METHOD OF CONTINUOUSLY PRODUCING GLUTATHIONE USING PHOTOSYNTHETIC MEMBRANE VESICLES
20180010163 · 2018-01-11
Assignee
Inventors
Cpc classification
C12N9/00
CHEMISTRY; METALLURGY
International classification
C12P21/02
CHEMISTRY; METALLURGY
Abstract
The present invention relates to a method of producing glutathione, wherein photosynthetic membrane vesicles and enzymes catalyzing glutathione synthesis are combined and glutamate, cysteine and glycine are used as reaction substrates. As enzymes catalyzing glutathione synthesis, γ-glutamylcysteine synthetase and glutathione synthetase may be used together, or bifunctional glutathione synthetase may be used alone. According to the conventional methods, there is a problem in that expensive adenosine triphosphate should be continuously supplied when glutathione is produced. However, according to the present invention, since photosynthetic membrane vesicles are used as a source to regenerate adenosine triphosphate, it is possible to continuously produce glutathione without additionally adding adenosine triphosphate, thereby reducing production costs of glutathione.
Claims
1. A method of producing glutathione, comprising: a) a step of generating adenosine triphosphate (ATP) from adenosine diphosphate (ADP) and an inorganic phosphate by irradiating photosynthetic membrane vesicles with light; and b) a step of synthesizing glutathione by enzymes that catalyze glutathione synthesis using ATP generated in step a), and forming ADP and an inorganic phosphate.
2. The method according to claim 1, further comprising c) a step of reusing ADP and an inorganic phosphate forming in step b) to generate ATP in photosynthetic membrane vesicles.
3. The method according to claim 1, wherein the photosynthetic membrane vesicles are selected from the group consisting of chromatophore membrane vesicles isolated from purple non-sulfur bacteria and thylakoid membrane vesicles isolated from cyanobacteria or algae.
4. The method according to claim 1, wherein the enzymes that catalyze glutathione synthesis are one or more selected from the group consisting of γ-glutamylcysteine synthetase (GSH-I), glutathione synthetase (GSH-II) and bifunctional glutathione synthetase (bifunctional γ-glutamylcysteine synthetase/glutathione synthetase, GshF).
5. The method according to claim 1, further comprising a step of adding glutamate, cysteine and glycine as substrates for producing glutathione.
6. The method according to claim 1, wherein step b) comprises a step of synthesizing γ-glutamylcysteine from glutamate and cysteine by γ-glutamylcysteine synthetase while converting adenosine triphosphate generated in step a) into adenosine diphosphate and an inorganic phosphate; and a step of synthesizing glutathione from the synthesized γ-glutamylcysteine and glycine by glutathione synthetase while converting adenosine triphosphate generated in step a) into adenosine diphosphate and an inorganic phosphate.
7. The method according to claim 1, wherein step b) comprises a step of synthesizing glutathione from glutamate, cysteine and glycine by bifunctional glutathione synthetase while converting adenosine triphosphate generated in step a) into adenosine diphosphate and an inorganic phosphate.
8. The method according to claim 6, wherein a relative activity ratio of γ-glutamylcysteine synthetase to glutathione synthetase is 4:1 to 20:1.
9. The method according to claim 6, wherein a relative activity ratio of the photosynthetic membrane vesicles to γ-glutamylcysteine synthetase to glutathione synthetase is 1:12:1 to 50:12:1.
10. The method according to claim 7, wherein a relative activity ratio of photosynthetic membrane vesicles to bifunctional glutathione synthetase is 10:1 to 500:1.
11. A composition for producing glutathione, comprising: i) photosynthetic membrane vesicles; and ii) enzymes that catalyze glutathione synthesis, wherein the enzymes are selected from the group consisting of γ-glutamylcysteine synthetase (GSH-I), glutathione synthetase (GSH-II) and bifunctional glutathione synthetase (bifunctional γ-glutamylcysteine synthetase/glutathione synthetase, GshF).
12. A system for continuously producing glutathione, comprising: i) photosynthetic membrane vesicles as a means for supplying adenosine triphosphate; ii) enzymes that catalyze glutathione synthesis, wherein the enzymes are selected from the group consisting of γ-glutamylcysteine synthetase (GSH-I), glutathione synthetase (GSH-II) and bifunctional glutathione synthetase (bifunctional γ-glutamylcysteine synthetase/glutathione synthetase, GshF), as a means for catalyzing glutathione synthesis
13. A method of continuously producing glutathione, the method comprising a step of adding glutamate, cysteine and glycine as substrates for producing glutathione to the system according to claim 12.
Description
DESCRIPTION OF DRAWINGS
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MODES OF THE INVENTION
[0053] Hereinafter, the present invention is described in more detail with reference to the following examples. These examples are only intended to explain the present invention more specifically, and it will be apparent to those skilled in the art that the scope of the present invention is not limited by these examples.
EXAMPLES
Example 1: Isolation of Chromatophore Membrane Vesicles
[0054] Chromatophore membrane vesicles are isolated using the method described in Korean Patent Application No. 10-2014-0151907. Rhodobacter sphearoides (Rhodobacter sphearoides 2.4.1, ATCC BAA-808, Cohen-Bazire et al. 1956. J. Cell. Comp. Physiol. 49: 25-68), a type of purple non-sulfur bacteria, was used to isolate chromatophore membrane vesicles. The strain was cultured in Sistrom's minimal medium (Sistrom. 1962. J. Gen. Microbiol. 28: 607-616, Table 1). The culture method is as follows. First, a test tube containing 5 ml of the medium was inoculated with the strain, and was subjected to shaking culture at 30° C. and 250 rpm. When culture absorbance at 660 nm was about 2.0, the medium was subcultured in an 18-ml screw cap test tube to an initial absorbance of 0.05, and then the screw cap test tube was filled with a fresh medium and sealed to block the exposure to oxygen. Culture was performed under photosynthesis conditions. Specifically, the culture was performed for 18 hours in an incubator, wherein culture conditions were set as follows: temperature is maintained at 30° C. and light is irradiated by an incandescent lamp at a luminous intensity of 15 Watts/m.sup.2. After culture, 8 ml of the strain cultured in the 18 ml screw cap test tube was added to a 260 ml transparent bottle, and the remaining volume of the transparent bottle was filled with a fresh medium and sealed. The culture medium was subjected to anaerobic culture, as described above, at a temperature of 30° C. and at a luminous intensity of 15 Watts/m.sup.2 for 18 hours. Thereafter, the process of isolating chromatophore membranes was carried out in an anaerobic chamber (anaerobic chamber, model 10, Coy laboratory product). The gas composition in the anaerobic chamber is 90% nitrogen, 5% carbon dioxide and 5% hydrogen. The Rhodobacter sphearoides strain cultured in the 260 ml transparent bottle was subjected to centrifugation at 7,000 g and 4° C. for 10 minutes, and then a supernatant was discarded and a cell pellet was obtained. The cell pellet was resuspended in 4 ml of a phosphate buffer (10 mM Na.sub.2HPO.sub.4, 2 mM KH.sub.2PO.sub.4, pH 7.6), and a protease inhibitor mixture (protease inhibitor cocktail, Roche) was added thereto according to the manufacturer's instructions. In subsequent procedure, all samples were kept on ice. Next, cell lysis was performed using a sonicator (model VCX130, Sonics & Materials) under the following conditions: ultrasonic irradiation for 2 minutes with 100% amplification and then cooling in ice water for 2 minutes, and repeating this process three times. When irradiating ultrasonic waves, the cell pellets were cooled with ice water to prevent overheating. The lysed cells were subjected to centrifugation at 6,000 g and 4° C. for 10 minutes to obtain a supernatant, and then the supernatant was subjected to centrifugation at 200,000 g and 4° C. for 1 hour using an ultracentrifuge (Optima XE-90, Beckman Coulter). After centrifugation, a supernatant was removed, and a pellet containing chromatophore membrane vesicles was dissolved in 1 ml of a phosphate buffer to perform sucrose-density gradient centrifugation. A sucrose-density gradient was formed in the order of 8 ml of a 60% (w/v, dissolved in a phosphate buffer) sucrose solution, 1 ml of a 40% sucrose solution and 1 ml of a 20% sucrose solution from the bottom layer of an ultracentrifuge tube with a volume of 13.5 ml. 1 ml of the pellet containing chromatophore membrane vesicles was placed on the top layer, and ultracentrifugation was performed at 200,000 g for 4 hours. A reddish brown layer containing chromatophore membrane vesicles was located between a layer of the 20% sucrose solution and a layer of the 40% sucrose solution. The reddish brown layer was separated, and then diluted by addition of the same volume of a phosphate buffer. In addition, kanamycin was added at a concentration of 100 μg/ml to prevent the growth of common contaminants, and a protease inhibitor mixture was added according to the manufacturer's instructions. The mixture was anaerobically sealed and stored at 4° C.
TABLE-US-00001 TABLE 1 Composition of Sistrom's minimal medium for culturing Rhodobacter sphearoides Additives Final Concentration KH.sub.2PO.sub.4 20 mM NaCl 8.5 mM (NH.sub.4).sub.2SO.sub.4 3.78 mM L-Glutamate 0.67 mM L-Aspartic acid 0.25 mM Succinic acid 34 mM Nitrilotriacetic acid 1.05 mM MgCl.sub.2•6H.sub.2O 1.2 mM CaCl.sub.2•2H.sub.2O 0.23 mM FeSO.sub.4•7H.sub.2O 7 μM (NH.sub.4).sub.6Mo.sub.7O.sub.24 0.16 μM EDTA 4.7 μM ZnSO.sub.4•7H.sub.2O 38 μM MnSO.sub.4•H.sub.2O 9.1 μM CuSO.sub.4•5H.sub.2O 1.6 μM Co(NO.sub.3).sub.2•6H.sub.2O 0.85 μM H.sub.3BO.sub.3 1.8 μM Nicotinic acid 8.1 μM Thiamine hydrochloride 1.5 μM Biotin 41 nM
Example 2: Preparation of Genes Encoding Enzymes Involved in Glutathione Synthesis
[0055] To clone genes encoding γ-glutamylcysteine synthetase and glutathione synthetase of overall reaction A (
TABLE-US-00002 TABLE 2 Primers for amplifying gene encoding γ- glutamylcysteine synthetase SEQ ID NO. Direction Sequences 1 gshA-F 5′-AAAAAAGGTCTCTGCGCTTGATCCCGGACG TATCACA-3′ 2 gshA-R 5′-AAAAAAGGTCTCTTATCATCAGGCGTGTTT TTCCAGCC-3′
TABLE-US-00003 TABLE 3 Primers for amplifying gene encoding glutathione synthetase SEQ ID NO. Direction Sequences 3 gshB-F 5′-AAAAAAGGTCTCTAATGATCAAGCTCGGC ATCGT-3′ 4 gshB-R 5′-AAAAAAGGTCTCTGCGCTCTGCTGCTGTA AACGTGCTT-3′
TABLE-US-00004 TABLE 4 Primers for amplifying gene encoding bifunctional glutathione synthetase SEQ ID NO. Direction Sequences 5 gshF-F 5′-AAAAAAGGTCTCAGCGCATGATTATCGAT CGACTGTTAC-3′ 6 gshF-R 5′-AAAAAAGGTCTCGTATCATTATAATTCTG GGAACAGTTTAG-3′
Example 3: Purification of Enzymes that Catalyze Glutathione Synthesis Reaction
[0056] Escherichia coli strains BL21 (DE3) were transformed with the expression vectors prepared in Example 2, and transformed strains overexpressing γ-glutamylcysteine synthetase, glutathione synthetase and bifunctional glutathione synthetase, respectively, were obtained. The same method was used for purifying these enzymes. First, 5 ml of LB (Luria-Bertani) medium containing 50 μg/ml ampicillin was added to a test tube, and the transformed strain was inoculated in the test tube, followed by shaking culture at 250 rpm and 37° C. for 12 hours. The cells, then, were inoculated into a 1 L flask filled with 500 ml LB medium containing 50 μg/ml ampicillin. At the time of inoculation, an initial absorbance at 600 nm was adjusted to 0.05, and then shaking culture was performed at 250 rpm and 37° C. until absorbance reached 0.4. Anhydrotetracycline was added to the culture at a concentration of 0.2 μg/ml and shaking culture was further continued at 250 rpm and 30° C. for about 12 hours. After culture, cells were centrifuged at 4,000 g for 10 minutes, and a cell pellet was obtained, followed by suspension in 10 ml of buffer W (100 mM Tris-HCl, pH 8.0, 150 mM NaCl, 1 mM EDTA). A protease inhibitor mixture (Roche) was added thereto in an amount recommended by the manufacturer, and the cell pellet was lysed using a sonicator (Branson sonifier 250). Sonication was performed on the suspended cell pellet for 5 minutes at the intensity of output 3, followed by cooling in ice water for 5 minutes. This process was repeated three times. After cell lysis, centrifugation was performed at 6,000 g for 10 minutes to separate a supernatant containing water-soluble enzymes, and the enzymes were purified using strep-tag affinity chromatography. The strep-tag affinity chromatography was performed according to the manufacturer (IBA)'s recommended method. The purified enzymes were verified by 10% SDS polyacrylamide gel electrophoresis (
Example 4: Measurement of Adenosine Triphosphate Production Activity of Chromatophore Membrane Vesicles Under Light Irradiation
[0057] The quantification and activity measurement of chromatophore membrane vesicles were carried out according to the method described in Korean Patent Application No. 10-2014-0151907. Chromatophore membrane vesicles were quantified using a bacteriochlorophyll a (bch a) concentration. When measuring adenosine triphosphate (ATP) production activity, chromatophore membrane vesicles were used at a concentration of 0.25-0.5 μg bch a/ml. An appropriate amount of chromatophore membrane vesicles was added to a buffer containing 10 mM sodium phosphate (Na.sub.2HPO.sub.4), 2 mM potassium phosphate (KH.sub.2PO.sub.4), 10 mM magnesium chloride (MgCl.sub.2), and 0.4 mM adenosine diphosphate, and the mixture was allowed to react under anaerobic conditions in which a temperature was maintained at 30° C. and light having a luminous intensity of 15 Watts/m.sup.2 was irradiated by incandescent lamp. The amount of adenosine triphosphate produced over time was measured by an adenosine triphosphate detection kit (Sigma-Aldrich). The activity of chromatophore membrane vesicles was expressed as the amount of adenosine triphosphate produced per unit time (nmole ATP/min).
Example 5: Measurement of Enzyme Activity of γ-Glutamylcysteine Synthetase and Glutathione Synthetase
[0058] To measure enzyme activity of γ-glutamylcysteine synthetase and glutathione synthetase purified in Example 3, a method of measuring adenosine diphosphate formation (Seelig and Meister. 1985. Methods in Enzymol. 113: 379-390) was used. A reaction buffer containing 0.1 mM Tris (Tris-C1, pH 7.6), 10 mM magnesium chloride (MgCl.sub.2), 0.8 mM adenosine triphosphate (ATP), 2 mM phosphoenolpyruvate, 0.2 mM reduced nicotinamide adenine dinucleotide (NADH), 14.3 Unit/ml pyruvate kinase, and 14.3 Unit/ml lactic dehydrogenase was used for activity measurement. When measuring the activity of γ-glutamylcysteine synthetase, 10 mM L-glutamate and 10 mM L-cysteine were added to the reaction buffer. When measuring the activity of glutathione synthetase, 10 mM glycine and 1 mM γ-glutamylcysteine were added to the reaction buffer. The reaction temperature was 30° C. When γ-glutamylcysteine synthetase and glutathione synthetase perform enzymatic reactions, adenosine diphosphate is produced, and at the same time, an amount of reduced nicotinamide adenine dinucleotide (NADH) equivalent to that of the adenosine diphosphate is converted into the oxidized form (NAD.sup.+). Since NADH absorbs light at 340 nm and NAD.sup.+ does not absorb light at 340 nm, the activity of the two enzymes can be determined by measuring the decrease in absorbance at 340 nm over time.
Example 6: Confirmation of Glutathione Production by γ-Glutamylcysteine Synthetase and Glutathione Synthetase
[0059] In this example, it was confirmed that glutathione was produced from L-glutamate, L-cysteine, glycine and adenosine triphosphate by γ-glutamylcysteine synthetase and glutathione synthetase. A reaction buffer containing 10 mM sodium phosphate (Na.sub.2HPO.sub.4), 2 mM potassium phosphate (KH.sub.2PO.sub.4), 10 mM magnesium chloride (MgCl.sub.2), 0.8 mM adenosine triphosphate (ATP), 10 mM L-glutamate, 10 mM L-cysteine, and 10 mM glycine was used. To prevent oxidation of the resulting glutathione, the reaction was performed at 30° C. under anaerobic conditions. A glutathione detection kit (GSH-Glo™ Glutathione Assay, Promega) was used to detect glutathione. The activity of each enzyme was measured using the method described in Example 5, and relative activity of each enzyme was adjusted based on the measured activity.
Example 7: Confirmation of Glutathione Production by Chromatophore Membrane Vesicles, γ-Glutamylcysteine Synthetase and Glutathione Synthetase Under Light Conditions
[0060] In this example, it was confirmed that glutathione was produced by chromatophore membrane vesicles, γ-glutamylcysteine synthetase, and glutathione synthetase in the conditions in which adenosine triphosphate (ATP) was not supplied but light was irradiated. A reaction buffer containing 10 mM sodium phosphate (Na.sub.2HPO.sub.4), 2 mM potassium phosphate (KH.sub.2PO.sub.4), 10 mM magnesium chloride (MgCl.sub.2), 0.4 mM adenosine diphosphate (ADP), 10 mM L-glutamate, 10 mM L-cysteine, and 10 mM glycine was used, and the reaction was performed at 30° C. under anaerobic conditions. An incandescent lamp with a luminous intensity of 15 Watts/m.sup.2 was used as a light source.
Example 8: Measurement of Activity of Bifunctional Glutathione Synthetase on Glutathione Production
[0061] In this example, it was confirmed that glutathione was produced by bifunctional glutathione synthetase in a reaction solution containing L-glutamate, L-cysteine, glycine, and adenosine triphosphate. The composition of the reaction solution was 10 mM sodium phosphate (Na.sub.2HPO.sub.4), 2 mM potassium phosphate (KH.sub.2PO.sub.4), 10 mM magnesium chloride (MgCl.sub.2), 100 mM L-glutamate, 10 mM L-cysteine, 25 mM glycine, and 0.8 mM adenosine triphosphate (ATP). The reaction was performed at 30° C.
Example 9: Confirmation of Glutathione Production by Chromatophore Membrane Vesicles and Bifunctional Glutathione Synthetase Under Light Conditions
[0062] In this example, it was confirmed that glutathione was produced from L-glutamate, L-cysteine, and glycine when chromatophore membrane vesicles and bifunctional glutathione synthetase were used together under conditions in which adenosine diphosphate was added instead of adenosine triphosphate and light was irradiated. 0.4 mM adenosine diphosphate was added in place of 0.8 mM adenosine triphosphate in the reaction solution of Example 8. The reaction was performed under anaerobic conditions in which temperature is maintained at 30° C. and light was irradiated by an incandescent lamp with a luminous intensity of 15 Watts/m.sup.2.
[0063] The present invention has been described in detail with reference to preferred embodiments. It will be apparent to those skilled in the art that the preferred embodiments are only illustrative and that the scope of the present invention is not limited thereto. Accordingly, the actual scope of the present invention will be defined by the appended claims and equivalents thereof.