CN116790455A - Genetically engineered bacterium and method for preparing chiral phenyllactic acid by converting L-phenylalanine - Google Patents

Genetically engineered bacterium and method for preparing chiral phenyllactic acid by converting L-phenylalanine Download PDF

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CN116790455A
CN116790455A CN202211122255.6A CN202211122255A CN116790455A CN 116790455 A CN116790455 A CN 116790455A CN 202211122255 A CN202211122255 A CN 202211122255A CN 116790455 A CN116790455 A CN 116790455A
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phenylalanine
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amino acid
dehydrogenase
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邵慧
阎冬
吴玉双
孟诗雨
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Shanghai Guangyue Biotechnology Co ltd
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Abstract

The invention discloses a genetic engineering bacterium and a method for preparing chiral phenyllactic acid by converting L-phenylalanine, wherein the genetic engineering bacterium contains a coding gene of a first group of enzymes or a coding gene of a second group of enzymes; the first set of genes encoding enzymes includes genes encoding L-amino acid deaminase, phosphite dehydrogenase and L-lactate dehydrogenase; the genes encoding the second set of enzymes include genes encoding L-amino acid deaminase, phosphite dehydrogenase and D-lactate dehydrogenase. The genetically engineered bacterium provided by the invention can catalyze the L-phenylalanine to prepare two chiral phenyllactic acids, and the genetically engineered bacterium utilizes the phosphite dehydrogenase to catalyze inorganic phosphite to provide reduced coenzyme, so that the addition of organic substrate formate or glucose for coenzyme regeneration is avoided, the utilization efficiency of carbon atoms is improved, the L-phenylalanine can be efficiently converted into the L-phenyllactic acid or the D-phenyllactic acid, and the genetically engineered bacterium is a green biosynthesis technology with important industrialization prospect.

Description

Genetically engineered bacterium and method for preparing chiral phenyllactic acid by converting L-phenylalanine
Technical Field
The invention relates to a technology for preparing two chiral phenyllactic acids by catalyzing L-phenylalanine by genetically engineered microorganisms and whole cells, and belongs to the technical field of biology.
Background
Phenyllactic acid (phenyllactic acid, PLA) is a natural organic acid with high added value, exists in lactobacillus fermentation products and honey, has special biological activity, and can be widely applied to the fields of chemical industry, medicine, pesticide, food and the like as a chiral intermediate. As a small-molecule organic acid having optical activity, PLA has two enantiomers of L-phenyllactic acid and D-phenyllactic acid. Both chiral PLA have broad-spectrum antibacterial property, can be used as biological preservative to inhibit various food-borne pathogenic bacteria, and has stronger antibacterial activity and safety performance than some common chemical food preservatives. PLA can also be added into dermatological treatment drugs, and has the beauty effect of removing wrinkles and brightening skin in the cosmetic industry. In addition, phenyllactic acid is also a precursor of drugs such as anti-HIV agents and hypoglycemic agents, and for example, PLA derivatives tanshinol have the effects of inhibiting platelet aggregation and dilating coronary arteries. The current industrial method for producing phenyllactic acid is mainly a chemical synthesis method, and the method has complex process, needs high temperature and high pressure and can bring serious environmental pollution. Meanwhile, the chemical synthesis product is a mixed product of D type and L type, the product with single chiral is difficult to obtain, and the separation and the purification are difficult. The microbial fermentation method is a green production mode for synthesizing the phenyllactic acid, but generally has low product concentration and low efficiency, increases the cost of subsequent separation and refining, and is not suitable for industrial production.
With the continuous development of synthetic biology and enzyme catalysis technology, whole cell catalysis technology has been used for producing raw material substances in the fields of medicine, chemical industry, food and the like, and research on chiral phenyllactic acid biocatalysis synthesis is increasing at present. In 2018, zheng et al expressed L-amino acid deaminase, formate dehydrogenase, L-lactate dehydrogenase or D-lactate dehydrogenase in E.coli, and synthesized 59.9. 59.9 mM of L-phenyllactic acid or 60.3. 60.3 mM of D-phenyllactic acid (Zheng, Z., et al Enhanced biosynthesis of chiral phenyllactic acid from L-phenylalanine through a new whole-cell biocatalyst. Bioprocess biosystem. Eng. 2018, 41:1205-1212); in 2018, wang et al expressed L-amino acid deaminase, L-lactate dehydrogenase and formate dehydrogenase in E.coli, almost completely converting 30 g/L phenylalanine to L-phenyllactic acid (Wang, X., et al A new approach for efficient synthesis of phenyllactic acid from L-phenalane: pathway design and cofactor engineering J. Food biochem. 2018, 42:e 12584); in 2019, hou et al expressed L-amino acid deaminase, lactate dehydrogenase and formate dehydrogenase in E.coli, and 54 g/L of L-phenyllactic acid was synthesized using L-phenylalanine (Hou, Y., et al Combination of multi-enzyme expression fine-tuning and co-substrates addition improves phenyllactic acid production with an Escherichia coli whole-cell biocatalyst. Bioresource. Technique. 2019, 287: 121423); in 2022, zhang et al co-expressed L-lactate dehydrogenase and glucose dehydrogenase in Pichia pastoris, 400 mM phenylpyruvate was converted to 359.8 mM L-phenyllactic acid (Zhang, D., et al Enantioselective biosynthesis of L-phenyllactic acid from phenylpyruvic acid in vitro by L-lactate dehydrogenase coupling with glucose dehydrogenase, front, bioeng, biotechnol, 2022, 10: 846489). However, these methods generally utilize lactate dehydrogenase coupled formate dehydrogenase or glucose dehydrogenase for coenzyme regeneration, require the addition of higher concentrations of organic substrate formate or glucose to the reaction system, reduce the carbon utilization of the synthesis system and increase the cost. Therefore, there is still a need to develop a green synthesis method of chiral phenyllactic acid with high reaction efficiency, recycling of coenzyme and high atom utilization.
Disclosure of Invention
In view of the above-mentioned shortcomings of the prior art, the invention provides a genetic engineering bacterium for producing chiral phenyllactic acid, which uses phosphite dehydrogenase to catalyze inorganic phosphite to provide reduced coenzyme, thereby realizing stable and efficient conversion of L-phenylalanine into chiral phenyllactic acid, and having important application prospect.
The technical scheme adopted by the invention is as follows:
a genetically engineered bacterium comprising a gene encoding a first set of enzymes or a gene encoding a second set of enzymes; the first set of genes encoding enzymes includes genes encoding L-amino acid deaminase, phosphite dehydrogenase and L-lactate dehydrogenase; the second set of genes encoding enzymes includes genes encoding L-amino acid deaminase, phosphite dehydrogenase and D-lactate dehydrogenase; the amino acid sequence of the L-amino acid deaminase is shown as SEQ ID NO. 1, and the amino acid sequence of the phosphite dehydrogenase is shown as SEQ ID NO. 2; the amino acid sequence of the L-lactate dehydrogenase is shown as SEQ ID NO. 3; the amino acid sequence of the D-lactate dehydrogenase is shown as SEQ ID NO. 4.
Further improvement, the nucleotide sequence of the coding gene of the coding L-amino acid deaminase is shown as SEQ ID NO. 5, and the nucleotide sequence of the coding gene of the coding phosphite dehydrogenase is shown as SEQ ID NO. 6; the nucleotide sequence of the coding gene of the coding L-lactate dehydrogenase is shown as SEQ ID NO. 7, and the nucleotide sequence of the coding gene of the coding D-lactate dehydrogenase is shown as SEQ ID NO. 8.
Further improvement, the coding gene of the L-amino acid deaminase and the coding gene of the phosphite dehydrogenase are respectively synthesized into pRSFDuet-1 plasmid to form recombinant expression plasmid pRSFDuet-laad-ptxD;The coding gene of the L-lactate dehydrogenase is synthesized into pETDuet-1 plasmid to form recombinant expression plasmid pETDuet-lldh,The coding gene of D-lactate dehydrogenase is synthesized into pETDuet-1 plasmid to form recombinant expression plasmid pETDuet-dldh
Further improved, the genetically engineered bacterium is formed by pouring a gene encoding a first set of enzymes or a gene encoding a second set of enzymes into a host strain, the host strain being an E.coli BL21 (DE 3) strain.
A method for preparing chiral phenyllactic acid by converting L-phenylalanine comprises the following steps: l-phenylalanine solution is used as a substrate, and the genetically engineered bacterium is added to convert the L-phenylalanine into L-phenyllactic acid or D-phenyllactic acid.
Further improvement, the conditions of the transformation are: the final concentration of L-phenylalanine in the L-phenylalanine solution is 20-200 mM, the pH value is 6-8, the conversion temperature is 25-40 ℃, and the conversion time is 6-12 h.
Further improved, the conditions of the transformation are as follows: the L-phenylalanine solution contains 200 mM L-phenylalanineAcid, 200 mM Na 2 HPO 3 The added amount of the pH=8 genetically engineered bacteria is 20 g/L of final concentration, the conversion temperature is 30 ℃, the conversion time is 12h, and the stirring rotation speed during conversion is 200 rpm.
The beneficial effects of the invention are as follows: the invention provides a genetically engineered bacterium which is used for converting L-phenylalanine to prepare L-phenyllactic acid or D-phenyllactic acid. Compared with the prior chiral phenyllactic acid biosynthesis method for regenerating the coenzyme by using formate dehydrogenase or glucose dehydrogenase, the invention utilizes phosphite dehydrogenase to catalyze inorganic phosphite to regenerate the coenzyme, avoids adding organic substrate formate or glucose, improves the utilization efficiency of carbon atoms, can efficiently convert L-phenylalanine into L-phenyllactic acid or D-phenyllactic acid, and is a green biosynthesis technology with important industrialization prospect.
The conception, specific structure, and technical effects of the present invention will be further described with reference to the accompanying drawings to fully understand the objects, features, and effects of the present invention.
Drawings
FIG. 1 is a schematic diagram of the synthesis route of L-phenyllactic acid by converting L-phenylalanine to Lumy-E209 in example 1 of the present invention.
FIG. 2 is a schematic diagram of the synthesis route of L-phenylalanine by converting Lumy-E210 in example 2 of the present invention.
FIG. 3 is a graph showing the yields of L-phenyllactic acid produced by Lumy-E209 and D-phenyllactic acid produced by Lumy-E210 in examples 3 and 4 of the present invention.
Detailed Description
The technical contents of the present invention are further described below with reference to examples: the following examples are illustrative, not limiting, and are not intended to limit the scope of the invention. The test methods used in the following examples are conventional methods unless otherwise specified. Materials, reagents and the like used in the examples described below are commercially available unless otherwise specified.
The strains and growth conditions used in the present invention are as follows:
cloning host DH 5. Alpha. And expression host BL21 (DE 3) were purchased from Invitrogen, all E.coli were cultivated at 37℃in LB medium containing 100mg/l ampicillin or 100mg/l kanamycin.
Wherein, the formula of the LB liquid medium is as follows: peptone 10 g/L, yeast extract 5 g/L, naCl 10 g/L, pH 7.0; LB solid culture medium 20 g/L agar is added into LB liquid culture medium; sterilizing with steam at 121deg.C under high temperature and high pressure for 20 min.
All plasmids were pETDuet-1 or pRSFDuet-1 (purchased from Novagen) derived plasmids for expression of the gene of interest.
Example 1
Constructing genetically engineered bacteria Lumy-E209 and Lumy-E210:
(1) Synthesis of L-amino acid deaminasePmLAAD) coding gene [ (]laad) Fragment, phosphite dehydrogenaseRaPPDH) coding gene [ ]ptxD) Fragment, L-lactate dehydrogenaseLpLLDH) coding genelldh) And D-lactate dehydrogenase [ ]LnDLDH) coding genedldh):
Utilizing online software JCat to ensure that the colibacillus is produced according to the codon preference of the escherichia coliProteus myxofaciens) In (a) and (b)laadGene, ralstonia strainRalstoniasp.)ptxDGene, cheese bacillus and its preparing processLacticaseibacillus paracasei) In (a) and (b)lldhGene and Nasalidis lactobacillusLactobacillus nasalidis) In (a) and (b)dldhCodon optimization is carried out on the gene, and after optimizationlaadThe nucleotide sequence of (2) is shown as SEQ ID NO. 5,ptxDthe nucleotide sequence of (2) is shown as SEQ ID NO. 6,lldhthe nucleotide sequence of (2) is shown as SEQ ID NO. 7,dldhthe nucleotide sequence of (2) is shown as SEQ ID NO. 8. The above gene sequence was sent to the gene synthesis company (GENEWIZ),laadthe pRSFDuet-1 was obtained by synthesizing the plasmid intermediate the BamHI and HindIII cleavage sites of pRSFDuet-1laadptxDSynthesis into pRSFDuet-laadIntermediate NdeI and XhoI cleavage sites to obtain recombinant expression plasmid pRSFDuet-laad-ptxDlldhAnddldhrespectively synthesizing the recombinant expression plasmid pETDuet-1 into the middle of BamHI and HindIII enzyme cutting sites of pETDuet-1 to obtain recombinant expression plasmid pETDuet-lldhAnd pETDuet-dldh
(2) Obtaining genetically engineered bacterium Lumy-E209:
mu.L of the recombinant plasmid pRSFDuet obtained in step (1) was used for preparing a plasmid pRSFDuet-laad-ptxDAnd 5. Mu.L of the recombinant plasmid pETDuet obtained in step (1)lldhTransformation into competent cells of E.coli BL21 (DE 3) was carried out by the heat shock method. The heat-shocked bacterial liquid is coated on LB solid medium flat plate containing 100mg/L ampicillin and kanamycin, and cultured in a constant temperature incubator at 37 ℃ for 12 hours. Single colony was picked up on a plate to 5mL of LB liquid medium (containing 100mg/L ampicillin and kanamycin) and incubated in a shaker at 37 ℃ at 200 rpm; and (3) carrying out PCR amplification verification on the cultured bacterial liquid to obtain a genetic engineering strain Lumy-E209, wherein the Lumy-E209 can be used for converting phenylalanine to prepare L-phenyllactic acid as shown in figure 1.
(3) Obtaining genetically engineered bacterium Lumy-E210:
mu.L of the recombinant plasmid pRSFDuet obtained in step (1) was used for preparing a plasmid pRSFDuet-laad-ptxDAnd 5. Mu.L of the recombinant plasmid pETDuet obtained in step (1)dldhTransformation into competent cells of E.coli BL21 (DE 3) was carried out by the heat shock method. The heat-shocked bacterial liquid was spread on LB solid medium plates containing 100mg/L ampicillin and 100mg/L kanamycin, and cultured in a constant temperature incubator at 37℃for 12 hours. Single colonies were picked on plates into 5mL LB liquid medium (containing 100mg/L ampicillin and 100mg/L kanamycin) and incubated in a shaker at 37℃at 200 rpm. And (3) carrying out PCR amplification verification on the cultured bacterial liquid to obtain a genetic engineering strain Lumy-E210, wherein the Lumy-E210 can be used for converting L-phenylalanine to prepare D-phenyllactic acid as shown in figure 2.
Example 2
Preparation of L-phenyllactic acid by converting genetically engineered bacterium Lumy-E209 into L-phenylalanine
(1) Preparing a whole cell catalyst of genetically engineered bacterium Lumy-E209:
the genetically engineered bacterium Lumy-E209 obtained in the step (2) of the embodiment 1 is inoculated into 50mL of LB liquid medium (containing 100mg/L ampicillin and 100mg/L kanamycin) by an inoculating loop for strain activation, and the strain is subjected to 37 ℃ C. Strain activationCulturing at night; subsequently, the activated bacterial liquid was inoculated into 1L of LB liquid medium (containing 100mg/L ampicillin and 100mg/L kanamycin) at 37℃and 200rpm in an inoculum size of 1% (volume ratio), and cultured for 3-5 hours to OD 600 Reaching 0.6-0.8, adding 0.2 mM IPTG,16 ℃, and carrying out induction culture at 200rpm for 16h; the resulting culture broth was collected, centrifuged at 3500rpm at 4℃for 15 minutes to collect the cells, and the cells were washed with phosphate buffer for 2 times for use.
(2) Preparation of L-phenyllactic acid by conversion of L-phenylalanine from Lumy-E209
Constructing a reaction system by taking the thalli collected in the step (1) as a catalyst, adding 200 mM of L-phenylalanine and 200 mM of Na into the reaction system, wherein the addition amount of the thalli is 20 g/L 2 HPO 3 Ph=8, reaction conditions were 30 ℃, stirring speed was 200rpm, 12h. The amount of L-phenyllactic acid produced was measured by HPLC, using an Agilent1260 liquid chromatograph, a chromatography column of Agilent Zorbax SB-C18 (4.6X150 mm), a detection wavelength of 210 nm, a column temperature of 30℃and a mobile phase A of water (containing 1% trifluoroacetic acid), a mobile phase B of acetonitrile (containing 1% trifluoroacetic acid), a flow rate of 1 mL/min, and a gradient elution procedure of: 0 minutes, 90% mobile phase a+10% mobile phase B; 15 minutes, 5% mobile phase a+95% mobile phase B;18 minutes, 5% mobile phase a+95% mobile phase B; 20 minutes, 90% mobile phase A+10% mobile phase B. The flow rate was 1 mL/min. As shown in FIG. 3, L-phenylalanine is transformed by a recombinant bacterium to obtain 29.42 g/L-phenyllactic acid. Acidifying the reaction liquid, extracting with ethyl acetate, and vacuum rotary evaporating the extractive solution to obtain pure L-phenyllactic acid product with e.e. value of above 99%.
Example 3
Preparation of D-phenyllactic acid by converting genetically engineered bacterium Lumy-E210 into L-phenylalanine
(1) Preparing a whole cell catalyst of genetically engineered bacterium Lumy-E210:
inoculating the genetically engineered bacterium Lumy-E210 obtained in the step (3) in the embodiment 1 into 50mL of LB liquid medium (containing 100mg/L ampicillin and 100mg/L kanamycin) by an inoculating loop for strain activation, and culturing at 37 ℃ overnight; then, the activated bacterial liquid was inoculated into 5L LB liquid culture according to an inoculum size of 1% (volume ratio)Culturing in medium (containing 100mg/L ampicillin and 100mg/L kanamycin) at 37deg.C and 200rpm for 3-5 hr to OD 600 Reaching 0.6-0.8, adding 0.2 mM IPTG,16 ℃, and carrying out induction culture at 200rpm for 16h; the resulting culture broth was collected, centrifuged at 3500rpm at 4℃for 15 minutes to collect the cells, and the cells were washed with phosphate buffer for 2 times for use.
(2) Preparation of D-phenyllactic acid by converting Lumy-E210 into L-phenylalanine
Constructing a reaction system by taking the thalli collected in the step (1) as a catalyst, adding 200 mM of L-phenylalanine and 200 mM of Na into the reaction system, wherein the addition amount of the thalli is 20 g/L 2 HPO 3 Ph=8, reaction conditions were 30 ℃, stirring speed was 200rpm, 12h. The amount of L-phenyllactic acid produced was measured by HPLC, using an Agilent1260 liquid chromatograph, a chromatography column of Agilent Zorbax SB-C18 (4.6X150 mm), a detection wavelength of 210 nm, a column temperature of 30℃and a mobile phase A of water (containing 1% trifluoroacetic acid), a mobile phase B of acetonitrile (containing 1% trifluoroacetic acid), a flow rate of 1 mL/min, and a gradient elution procedure of: 0 minutes, 90% mobile phase a+10% mobile phase B; 15 minutes, 5% mobile phase a+95% mobile phase B;18 minutes, 5% mobile phase a+95% mobile phase B; 20 minutes, 90% mobile phase A+10% mobile phase B. The flow rate was 1 mL/min. As shown in FIG. 3, the D-phenyllactic acid of 27.32 g/L was obtained after transformation of L-phenylalanine by a recombinant bacterium. Acidifying the reaction liquid, extracting with ethyl acetate, and vacuum rotary evaporating the extractive solution to obtain pure D-phenyllactic acid product with e.e. value of above 99%.
The foregoing describes in detail preferred embodiments of the present invention. It should be understood that numerous modifications and variations can be made in accordance with the concepts of the invention without requiring creative effort by one of ordinary skill in the art. Therefore, all technical solutions which can be obtained by logic analysis, reasoning or limited experiments based on the prior art by the person skilled in the art according to the inventive concept shall be within the scope of protection defined by the claims.

Claims (7)

1. A genetically engineered bacterium, comprising a gene encoding a first set of enzymes or a gene encoding a second set of enzymes; the first set of genes encoding enzymes includes genes encoding L-amino acid deaminase, phosphite dehydrogenase and L-lactate dehydrogenase; the second set of genes encoding enzymes includes genes encoding L-amino acid deaminase, phosphite dehydrogenase and D-lactate dehydrogenase; the amino acid sequence of the L-amino acid deaminase is shown as SEQ ID NO. 1, and the amino acid sequence of the phosphite dehydrogenase is shown as SEQ ID NO. 2; the amino acid sequence of the L-lactate dehydrogenase is shown as SEQ ID NO. 3; the amino acid sequence of the D-lactate dehydrogenase is shown as SEQ ID NO. 4.
2. The genetically engineered bacterium of claim 1, wherein the nucleotide sequence of the coding gene encoding an L-amino acid deaminase is shown in SEQ ID No. 5 and the nucleotide sequence of the coding gene encoding a phosphite dehydrogenase is shown in SEQ ID No. 6; the nucleotide sequence of the coding gene of the coding L-lactate dehydrogenase is shown as SEQ ID NO. 7, and the nucleotide sequence of the coding gene of the coding D-lactate dehydrogenase is shown as SEQ ID NO. 8.
3. The genetically engineered bacterium of claim 1, wherein the gene encoding an L-amino acid deaminase and the gene encoding a phosphite dehydrogenase are synthesized into pRSFDuet-1 plasmid to form recombinant expression plasmid pRSFDuet-laad-ptxD;The coding gene of the L-lactate dehydrogenase is synthesized into pETDuet-1 plasmid to form recombinant expression plasmid pETDuet-lldh,The coding gene of D-lactate dehydrogenase is synthesized into pETDuet-1 plasmid to form recombinant expression plasmid pETDuet-dldh
4. The method of claim 1, wherein the genetically engineered bacterium is formed by pouring a gene encoding a first set of enzymes or a gene encoding a second set of enzymes into a host strain, the host strain being E.coli BL21 (DE 3) strain.
5. The method for preparing chiral phenyllactic acid by converting L-phenylalanine is characterized by comprising the following steps: the method comprises the steps of using an L-phenylalanine solution as a substrate, adding the genetically engineered bacterium of any one of claims 1-4, and converting the L-phenylalanine into L-phenyllactic acid or D-phenyllactic acid.
6. The method for preparing chiral phenyllactic acid by converting L-phenylalanine according to claim 5, wherein the conditions for the conversion are: the final concentration of L-phenylalanine in the L-phenylalanine solution is 20-200 mM, the pH value is 6-8, the conversion temperature is 25-40 ℃, and the conversion time is 6-12 h.
7. The method for preparing chiral phenyllactic acid by converting L-phenylalanine according to claim 6, wherein the conditions for the conversion are as follows: the L-phenylalanine solution contains 200 mM Na and 200 mM L-phenylalanine of 200 mM 2 HPO 3 The added amount of the pH=8 genetically engineered bacteria is 20 g/L of final concentration, the conversion temperature is 30 ℃, the conversion time is 12h, and the stirring rotation speed during conversion is 200 rpm.
CN202211122255.6A 2022-09-15 2022-09-15 Genetically engineered bacterium and method for preparing chiral phenyllactic acid by converting L-phenylalanine Pending CN116790455A (en)

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