JP6026494B2 - Use of sucrose as a substrate for the fermentation production of 1,2-propanediol - Google Patents

Description

Background of the Invention

  The present invention relates to a fermentation method, microorganisms and substrates useful for fermentation. In particular, the present invention relates to the production of 1,2-propanediol by fermentation from sucrose-containing media, particularly plant biomass.

  C3-dialcohol, 1,2-propanediol or propylene glycol, is a widely used chemical. This is a component of unsaturated polyester resins, liquid detergents, coolants, antifreezes and aircraft slow ice. Propylene glycol has increased use since 1993-1994 as an alternative to ethylene derivatives that are recognized as being more toxic than propylene derivatives.

  1,2-propanediol is currently produced by chemical means using a propylene oxide hydration method that consumes large amounts of water. Propylene oxide can be prepared by either of two methods, one using epichlorohydrin and the other using hydroperoxide. Both routes use highly toxic substances. In addition, the hydroperoxide pathway yields by-products such as tert-butanol and 1-phenylethanol. In order to favor the production of propylene, the use of these by-products must be found. This chemical route generally produces racemic 1,2-propanediol, but the two stereoisomers (R) 1,2-propanediol and (S) 1,2-propanediol, respectively, Of note are applications (eg, chiral starting materials for specialty chemicals and pharmaceuticals).

In view of the shortcomings of the prior art chemical processes for the production of these 1,2-propanediols, biosynthesis is an attractive option. Two pathways have been identified for the natural production of 1,2-propanediol from sugars by microorganisms. In the first route, a 6-deoxy sugar (eg, L-rhamnose or L-fucose) is cleaved to dihydroxyacetone phosphate and (S) -lactoaldehyde, and further to (S) -1,2-propanediol. (Badia et al, 1985). Although this pathway functions in E. coli, the high cost of deoxyhexose cannot provide an economically feasible method. The second pathway is the metabolism of a general sugar (eg glucose or xylose) via the glycolysis pathway followed by the methylglyoxal pathway. Dihydroxyacetone phosphate is converted to methylglyoxal, which can be reduced to either lactaldehyde or acetol. These two compounds can then undergo a second reduction reaction to yield 1,2-propanediol. This pathway has been used by natural (R) -1,2-propanediol producers such as Clostridium sphenoides and Thermoanaerobacter thermosaccharolyticum. These two microorganisms are different saccharides, ie monosaccharides (D-glucose, D-mannose, D-galactose for hexose and D-xylose or L-arabinose for pentose) or disaccharide (Lactose or cellobiose) or mixtures to make 1,2-propanediol (Tran Din and Gottschalk, 1985, Cameron and Cooney, 1986, Sanchez-Rivera et al, 1987, Altaras et al, 2001 ). The highest performance obtained was a titer of 9 g / l and the yield from glucose was 0.2 g / g (Sanchez-Rivera et al, 1987). However, the performance improvements obtained with these organisms appear to be limited due to the lack of available genetic tools. Several studies on the production of 1,2-propanediol using carbon sources limited to D-glucose or D-fructose in which the same synthetic pathway is functional in E. coli or other Enterobacteriaceae Were made by Cameron's group (Cameron et al, 1998, Altaras and Cameron, 1999, Altaras and Cameron, 2000) and Bennett's group (Huang et al, 1999, Berrios-Rivera et al, 2003). The best results obtained in an anaerobic fed-batch fermenter were 1,2-propanediol production of 4.5 g / l and a yield from glucose of 0.19 g / g (Altaras and Cameron , 2000). Although obtained with the same approach, lower titers and yields are also described in patent WO 98/37204, but with different carbon sources, ie galactose, lactose, sucrose and xylose. Nonetheless, glucose was also used. The titers obtained with disaccharides (lactose and sucrose) were very low (6 mg / l and 7 mg / l, respectively). Patent application WO2005 / 073364 describes better production results using rationally designed and evolved E. coli strains. A 1,2-propanediol titer of 1.8 g / l was obtained and the yield was 0.35 g / g of glucose consumed. Patent WO99 / 28481 describes the production of 1,2-propanediol and hydroxyacetone using recombinant yeast.

  The carbon source used in the fermentation medium generally consisted of carbohydrates, most often plant-derived carbohydrates. Sucrose is obtained from sugar plants such as sugar beet, sugar cane, sugar corn, sugar maple, sugar palm or blue agave. Starch is the most abundant stored carbohydrate in plants. The most important starch sources are cereals (corn, wheat, rice), cassava, sweet potato and potato. Starch is not metabolized by most microorganisms, but can be processed into fermentable raw materials by the starch industry. Insulin or insulin-like polymers (consisting mainly of fructose units) are the second most stored carbohydrate in plants and are found in chicory, quill or dahlia. Lignocellulose biomass consisting of cellulose, hemicellulose and lignin is also a promising carbohydrate source but is still under development (Peters, 2006). Since the cost of daily chemical products produced by biotechnology is primarily related to the cost of the raw material (ie, the cost of the fermentation substrate), the cost of using purified sugars such as glucose or sucrose is the cost of manufacturing on an industrial scale. It is not an economically sustainable option. There is a need for an ineffective substrate that retains a high content of fermentable sugar. In this regard, a sucrose-containing carbon source from the refined sugar industry is a good choice.

  Sucrose is produced from sugar beet containing 16-24% sucrose by several stages of sugar beet processing. The cleaned and washed beets are sliced into strips called cossettes and extracted by diffusion with hot water to obtain sucrose juice, called raw fruit juice, containing 10-15% sucrose. The second step is the purification of the raw fruit juice by alkalinization and carbonation saturation with lime and then carbon dioxide to remove impurities and obtain a diluted fruit juice. By removing water during the evaporation process, the sucrose concentration in the diluted fruit juice is increased, and a concentrated fruit juice having a sucrose content of 50 to 65% is obtained. This concentrated sucrose juice is then crystallized, the crystals separated by centrifugation, washed and dried to obtain pure sugar. One or more crystallization steps can be applied to obtain sucrose of varying purity. Sugar beet processing by-products include pulp (waste coset) and molasses (residual mother liquor from crystallization, still having a sucrose content of 40-60%).

  Sucrose is also produced by the sugar industry from sugarcane (sucrose content 7-20%). After the harvested sugarcane is cleaned, a crushing process for extracting juice is performed. After destroying the structure of sugarcane, it is pulverized and at the same time, sucrose is extracted with water to obtain raw fruit juice. The remaining crushed sugarcane from which the sugar has been removed is called bagasse. This residue is mainly used as a fuel source for producing process steam. Next, this raw fruit juice is clarified by adding lime and heating, and the clarified fruit juice is separated from the precipitate. The evaporation and crystallization to obtain the concentrated syrup, the final step of this process, is essentially the same as in the sugar beet process. Sugar cane processing by-products include bagasse, filter cake from clarification of raw fruit juice and various molasses, but still contain substantial amounts of sucrose.

  Various sucrose-containing intermediates, products or by-products from the refined sugar process (raw juice, dilute or clarified juice, concentrated juice, sucrose syrup, pure sucrose, molasses) can serve as fermentation raw materials. For example, the refined sugar industry in Brazil uses clarified sugarcane juice for ethanol production for use as an alternative to gasoline. Recent examples in the literature using unpurified sucrose-containing products include ethanol production from sugar beet diffusion juice by Zymomonas mobilis (Beckers et al., 1999), D-lactic acid from molasses by E. coli. Production (Shukla et al., 2004) and production of D-lactic acid from sugar cane molasses, sugar cane juice or sugar beet juice (Calabia et al., 2007) by Lactobacillus delbrueckii.

  Two different systems have been identified for sucrose uptake and utilization in sucrose positive bacteria (ie, sucrose accessible bacteria).

  The first is a phosphoenolpyruvate (PEP) -dependent sucrose phosphotransferase that takes up and phosphorylates sucrose using phosphoenolpyruvate (PEP) as a donor to produce intracellular sucrose-6-phosphate. Based on the system (sucrose PTS). Sucrose-6-phosphate is then hydrolyzed by invertase to D-glucose-6-phosphate and D-fructose. D-fructose can enter the central metabolism after further phosphorylation of ATP-dependent fructokinase to D-fructose-6-phosphate. Such systems have been described with several gram positive as well as gram negative bacterial species. Within the Enterobacteriaceae, more than 90% are wild-type Klebsiella, less than 50% are Escherichia, and less than 10% are Salmonella strains are sucrose-positive.

  A conjugative plasmid pUR400 carrying the gene scrKYABR encoding sucrose PTS has been isolated from the genus Salmonella (Schmid et al., 1982, Schmid et al, 1988).

  More recently, a second non-PTS system was discovered in E. coli EC3132 (Bockmann et al., 1992). This system includes the gene cscBKAR, which encodes a sucrose: proton cotransport system (CscB), fructokinase (CscK), invertase (CscA) and a sucrose-specific repressor (CscR).

  Escherichia coli K12 and its derivatives (including MG1655) cannot utilize sucrose. However, this ability can be conferred by the introduction of genes encoding the two systems described previously. This is due to the introduction of plasmid pUR400 in E. coli K12 (Schmid et al. 1982) or the introduction of various plasmids (including pKJL101-1) carrying the cscBKAR gene in a sucrose negative strain of E. coli (Jahreis et al., 2002). It has been proven by For industrial use, tryptophan production from sucrose has been reported in E. coli K12 (Tsunekawa et al., 1992), hydrogen production has been demonstrated in E. coli carrying the pUR400 plasmid (Penfold and Macaskie, 2004), and patent application EP1149911. Thus, the production of various amino acids by introduction of PTS and non-PTS quantitative systems has been reported.

  The production of 1,2-propanediol from sucrose is described by Cameron and Cooney (1986) in Clostridium thermosaccharolyticum (hereinafter referred to as T. thermosaccharolyticum), but a trace amount is recorded. On the other hand, with other carbon sources, amounts higher than 3 g / l were obtained and the yield was 0.1 g / g (substrate).

  The production of 1,2-propanediol from sucrose is also described in patent application WO 98/37204. However, E. coli strain AA200 transformed with plasmid pSEARX produces only 7 mg / l 1,2-propanediol from 10 g / l sucrose, whereas the same microorganism is 49-71 mg / l from monosaccharides. l of 1,2-propanediol. From these extremely low production figures, the ability of these microorganisms to produce 1,2-propanediol from sucrose is questionable. In our view, the AA200 strain derived from E. coli K12 does not have the ability to transport and metabolize sucrose.

  These past reports clearly indicate to those skilled in the art that the use of sucrose to produce 1,2-propanediol is not a good option.

  Surprisingly, by introducing various systems for sucrose utilization into E. coli strains where sucrose is not available, we can obtain high yields for the production of 1,2-propanediol from sucrose. did it.

  In addition, the inventors have demonstrated that sucrose-containing media such as fruit juice or molasses from plant materials can be used as a fermentable acid substrate for 1,2-propanediol.

The present invention is a method for producing 1,2-propanediol by fermentation,
Culturing a microorganism producing 1,2-propanediol in a suitable medium comprising a source of sucrose, and recovering the produced 1,2-propanediol, wherein the microorganism comprises , Sucrose as a sole carbon source for the production of 1,2-propanediol.

  In particular, the present invention discloses the use of a modified microorganism that can utilize sucrose as the sole carbon source, which is obtained from biomass, particularly plant biomass.

Detailed description of the invention

  In this specification, the following terms can be used for interpretation of a claim and a specification.

  According to the present invention, “cultivatin”, “culture”, “growth” and “fermentation” are intended to represent the growth of bacteria in a suitable growth medium containing a simple carbon source. Used interchangeably. Fermentation is a conventional process that can be performed under aerobic, microaerobic or anaerobic conditions.

  According to the present invention, “appropriate medium” refers to a medium of known molar composition adapted to the growth of microorganisms. In particular, the medium contains at least a phosphorus source and a nitrogen source. The suitable medium is, for example, an inorganic culture medium of a known set of compositions that contains at least one carbon source and is adapted to the bacteria used. The suitable medium also represents any liquid comprising a nitrogen source and / or a phosphorus source, which is added to and / or mixed with a source of sucrose. Thus, in particular, inorganic growth media for Enterobacteriaceae are media such as those defined by M9 media (Anderson, 1946), M63 media (Miller, 1992) or Schaefer et al. (1999), in particular It can be of the same or similar composition as the minimal culture medium called MML11PG1_100 below.

  The pH of the medium is adjusted to 6.8 with sodium hydroxide.

  The carbon source “glucose” in this medium can be replaced by any other carbon source, in particular any sucrose-containing carbon source such as sucrose or sugar cane juice or sugar beet juice.

  The growth medium for the Clostridial family is the same or similar to the Clostridial growth medium (CGM, Wiesenborn et al., 1987) or the inorganic growth medium shown by Monot et al. (1982) or Vasconcelos et al. (1994). Can be of the following composition.

“Sucrose” refers to a disaccharide of glucose and fructose linked by α (1,2) glycosidic bonds having the molecular formula C ₁₂ H ₂₂ O ₁₁ . Its tissue name is α-D-glucopyranosyl- (1 ← → 2) -β-D-fructofuranoside.

  “Sucrose source” or “source of sucrose” refers to any medium, liquid or solid containing various concentrations of sucrose, in particular 1-100% sucrose.

  “Preparing 1,2-propanediol” means that the production of the microorganism in the culture can be clearly recorded by standard analytical means known to those skilled in the art. The quantification limit for 1,2-propanediol by HPLC, the preferred technique used for quantification of this compound, is 25 mg / l. Thus, according to the present invention, “manufacturing 1,2-propanediol” means that the production level must exceed 25 mg / l.

  “Sucrose can be used as the sole carbon source” indicates that the microorganism can grow on a medium containing a unique carbon source and sucrose. Therefore, “a microorganism that can utilize sucrose as the sole carbon source for the production of 1,2-propanediol” means that the microorganism is grown in a medium containing sucrose as the sole carbon source. Meaning that at least 25 mg / l of 1,2-propanediol can be produced. However, in the method for producing 1,2-propanediol according to the present invention, the source of sucrose in the culture medium is not only sucrose but also hexose sugars (such as glucose, galactose or lactose), pentose sugars, monosaccharides, disaccharides ( It is understood that additional carbon sources such as sucrose, cellobiose or maltose), oligosaccharides, starch or derivatives thereof, hemicellulose, glycerol and combinations thereof may be included.

  According to a preferred embodiment of the invention, the microorganism has been genetically modified so that sucrose can be utilized as the sole carbon source for the production of 1,2-propanediol.

  In certain embodiments of the invention, the microorganism comprises a functional gene encoding a PTS sucrose utilization system. The PTS sucrose utilization system is a system for sucrose utilization based on the transport of sucrose by the phosphoenolpyruvate (PEP) -dependent sucrose phosphotransferase system (sucrose-PTS). This phosphotransferase system couples the transport of sugars (eg sucrose or glucose) and the phosphorylation of sugars using PEP as a phosphate donor. After being transported into the cell, sucrose-phosphate is cleaved to glucose-6-phosphate and fructose by invertase. Thereafter, fructose is phosphorylated by fructokinase to become fructose-6-phosphate. The gene encoding this PTS sucrose utilization system can be controlled by a regulatory protein.

  In a preferred embodiment of the present invention, the microorganism is a gene derived from the genus Salmonella: scrKYABR (scrK encoding fructokinase, scrY encoding porin, scrA encoding protein IIBC, scrB encoding sucrose-6-P invertase, ScrK) which encodes the repressor is naturally expressed or modified by introduction of these genes. Microorganisms can be transformed with the conjugative plasmid pUR400 carrying the gene scrKYABR. All of these genes can be used in combination together or in any combination comprising at least one of these genes. In particular, the gene scrK can be omitted.

  According to the present invention, these gene designations have a more general meaning and include the corresponding genes of other microorganisms. One skilled in the art can identify equivalent genes in microorganisms other than Salmonella using the GenBank reference numbers of these genes from Salmonella.

  Means for identifying homologous sequences and% homology are well known to those skilled in the art, and in particular the defaults indicated on the website at http://www.ncbi.nlm.nih.gov/BLAST/ BLAST programs that can be used with parameters. The resulting sequence can be utilized (aligned) using, for example, the program CLUSTALW (http://www.ebi.ac.uk/clustalw/) with the default parameters shown on these websites. it can.

  The PFAM database (protein families database of alignments and hidden Markov models http://www.sanger.ac.uk/Software/Pfam/) is a large collection of protein sequence alignments. Each PFAM can display multiple alignments, visually recognize protein domains, assess distribution in organisms, access other databases, and display known protein structures.

  COG (clusters of orthologous groups of proteins http://www.ncbi.nlm.nih.gov/COG/) is derived from 66 fully sequenced single cell genomes representing 14 major phylogenetic strains Obtained by comparing protein sequences. Each COG is defined from at least three strains, which makes it possible to identify an old conserved domain.

  Several techniques have been used by those skilled in the art to introduce DNA into bacterial strains. A preferred technique is electroporation, which is well known to those skilled in the art.

In another embodiment of the invention, the microorganism comprises a functional gene encoding a non-PTS sucrose utilization system. A non-PTS sucrose utilization system is a system for sucrose utilization based on sucrose transport by a system independent of phosphoenolpyruvate. After being transported into the cell, sucrose is cleaved into glucose and fructose by invertase.
Thereafter, fructose is phosphorylated by fructokinase to become fructose-6-phosphate, and glucose is phosphorylated by glucokinase to become glucose-6-phosphate. The gene encoding this non-PTS sucrose utilization system can be controlled by a regulatory protein. In a preferred embodiment of the present invention, the microorganism encodes genes from E. coli EC3132, ie sucrose: proton cotransport system (cscB), fructokinase (cscK), invertase (cscA) and sucrose-specific repressor (cscR). The gene cscBKAR to be expressed is naturally expressed or modified by introduction of these genes. All of these genes can be used in combination together or in any combination comprising at least one of these genes. In particular, the gene cscR can be omitted. In addition, homologous genes derived from other organisms can be used.

  According to the present invention, these gene designations have a more general meaning and include the corresponding genes of other microorganisms. One skilled in the art can identify equivalent genes in microorganisms other than E. coli using the GenBank reference numbers of these genes from E. coli.

  In a particular embodiment of the invention, the microorganism is characterized by an improved activity of the 1,2-propanediol biosynthetic pathway. Microorganisms optimized for the production of 1,2-propanediol are described in patent applications WO2005 / 073364, WO2008 / 116853, WO2008 / 116852 and WO2008 / 116848, which are hereby incorporated by reference. It is disclosed comprehensively.

  The microorganism according to the present invention is a bacterium, yeast or fungus.

  Preferably, the microorganism is selected from the group consisting of Enterobacteriaceae, Bacillus, Clostridium, Streptomyces and Corynebacteriaceae.

  More preferably, the microorganism is Escherichia coli, Klebsiella pneumonia, Thermoanaerobacter thermosaccharolyticum, Clostridium sphenoides or Saccharomyces cerevisiae S. Selected from the group.

  The culture conditions for the fermentation process can be easily defined by those skilled in the art. In particular, the bacteria are fermented at a temperature between 20 ° C. and 55 ° C., preferably between 25 ° C. and 40 ° C., preferably about 35 ° C. for Clostridium and about 37 ° C. for Enterobacteriaceae.

  This process can be carried out either batchwise, fed-batch or continuous. Fermentation is a conventional process that can be performed under aerobic, microaerobic or anaerobic conditions.

  “Aerobic conditions” means supplying oxygen to the culture by dissolving gas in the liquid phase. This can be done by (1) sparging an oxygen-containing gas (eg, air) in the liquid phase, or (2) shaking the container containing the culture medium to transfer the oxygen contained in the headspace to the liquid phase. can get. The advantage of fermenting under aerobic conditions instead of anaerobic conditions is that the presence of oxygen as an electron acceptor increases the ability of the strain to produce more energy in the form of ATP for cellular processes. That is.

  Microaerobic conditions are defined as culture conditions that dissolve a low percentage of oxygen (eg, using a mixture containing between 0.1-10% oxygen and 100% nitrogen) in the liquid phase. .

  Anaerobic conditions are defined as culture conditions in which oxygen is not supplied to the culture medium. Strictly speaking, anaerobic conditions are obtained by sprinkling an inert gas such as nitrogen over the culture medium to remove traces of other gases. Nitrate can be used as an electron acceptor to increase ATP production by the strain and increase its metabolism.

  In a particular embodiment of the invention, the sucrose source is obtained from biomass, in particular plant biomass. The raw material used as a sucrose source can be prepared using the whole plant or any specific part of the plant. This preparation may be based on any treatment known to those skilled in the art for extracting sucrose from sucrose-containing plant biomass.

  In a preferred embodiment of the invention, the sucrose source is obtained from a plant selected from the group consisting of sugarcane, sugar beet, sweet corn, sugar maple, sugar palm and blue agave.

  The source of sucrose can be obtained in particular from sugar cane or sugar beet.

  According to the present invention, various forms of sucrose sources such as fruit juice, concentrated fruit juice, syrup, clarified fruit juice, molasses or crystallized sucrose can be used.

  A preferred form is raw sugar juice derived from sugarcane extracted directly from plants without any treatment. In short, harvested sugarcane is cleaned and then ground for fruit juice extraction. After destroying the structure of sugarcane, it is pulverized and at the same time, sucrose is extracted with water to obtain raw fruit juice.

  This original fruit juice is clarified by adding lime and heating, and the clarified fruit juice is separated from the precipitate. Evaporation gives a concentrated syrup.

  In another embodiment of the present invention, the sucrose source may be a sugarcane or sugar beet industry end product, intermediate product or by-product.

  Some crude sucrose sources, particularly those obtained from biomass as described above, contain other nutrients that can be used for microbial growth in addition to the carbon source, and suitable media for microbial growth are sucrose sources Or by supplementing the sucrose source with a phosphorus source and / or nitrogen source.

  Preferably, the sucrose source comprises at least 7% sucrose.

Example 1: Construction of two E. coli strains that produce 1,2-propanediol and can use sucrose as the only carbon source E. coli strains MG1655 lpd ^* , ΔtpiA, ΔpflAB, ΔadhE, ΔldhA :: Cm, ΔgloA, ΔaldA, ΔaldB, Δedd were evolved in chemostat culture under anaerobic conditions and adapted for growth on minimal medium as described in WO2008 / 116852. This strain was called the evolutionary strain E. coli MG1655 lpd ^* , ΔtpiA, ΔpflAB, ΔadhE, ΔldhA :: Cm, ΔgloA, ΔaldA, ΔaldB, Δedd.

  The chloramphenicol resistance cassette was removed from the evolved strain and the presence of the modifications previously constructed in this strain was confirmed as previously described in accordance with WO 2008/116852.

Two plasmids were used to confer sucrose utilization on the E. coli strain.
PUR400 carrying a gene encoding the sucrose-PTS system such as that described in Schmid et al. (1982)
PKJL101.1 carrying genes encoding sucrose permease and kinase systems such as those described in Jahreis et al. (2002)

These plasmids were respectively introduced into Escherichia coli strains MG1655 lpd ^* , ΔtpiA, ΔpflAB, ΔadhE, ΔldhA, ΔgloA, ΔaldA, ΔaldB, Δedd evolved by electroporation.

The obtained two strains, respectively, evolved E. coli ^{MG1655 lpd *, ΔtpiA, ΔpflAB,} ΔadhE, ΔldhA, ΔgloA, ΔaldA, ΔaldB, Δedd (pUR400) and - evolved E. coli ^{MG1655 lpd *, ΔtpiA, ΔpflAB,} ΔadhE, ΔldhA , ΔgloA, ΔaldA, ΔaldB, Δedd (pKJL101.1)
I called it.

Example 2: Preparation of 1,2-propanediol using sucrose as the sole carbon source . The strain obtained as described in Example 1 and the strain without plasmid used as a control were placed in an Erlenmeyer flask. The assay was cultured in a minimal medium MML11PG1_100 (see composition above) containing 20 g / l glucose or sucrose as the sole carbon source under aerobic conditions. Glucose as a carbon source was used as a control.

  The culture was carried out at 34 ° C., and the pH was maintained by buffering the culture medium with MOPS.

  At the end of the culture, 1,2-propanediol and glucose or sucrose remaining in the fermentation broth are analyzed by HPLC, and the yield of 1,2-propanediol relative to glucose or the yield of 1,2-propanediol relative to sucrose Was calculated.

Example 3: Production of 1,2-propanediol using sugar cane juice as a carbon source A strain obtained as described in Example 1 was subjected to carbon in an Erlenmeyer flask assay under aerobic conditions. It was cultured in minimal medium MML11PG1_100 containing sugarcane juice (20 g / l sucrose equivalent) as a source.

  The sugarcane juice used in this experiment was obtained from a refinery in Southeast Asia and was collected immediately after clarification of the original juice with lime.

  The culture was carried out at 34 ° C., and the pH was maintained by buffering the culture medium with MOPS. At the end of the culture, 1,2-propanediol and sucrose, glucose and fructose remaining in the fermentation broth were analyzed by HPLC to calculate the yield of 1,2-propanediol relative to the total carbon source.

Example 4: Production of 1,2-propanediol using sugarcane juice alone or sugarcane juice supplemented with nutrients . The strain obtained as described in Example 1 was successfully tested in an Erlenmeyer flask assay. Replenish phosphate and ammonium ((NH ₄ ) ₂ HPO ₄ 2.5 g / l), iron (iron citrate, 0.1 g / l H ₂ O) and thiamine (0.02 g / l) under temper conditions Cultured in medium containing diluted sugarcane juice (20 g / l sucrose equivalent) with or without supplement.

  Culturing was performed at 34 ° C., and the pH was maintained by buffering the culture medium with MOPS (40 g / l). At the end of the culture, 1,2-propanediol and sucrose, glucose and fructose remaining in the fermentation broth were analyzed by HPLC to calculate the yield of 1,2-propanediol relative to the total carbon source.

Claims (9)

A process for producing 1,2-propanediol by fermentation comprising:
Incubating an Escherichia coli microorganism that produces 1,2-propanediol in a suitable medium comprising a source of sucrose, and recovering the produced 1,2-propanediol. It becomes, wherein the microorganism is genetically modified to be capable of utilizing sucrose as a sole carbon source for the production of 1,2-propanediol, wherein the genetic modification, the PTS sucrose utilization system A method, which is the introduction of the encoding gene scrKYABR or the introduction of the gene cscBKAR encoding a non-PTS sucrose utilization system . Source of sucrose, is obtained biomass or al, The method of claim 1. The method of claim 2 , wherein the biomass is plant biomass. The method according to claim 2 or 3 , wherein the source of sucrose is obtained from a plant selected from the group consisting of sugarcane, sugar beet, sweet corn, sugar maple, sugar palm and blue agave. The method according to any one of claims 2 to 4 , wherein the source of sucrose is in the form of fruit juice, concentrated fruit juice or syrup, clarified fruit juice, molasses or crystallized sucrose. The method according to any one of claims 2 to 5 , wherein the sucrose source is a sugarcane or sugar beet industry end product, intermediate product or by-product. The method according to any one of claims 1 to 6 , wherein the suitable medium comprises a source of sucrose. The method according to any one of claims 1 to 6, wherein a suitable medium contains at least a phosphorus source and / or a nitrogen source in addition to a source of sucrose. 9. A method according to any one of claims 1 to 8 , wherein the sucrose source comprises at least 7% sucrose.