10% ethanol was examined (Figure IB) . All mutants tested were more resistant than KOll. This difference was particularly dramatic for 0.5 mm exposure where 63-84% of the mutants retained colony forming ability while less than 10% of KOll survived.
The stability of the ethanol -tolerance trait was also examined. LYOl, LY02 , LY03 , and LY04 were transferred daily on solid medium lacking alcohol for 30 days. Cells were then used to inoculate broth cultures containing ethanol as shown m Figures 2C and 2D. The resulting growth curves were identical to those initially determined. The retention of osmotic tolerance to sugars is essential for the utility of ethanol-tolerant mutants of KOll. As illustrated m Figures 3A and 3B, tolerance to xylose and glucose are similar on a molar basis. With both sugars, KOll appeared more resistant to osmotic stress than the ethanol -resistant mutants, although this difference was not dramatic. No differences were observed m growth at 48°C, the maximum temperature for growth. Both KOll and the mutants grew slowly at this temperature .
TABLE 1A Fermentation of 14% glucose to ethanol
t
Figure imgf000024_0001
TABLE 1A Fermentation of 14% glucose to ethanol (Continued)
t
Figure imgf000025_0001
Figure imgf000025_0002
TABLE 1A Fermentation of 14% glucose to ethanol (Continued)
Figure imgf000026_0001
t
Cell dry weight, ± s.d.
Corrected for dilution by base
The theoretical yield is 0.51 g ethanol/g glucose.
TABLE IB Fermentation of 14% xylose to ethanol
Figure imgf000027_0001
Cell dry weight, ± s.d.
Corrected for dilution by base
The theoretical yield is 0.51 g ethanol/g xylose.
EXAMPLE 3 - Fermentation of Sugars to Ethanol
Twenty of the most promising mutants were screened for their ability to produce ethanol from 14% glucose (Figure 4A and Table 2) and 14% xylose (Figure 4B and Table 2) m pH-controlled fermenters . All were superior to the parent strain KOll m their ability to produce ethanol more rapidly and m their ability to achieve higher final ethanol concentrations. All mutants were also superior to the parent strain KOll m their ability to achieve higher yields. Mutants LYOl, LY02 , LY03 , and LY04 were examined m more detail to establish the variability testing. With all mutants, the cell mass produced during the fermentation of glucose or xylose was consistently higher than that produced by KOll. Base consumed for the neutralization of small amounts of organic acids and dissolved C02 was higher for glucose than for xylose due to the higher rate for fermentation. Roughly equivalent amounts of KOH were required to maintain pH 6.0 for both KOll and the mutants. Addition of base resulted a small dilution of product. Ethanol values m Table 2 are corrected for this dilution (ethanol produced = measured ethanol *(1000+ 1/2 mM KOH/1000) ) to allow the estimation of ethanol yield. After 96 h, the ethanol yield for KOll with 14% sugar was 74% and 80% of the theoretical maximum (0.51 g ethanol per gram of pentose or hexose) for glucose and xylose, respectively. Strain LYOl was among the best of the mutants tested. This strain achieved 85% of the maximum theoretical yield from glucose and xylose after 72 h and reached a final ethanol concentration of almost 60 g liter1 (7.5% ethanol by volume) . TABLE 2
Figure imgf000029_0001
EX7AMPLE 4 - Isolation of Plasmids Containing Native Genes from KOll Which Decrease Ethanol Tolerance
After D-cycloserine enrichment for survivors which fail to grow at 3.5% ethanol, a total of 32 recombinants of LY02 and 40 recombinants of LY03 were screened in triplicate for growth in Luria broth containing 5% glucose and 4% ethanol. All grew to a lower density after 24 h than the original mutant. Six replicates of the most promising 19 clones were compared simultaneously. Four clones which uniformly resulted in a decrease in ethanol tolerance as compared to LY02(pUC18) were selected for further study. EX7AMPLE 5 - Identification of Genes Which Reduce Ethanol Tolerance
Sequence analysis of the ends of the inserts m the four selected plasmids revealed that they consisted of two pairs of siblings. The entire E. coli genome is now available m the GenBank database. The cloned fragments were readily identified by using the terminal sequences and BLAST network server.
Plasmid pLOI1531 contains a 3.6 kbp fragment of KOll DNA within the 67.4 mm-76.0 mm region of the E . coli chromosome (GenBank Accession Number U18997) . Subclones were prepared and sequenced to confirm gene arrangement m KOll and to identify the genes which are responsible for a decrease m ethanol tolerance (Figure 5) . Only 2 open reading frames were present: crp and a large open reading frame of unidentified function (ORF 0696). A comparison of the effects of pUC18, pLOI1531 and deleted clones (pL0I1532 and pL0I1533) on LY03 indicated that the crp gene (cyclic AMP receptor protein) was responsible for the decrease m ethanol tolerance . pL0I1534 contains a 7.39 kbp fragment of KOll DNA within the 89.2 mm -92.8 mm segment (Accession Number U00006 of the E. coli chromosome (Figure 6) . Deleted derivatives of this clone were also sequenced to confirm gene arrangement and revealed the presence of 3 complete and 2 partial open reading frames: dnaB ' , air, tyrB, napA (hobH) , and uvrA ' . A comparison of deleted derivatives identified the air gene (biosynthetic alanme racemase) as being responsible for decreasing the ethanol tolerance of LY02. SEQUENCE LISTING
(1) GENERAL INFORMATION:
(i) APPLICANT: University of Florida Research Foundation Incorporated
(ii) TITLE OF INVENTION: Development of High-Ethanol Resistant Escherichia Coli
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AT ACAATTT CACACAGGA 19 EQUIVALENTS
While this invention has been particularly shown and described with references to preferred embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims. Those skilled in the art will recognize or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described specifically herein. Such equivalents are intended to be encompassed in the scope of the claims .

Claims

CLAIMSWhat is claimed is:
1. An ethanologenic microorganism comprising one or more nucleic acid molecules which encode alcohol dehydrogenase and pyruvate decarboxylase; wherein said bacterium does not express active cyclic AMP receptor protein, active biosynthetic alanine racemase or both.
2. The ethanologenic microorganism according to Claim 1, wherein said microorganism is a bacterium selected from the group consisting of Erwinia, Klebsiella, Xanthomonas and Escherichia.
3. The ethanologenic bacterium according to Claim 2, wherein said bacterium is Klebsi ella oxytoca .
4. The ethanologenic bacteria according to Claim 2, wherein said bacterium is Escheri chia coli .
5. The ethanologenic bacteria according to Claim 2 wherein said bacterium comprises a heterologous nucleic acid molecule which encodes Zymomonas alcohol dehydrogenase and pyruvate decarboxylase.
6. The ethanologenic bacterium according to Claim 5 wherein said Zymomonas alcohol dehydrogenase and pyruvate decarboxylase are encoded by a nucleic acid molecule isolated from Zymomonas mobilis .
7. An ethanologenic Escherichia coli which comprises a heterologous nucleic acid molecule isolated from Zymomonas mobili s which encodes alcohol dehydrogenase and pyruvate decarboxylase, wherein said bacterium does not express active cyclic AMP receptor protein, active biosynthetic alanme racemase or both.
8. An ethanologenic microorganism produced by the process comprising the steps of: (a) contacting an ethanologenic microorganism with a first liquid medium comprising an aqueous solution comprising ethanol, selecting one or more microorganisms that survive;
(b) contacting one or more microorganisms obtained from step (a) with a solid growth medium for a sufficient period of time to permit growth;
(c) contacting one or more microorganisms obtained from step (b) with a second liquid medium comprising an aqueous solution comprising an amount of ethanol greater than present m said first liquid medium, selecting one or more microorganisms that survive; and
(d) contacting one or more microorganisms obtained from step (c) with a solid growth medium for a sufficient period of time to permit growth.
9. The ethanologenic microorganism according to Claim 8 wherein said microorganism is a bacterium.
10. The ethanologenic microorganism according to Claim '
9, wherein said microorganism is selected from the group consisting of Erwinia, Klebsiella, Xanthomonas and Escherichia.
11. The ethanologenic microorganism according to Claim
10, wherein said microorganism is Klebsi ella oxytoca .
12. The ethanologenic microorganism according to Claim 10, wherein said microorganism is Escheri chia coli .
13. The ethanologenic microorganism according to Claim 10, wherein said microorganism comprises a heterologous nucleic acid molecule which encodes Zymomonas alcohol dehydrogenase and pyruvate decarboxylase .
14. The ethanologenic microorganism according to Claim 13, wherein said Zymomonas alcohol dehydrogenase and pyruvate decarboxylase are encoded by a nucleic acid molecule isolated from Zymomonas mobilis .
15. A method for producing an ethanologenic microorganism mutant comprising:
(a) contacting an ethanologenic microorganism with a first liquid medium comprising an aqueous solution comprising ethanol, selecting one or more microorganisms that survive; (b) contacting one or more microorganisms obtained from step (a) with a solid growth medium for a sufficient period of time to permit growth; (c) contacting one or more microorganisms obtained from step (b) with a second liquid medium comprising an aqueous solution comprising an amount of ethanol greater than present in said first liquid medium, selecting one or more microorganisms that survive; and
(d) contacting one or more microorganisms obtained from step (c) with a solid growth medium for a sufficient period of time to permit growth.
16. The method according to Claim 15 wherein said microorganism is a bacterium.
17. The method according to Claim 16, wherein said microorganism is selected from the group consisting of Erwinia, Klebsiella, Xanthomonas and Escherichia.
18. The method according to Claim 17, wherein said microorganism is Klebsiella oxytoca .
19. The method according to Claim 17, wherein said microorganism is Escherichia coli .
20. The method according to Claim 17, wherein said microorganism comprises a heterologous nucleic acid molecule which encodes Zymomonas alcohol dehydrogenase and pyruvate decarboxylase.
21. The method according to Claim 20 wherein said Zymomonas alcohol dehydrogenase and pyruvate decarboxylase are encoded by a nucleic acid molecule isolated from Zymomonas mobilis .
22. The method according to Claim 15, wherein said solid medium contains an antibiotic and a fermentable sugar.
23. The method according to Claim 22, wherein said antibiotic is selected from the group consisting of chloramphenicol, tetracyclme and ampicillm.
24. The method according to Claim 15, wherein said first liquid medium, said second liquid medium or both further comprise a sugar.
25. The method according to Claim 24, wherein said first liquid medium, said second liquid medium or both comprise at least about 3.5% (by weight) ethanol .
26. The method according to Claim 25, wherein said second liquid medium comprises at least about 4%
(by weight) ethanol.
27. The method according to Claim 26, further comprising steps
(e) contacting one or more microorganism obtained from step (d) with a third liquid medium comprising an aqueous solution comprising an amount of ethanol greater than present m said second liquid medium, selecting one or more microorganisms that survive; and (f) contacting one or more microorganisms obtained from step (e) with a solid growth medium for a sufficient period of time to permit growth.
28. The method according to Claim 15, wherein said ethanologenic microorganism mutant can grow in ethanol concentrations of greater than 35 g L"1.
29. The method according to Claim 15, wherein said ethanologenic microorganism mutant can produce at least 10% more ethanol than Escherichia coli KOll under equivalent fermentation conditions.
PCT/US1998/006405 1997-04-07 1998-03-31 DEVELOPMENT OF HIGH-ETHANOL RESISTANT $i(ESCHERICHIA COLI) WO1998045425A1 (en)

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CA002286334A CA2286334A1 (en) 1997-04-07 1998-03-31 Development of high-ethanol resistant escherichia coli
AU68752/98A AU6875298A (en) 1997-04-07 1998-03-31 Development of high-ethanol resistant (escherichia coli)
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US7947577B2 (en) * 2006-09-08 2011-05-24 Tokuyama Corporation Method and apparatus for producing group III nitride
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