NOVEL BACTERIAL STRAINS FOR THE PRODUCTION OF VANILLIN
The present patent application is filed pursuant to 35 U.S.C. § 371 as a U.S. National Phase Application of International Patent Application No. PCT/FR2016/052403 filed Sep. 22, 2016, claiming the benefit of priority to French Patent Application No. 1559142 filed Sep. 29, 2015. The International Application was published as WO 2017/055712 on Apr. 6, 2017. The contents of each of the aforementioned patent applications are herein incorporated by reference in their entirety. The instant application contains a Sequence Listing which has been submitted electronically in ASCII format and is hereby incorporated by reference in its entirety. Said ASCII copy, created on Mar. 16, 2018, is named 44980002023_SL.txt and is 16,194 bytes in size. The present invention relates to the field of production of vanillin. It relates particularly to an Vanillin is one of the major components constituting vanilla extract, which is a powerful natural aroma obtained from the bean of an orchid. The extraction of this molecule from vanilla beans is very expensive; the quantities produced are limited and do not cover market demand. Other ways of obtaining vanillin have been sought. It is for example possible to obtain vanillin from ferulic acid by bioconversion reaction with bacteria. In this patent application, we are interested only in the ferulic acid bioconversion pathway of vanillin by bacteria. Vanillin production by bacteria is done by deacetylation of ferulic acid by means of the following 3 steps: 1. Activation of ferulic acid in feruloyl-CoA, activation being catalysed by an enzyme, the feruloyl-CoA ligase, hereinafter FCS; 2. Hydroxylation of the feruloyl-CoA in 4-Hydroxy-3-methoxyphenyl-P-hydroxypropionyl-CoA, hydroxylation being catalysed by an enzyme, Enoyl-CoA Hydratase/Aldolase, hereinafter ECH; 3. Deacetylation of the 4-Hydroxy-3-methoxyphenyl-β-hydroxypropionyl-CoA allowing vanillin to be obtained, also catalyzed by the enzyme ECH. The vanillin obtained can subsequently be oxidized to vanillic acid by an enzyme, vanillin dehydrogenase, hereinafter VDH. However, converting vanillin to vanillic acid is not desired because only the vanillin has the desired aromatic characteristics. According to the EC nomenclature of the enzymes (Enzyme Commission number):
EP 2 721 148 A1 describes a microorganism of the genus EP 1 611 244 A1 describes a vanillin production process that does not use organic solvents during purification, as they are now considered undesirable in the food industry, to obtain a vanillin called “natural.” During said vanillin production process, the biotransformation of ferulic acid into vanillin is performed by the The book “Practical However, the strains of the prior art used in the bioconversion reaction do not allow an optimal conversion of ferulic acid to vanillin. Given the cost of ferulic acid, there remains a need for new strains of bacteria ensuring better conversion of ferulic acid to vanillin. The applicant has thus developed new strains of bacteria through an original transformation method, allowing for an improved molar yield during the bioconversion reaction. The invention thus provides an The invention also relates to a method for obtaining an The invention also relates to an integration cassette comprising the expression cassette of ECH genes and FCS. The invention also relates to the use of said strains in a process for obtaining vanillin. The invention also relates to a vanillin production process. The present invention relates to novel bacterial strains of the After extensive research, the inventors have developed new A bioconversion molar yield is defined as the ratio between the number of moles of the product obtained, in our case vanillin, divided by the number of moles of substrate implemented, in this case, ferulic acid. When in percentage, this ratio is multiplied by 100. “Improved molar yield compared to the prior art” means a molar yield of bioconversion greater than or equal to 80%, preferably greater than or equal to 85%, and more preferably equal to greater than 90%. The The terms “Zyl 926 strain”, “926 “ The inventors have further demonstrated that new strains of the invention can also improve productivity and consumption of almost all of the ferulic acid in the bioconversion reaction. “Consuming substantially all of the ferulic acid” means that at least 98% of ferulic acid is consumed during the bioconversion reaction, preferably at least 99%, and even more preferably 100%. The present invention therefore relates to an said additional copies of genes FCS and ECH being specifically integrated at the integration site of the phage φC31, also called attB site. The article by Keravala et al. (Methods Mol Biol. 2008) mentions the use of the phage φC31 integrase as a mediator for chromosomal integration site-specific. It thus allows a unidirectional recombination between two att sites called attP and attB. “Extra copy of the gene” means any copy of an integrated gene of interest into the genome of a strain as well as copies of the gene of interest initially present in the genome. A protein sequence or nucleic called identical to another when the alignment between the two sequences is perfect, i.e. when there is a perfect correspondence respectively between amino acids or nucleic acids of each sequence. The sequence identity percentage is calculated by giving a score of 0 or 1 for each amino acid or base sequence as to whether there is identity or not. The terms “ECH gene encoding Enoyl-CoA Hydratase/Aldolase” and “FCS gene encoding Feruloyl-CoA Synthetase” should not be narrowly interpreted but should also encompass sequences encoding functional variants of these enzymes. Typically, functional variants of these enzymes FCS and ECH have a protein sequence having an identity percentage of at least 80%, preferably at least 90% and more particularly preferably at least 95% with the protein sequences SEQ ID NO: 1 and SEQ ID NO: 2. Advantageously, the present invention relates to an The ermE* promoter is the ermE promoter modified to give a strong and constitutive expression. The ermE* promoter has nucleic acid sequence SEQ ID NO: 6 or any sequence at least 90%, preferably at least 95% and even more preferably at least 99% identical to SEQ ID NO: 6. The sequence of the ermE* promoter is described in the article by Bibb et al. (Mol Microbiol. 1994 November; 14(3):533-45) To obtain the new original strains of the invention that overexpress the FCS and ECH genes, the inventors revealed after much research and experimentation that the interspecific transfer method enabled transformants to be obtained that have integrated at least one supplementary copy of the genes ECH and FCS and that the success of this gene integration method was locus dependent. The term “locus dependent” means that supplementary copies of genes of interest must be specifically integrated at the φC31 phage integration site. The present invention therefore relates to a process for obtaining an a) amplification by PCR of the FCS genes encoding Feruloyl-CoA Synthetase having the sequence SEQ ID NO: 1 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO: 1 and ECH encoding Enoyl-CoA Hydratase/Aldolase having the sequence SEQ ID NO: 2 or any sequence at least 80%, preferably at least 90%, and even more preferably at least 95% identical to SEQ ID NO: 2, isolated from an b) constructing a vector carrying the nucleic acid sequences obtained in step a, from pSET152 plasmid having:
c) transformation by electroporation of the ET12567 d) selection of the ET12567 e) interspecific transfer between ET12567 f) selection of the The FCS and ECH genes have been isolated and amplified from an The sequences of the primers used are the following sequences: Preferably the FCS and ECH genes were isolated from the strain The pSET152 plasmid has apramycin resistance. The vector construction according to step b) is made by cloning additional copies of genes FCS and ECH amplified in step a in pSET152 plasmid (Bierman et al, Gene, 116 (1): 43-49, 1992). The PCR product containing ECH and FCS genes was obtained using as genomic DNA matrix of the strain Zyl926 and Van-ECH-F primer (SEQ ID NO: 7) and Van-ECH-R (SEQ ID NO: 8). The fragment to be integrated was obtained by HindIII digestion (+ Klenow) and XbaI. The HindIII fragments (Klenow+) and XbaI were cloned in the EcoRV and XbaI pSET152 sites. Int gene means the gene encoding the integrase of phage φC31 with the protein sequence SEQ ID NO: 3 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to the sequence SEQ ID NO: 3. The phage attachment site φC31, also called attP site present in the pSET152 plasmid, has the sequence SEQ ID NO: 4. SEQ ID NO: 4 is the following: Selecting ET 12567 Co-culturing for the production of the interspecific transfer of step e), is carried out under conventional conditions known to the person skilled in the art (Bierman et al, 1992 see above) and preferably by bringing into contact for several hours a part of the ET12567 The The selection according to step f) of According to a particular embodiment, the invention more particularly relates to a method of obtaining an The ermE* promoter has the sequence SEQ ID NO: 6 or any sequence at least 90%, preferably at least 95% and even more preferably at least 99% identical to SEQ ID NO: 6. According to a particular embodiment, the invention particularly relates to a method for obtaining an According to a particular embodiment, the invention more particularly relates to a method of obtaining an The present invention also purposes an The present invention also particularly relates to an The strains I-4922, I-4923 and I-4924 are strains ofAmycolatopsis sp. filed under the Budapest Treaty, on 11 Dec. 2014 with the CNCM (Collection Nationale de Cultures de Microorganismes [National Collection of Microorganism Cultures]), 25 rue du Docteur Roux, 75724 Paris Cedex 15, France. The present invention also relates to an integration cassette comprising: i. an expression cassette of the FCS gene encoding feruloyl-CoA synthetase having the sequence SEQ ID NO: 1 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO: 1 and ECH encoding Enoyl-CoA Hydratase/Aldolase having the sequence SEQ ID NO: 2 or any sequence at least 80%, preferably at least 90%, and even more preferably at least 95% identical to SEQ ID NO: 2; ii. means for integration of the cassette into the genome of the strain iii. means for selecting iv. means for selecting An integration cassette is a genetic construct comprising the necessary tools for the integration of one or more genes of interest into the genome of an organism, here the strain According to a particular embodiment of the invention, the genes encoding Feruloyl-CoA Synthetase and Enoyl-CoA Hydratase/Aldolase of the expression cassette described above are placed under the control of strong ermE* promoter having the sequence SEQ ID NO: 6 or any sequence at least 90%, preferably at least 95% and even more preferably at least 99% identical to SEQ ID NO: 6 said ermE* promoter being associated with a ribosome binding site, also known as RBS. According to a particular embodiment, the invention more particularly relates to an integration cassette as described above, wherein the beta-lactam is ampicillin. The invention also relates to the use of new The present invention also relates to a method of producing vanillin comprising the steps of: a. providing an b. culturing the new c. bringing ferulic acid into contact with said culture of d. extracting vanillin from the culture medium. The cultivation of the new derived A source of carbon may be, for example, glycerol. The incubation according to step c of vanillin production process is carried out until the consumption of substantially all of the ferulic acid and at a temperature between 37° C. and 41° C. According to a particular embodiment of the invention, the vanillin production process is the process described in EP 1 611 244 A1. The bioconversion reaction when vanillin production process is therefore carried out in a medium comprising a new According to a particular embodiment of the invention, the The invention more particularly relates to a vanillin production process as described above wherein the molar yield is greater than or equal to 80%, preferably greater than or equal to 85%, and more preferably equal to 90%. The invention more particularly relates to a vanillin production process as described above wherein at least 98% of ferulic acid is consumed, preferably at least 99%, and more preferably 100%. The inventors implementing said vanillin production process as described above with the new and this without the flow of vanillin dehydrogenase converting vanillin to vanillic acid being increased. The present invention also relates to a new The present invention also relates to a process for obtaining a novel Material and Method Bacterial strains:— Plasmids:—p SET152: carrying an ampicillin resistance gene
a. Amplification The ECH and FCS genes were amplified from the The primers used are: b. Cloning The fragment to be integrated is obtained by HindIII digestion (+ Klenow) and XbaI. The HindIII fragment (+ Klenow) and XbaI was then cloned in the EcoRV and XbaI sites of pSET152. The plasmid thus obtained is called pLSF01a. The pSET152 plasmid has the φC31 phage integration system namely:
The pSET152 plasmid also has the functional origin of transfer oriT allowing the mobilization thereof and transfer of b′. Amplification and Cloning of the ermE* Promoter The addition of the ermE* promoter and the chloramphenicol resistance gene was carried out by in vivo recombination between short identical sequences (PCR-targeting) as described by Yu et al. (2000) (Proc Natl Acad Sci USA. 2000 23 May; 97 (11): 5978-83). For this purpose, a sequence corresponding to the resistance gene for chloramphenicol, the ermE* promoter and the RBS of the tipA gene was obtained by PCR using as matrix the pOSV605 plasmid and as primers the oligonucleotides LG001 and LG002. The sequences of the primers used are following: This yielded a fragment having at each end sequences identical to those of two neighbouring regions on the pLSF01a plasmid:
The recombination took place in vivo in the strain DY330 (Yu et al. 2000) containing the pLSF01 plasmid after transformation with the PCR product. Clones that have integrated the ermE* promoter were selected on the basis of the acquisition of chloramphenicol resistance. Selected clones are called pLSF02 plasmids. c. Transformation The ET12567 strain containing the pUZ8002 plasmid was transformed by electroporation with the pLSF02 plasmid from steps b. and b′., comprising the additional copies of genes ECH and FCS and strong ermE* promoter associated with the RBS. d. Selection of Transformants Selecting transformants having the pLSF02 plasmid is done in a medium containing apramycin. e. Interspecific Transfer Transformants ( f. Selection of Transformed Zyl 926 Strains The selection of the This last step has led to the selection of the strains deposited with the CNCM under the numbers I-4922, I-4923, I-4924 and have integrated additional copies of the ECH and FCS genes at the φC31 phage integration site. Bacterial strains:— Plasmids:—pOSV408: carrying a gene for resistance to kanamycin.
a. Amplification The ECH and FCS genes were amplified from the The primers used are: b. Cloning The fragment to be integrated is obtained by HindIII digestion (+ Klenow) and XbaI. The HindIII fragment (+ Klenow) and XbaI was then cloned in the EcoRV and XbaI sites of pOSV408. The plasmid thus obtained is called pLSF01b The pOSV408 plasmid (KanaR) has the integration system of the φBT1 phage namely:
The pOSV408 plasmid also has the functional origin of transfer oriT allowing the mobilization thereof and transfer of b′. Amplification and Cloning of the ermE* Promoter The addition of the ermE* promoter and the chloramphenicol resistance gene was carried out by in vivo recombination between short identical sequences (PCR-targeting) as described by Yu et al. (2000) (Proc Natl Acad Sci USA. 2000 May 23; 97 (11): 5978-83). To this end, a sequence corresponding to the resistance gene for chloramphenicol, the ermE* promoter and for RBS of the tipA gene was obtained by PCR using as matrix the pOSV605 plasmid and as primers the LG001 and LG002 oligonucleotides having respectively the sequences SEQ ID NO: 9 and SEQ ID NO: 10. This resulted in a fragment having at each end sequences identical to those of two neighbouring regions on the pLSFOlb plasmid:
The recombination took place in vivo in the DY330 strain (Yu et al. 2000) containing the pLSFOlb plasmid after transformation by the PCR product. The clones which have integrated the ermE* promoter were selected on the basis of the acquisition of chloramphenicol resistance. The selected clones are called pLSF07 plasmids. c. Transformation The ET12567 strain containing the pUZ8002 plasmid is transformed by electroporation with the pLSF07 plasmid from the preceding steps, comprising the additional copies of the ECH and FCS genes and strong promoter ermE * associated with the RBS. d. Selection of Transformants Transformants which have integrated the pLSF07 plasmid are selected in a medium comprising kanamycin. e. Interspecific Transfer The cells of The transformants and f. Selecting Transformed Zyl 926 Strains The strains This last step was used to select the strains filed with the CNCM on 11 Dec. 2014 under number I-4925, 1-4926 and I-4927 having integrated additional copies of the FCS and ECH genes at the φBTI phage integration site. Bacterial strains:—CNCM-I-4922
The vanillin production process used in this example is the process mentioned in EP 1 611 244 A1. Maximum productivity is calculated using the following equation: The molar yield is calculated according to the following equation: The overall mass yield of vanillin/ferulic acid is calculated according to the following equation: The results obtained using the vanillin production process of EP 1 611 244 with the strain according to the invention I-4922 and the Zyl 926 strain are shown in Table 1 below. Note that the density is close to 1, the unit g/kg is equivalent to g/L. Conclusion The results obtained show that the strain according to the invention I-4922 provides a greater amount of vanillin, an improved molar yield, and the consumption of substantially all of the ferulic acid based on the Zyl 926 strain of the prior art. Bacterial strains:—CNCM-I-4922 (φC31)
The vanillin production process used in this example is the process mentioned of EP 1 611 244 A1. The results obtained using the vanillin production process of EP 1 611 244 with the strains I-4922, 14926 and Zyl 926 are presented in Table 2 below. The results show that the strain according to the invention I-4922 having integrated at least one copy of ECH and FCS genes at the φC31 phage integration site enables production of more vanillin compared to the strain of the prior art Zyl 926. The results also show that the I-4926 strain having incorporated at least one extra copy of the FCS and ECH genes at the φBTI phage integration site does not improve the production of vanillin compared to the Zyl 926 strain of the prior art. The integration of at least one additional copy of ECH and FCS genes of the invention in the Zyl 926 strain is locus dependent. The invention also relates to the method for producing such strains, the integration cassette of the FCS and ECH genes, the use of said strains in a method for producing vanillin, and a method for producing vanillin. 1. An 2. An 3. A process for obtaining an a. PCR amplification of the FCS gene encoding feruloyl-CoA-synthetase having the sequence SEQ ID NO: 1 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO sequence: 1 and ECH encoding enoyl-CoA-hydratase/Aldolase having sequence SEQ ID NO: 2 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO: 2, isolated from an b. constructing a vector carrying the nucleic acid sequences obtained in step a, from pSET152 plasmid. c. transformation by electroporation of the ET12567 d. selection of strains of e. interspecific transfer between f. selection of 4. A method according to 5. A method according to 6. Method according to 7. An 8. An 9. An integration cassette characterized in that it comprises:
i. an expression cassette of the FCS gene encoding feruloyl-coA-synthetase having the sequence SEQ ID NO: 1 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO: 1 and ECH encoding enoyl-coA-hydratase/aldolase having the sequence SEQ ID NO: 2 or any sequence at least 80%, preferably at least 90%, and more preferably at least 95% identical to SEQ ID NO: 2; ii. means for integration of the cassette into the genome of the strain iii. means for selecting transformed iv. means for selecting 10. An integration cassette according to 11. An integration cassette according to 12. Use in a method of producing vanillin from a 13. A method of producing vanillin, characterized in that the bioconversion reaction is carried out in a medium comprising an RELATED APPLICATIONS AND INCORPORATION BY REFERENCE
SEQUENCE LISTING
FIELD OF INVENTION
TECHNICAL BACKGROUND
SUMMARY OF THE INVENTION
DETAILED DESCRIPTION
SEQ ID NO: 7: Van-ECH-F: 5′ GAAGCTTGAGCGATGCATGAGCACAGC 3′ SEQ ID NO: 8: Van-ECH-R: 5′ GTCTAGACTGGTTGCGCACTACTTCTC 3′ GCCCCAACTGGGGTAACCTTTGAGTTCTCTCAGTTGGGG EXAMPLES
Example 1: Cloning of Additional Copies of the ECH and FCS Genes in Zyl 926 at the φC31 Phage Integration Site
SEQ ID NO: 7: Van-ECH-F: 5′ GAAGCTTGAGCGATGCATGAGCACAGC 3′ SEQ ID NO: 8: Van-ECH-R: 5′ GTCTAGACTGGTTGCGCACTACTTCTC 3′ SEQ ID NO: 9: LG001: 5′ CAGCTATGACATGATTACGAATTCGATAGCTTAGCGATGCTCACGCA GTTAGACACTCAC 3′ SEQ ID NO: 10: LG002: 5′ GCTCCGTCCGGACCCGCCCGTTGCCGACCGCTGTGCTCATATGTCCG CTCCCTTCTCCCGCGAATTCACTAGTGATT 3′ Results
Example 2: Cloning of Additional Copies of ECH and FCS Genes in Zyl 926 at the φBTI Phage Integration Site
Material and Method
SEQ ID NO: 7: Van-ECH-F: 5′ GAAGCTTGAGCGATGCATGAGCACAGC 3′ SEQ ID NO: 8: Van-ECH-R: 5′ GTCTAGACTGGTTGCGCACTACTTCTC 3′ Results
Example 3: Production of Vanillin by the
Material and Method
Results
Initial ferulic acid concentration 25.5 g/Kg 25 g/L Maximum productivity 0.52 g/Kg · h Non defined Residual ferulic acid 0.1 g/Kg 1.01 g/L Vanillin produced 17.1 g/Kg 13.8 g/L Vanillic acid produced 0.8 g/Kg Non defined Molar yield 86% 73% Overall vanillin/ferulic acid mass 67% 55% yield Example 4: Comparison of Vanillin Production Using Strains I-4922 and I-4926
Materials and Methods
Results
Initial ferrulic acid 25 g/L 24.8 g/Kg 25.5 g/Kg concentration Vanillin produced 13.8 g/L 14.4 g/Kg 17.5 g/Kg Conclusion