Method for producing culture product of <i>Lactobacillus plantarum</i>

Abstract

Provided is a method of producing a culture product of a microorganism, for obtaining a culture product excellent in anti-inflammatory property in which a ratio between the production amounts of IL-10 and IL-12 (ratio of IL-10/IL-12) is large. Specifically, provided is a method of producing a culture product of Lactobacillus plantarum, including culturing Lactobacillus plantarum using a medium containing an unsaturated fatty acid ester until a time point at or before an end of a logarithmic growth phase, to thereby obtain a culture product of Lactobacillus plantarum. The unsaturated fatty acid ester is an ester formed through a reaction between a monovalent or polyvalent unsaturated fatty acid and a polyhydric alcohol, or a derivative of the ester. A preferred example of the unsaturated fatty acid ester is a monooleic acid ester.

Claims

1. A method of producing a culture product of Lactobacillus plantarum, comprising culturing Lactobacillus plantarum using a medium containing an effective amount of an unsaturated fatty acid ester to obtain a cultured product of Lactobacillus plantarum having a larger ratio of production amounts of interleukin-10 to production amounts of interleukin-12 compared to another cultured product of Lactobacillus plantarum obtained by culturing the Lactobacillus plantarum in another medium identical to the medium but without the unsaturated fatty acid ester, wherein the culturing is continued for a time period from initiation of the culturing until an end time point, and the end time point is at or before an end of a logarithmic growth phase.

2. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the end time point of the culturing is represented by a time point at which bacterial count of the Lactobacillus plantarum during the logarithmic growth phase reaches a bacterial count that is half as large as a highest bacterial count attainable in the logarithmic growth phase.

3. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the end time point of the culturing is represented by a time point at which a consumption amount of a neutralizer to be used during neutral culture of the Lactobacillus plantarum reaches an amount that is half as large as a total consumption amount.

4. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the unsaturated fatty acid ester is an ester formed through a reaction between a monovalent or polyvalent unsaturated fatty acid and a polyhydric alcohol, or a derivative of the ester.

5. The method of producing a culture product of Lactobacillus plantarum according to claim 4, wherein the monovalent or polyvalent unsaturated fatty acid is a monovalent to trivalent unsaturated fatty acid having 16 to 23 carbon atoms.

6. The method of producing a culture product of Lactobacillus plantarum according to claim 4, wherein the unsaturated fatty acid ester is a monooleic acid ester.

7. The method of producing a culture product of Lactobacillus plantarum according to claim 6, wherein the unsaturated fatty acid ester is a polyglycerol fatty acid ester, a sorbitan fatty acid ester, or a polysorbate.

8. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the medium includes 0.05 wt % or more of the unsaturated fatty acid ester.

9. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the IL-10/IL-12 production amount ratio in the cultured product is larger by 20% or more compared to that obtained in the another cultured product.

10. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the unsaturated fatty acid ester is decaglycerol monooleate.

11. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the unsaturated fatty acid ester is sorbitan monooleate.

12. The method of producing a culture product of Lactobacillus plantarum according to claim 1, wherein the culturing is continued 9 to 11 hours from a starting point of the logarithmic growth phase.

13. A method of producing a culture product of Lactobacillus plantarum, comprising culturing Lactobacillus plantarum using a medium containing an effective amount of an unsaturated fatty acid ester for increasing production amounts of interleukin-10 relative to production amounts of interleukin-12 in a resulting cultured product of the Lactobacillus plantarum, wherein the culturing is continued for a time period from initiation of the culturing until an end time point which is at or before an end of a logarithmic growth phase.

14. The method of producing a culture product of Lactobacillus plantarum according to claim 13, wherein the end time point of the culturing is represented by a time point at which bacterial count of the Lactobacillus plantarum during the logarithmic growth phase reaches a bacterial count that is half as large as a highest bacterial count attainable in the logarithmic growth phase.

15. The method of producing a culture product of Lactobacillus plantarum according to claim 13, wherein the effective amount of the unsaturated fatty acid ester is 0.001 wt % or more, and the end time point of the culturing of the logarithmic growth phase is represented by a time point at which a consumption amount of a neutralizer to be used during neutral culture of the Lactobacillus plantarum reaches an amount that is half as large as a total consumption amount.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) FIG. 1 is a graph for showing the production amounts of IL-10 in cases in which Lactobacillus plantarum OLL2712 is cultured using media containing unsaturated fatty acid esters (4 kinds), a medium containing a saturated fatty acid ester (for comparison; 1 kind), or a medium containing no unsaturated fatty acid ester and no saturated fatty acid ester (for a control; 1 kind).

(2) FIG. 2 is a graph for showing the production amounts of IL-12 in the culture shown in FIG. 1.

(3) FIG. 3 is a graph for showing IL-10/IL-12 production amount ratios in the culture shown in FIG. 1.

(4) FIG. 4 is a graph for showing the production amounts of IL-10 in cases in which Lactobacillus plantarum OLL2712 is cultured using media containing substances other than unsaturated fatty acid esters (such as sodium ascorbate; 13 kinds) or a medium containing none of the substances (for a control; 1 kind).

(5) FIG. 5 is a graph for showing the production amounts of IL-12 in the culture shown in FIG. 4.

(6) FIG. 6 is a graph for showing IL-10/IL-12 production amount ratios in the culture shown in FIG. 4.

(7) FIG. 7 is a graph for showing temporal changes in production amount of IL-10 during a culture period in cases in which Lactobacillus plantarum OLL2712 is cultured using a medium containing decaglycerol monooleate as one kind of unsaturated fatty acid ester (Q-17S(+)) or a medium containing no decaglycerol monooleate (Q-17S(−)).

(8) FIG. 8 is a graph for showing temporal changes in production amount of IL-12 during the culture period in the culture shown in FIG. 7.

(9) FIG. 9 is a graph for showing temporal changes in IL-10/IL-12 production amount ratio during the culture period in the culture shown in FIG. 7.

(10) FIG. 10 is a graph for showing temporal changes in production amount of IL-10 during a culture period in cases in which Lactobacillus plantarum OLL2770 is cultured using a medium containing decaglycerol monooleate as one kind of unsaturated fatty acid ester (Q-17S(+)) or a medium containing no decaglycerol monooleate (Q-17S(−)).

(11) FIG. 11 is a graph for showing temporal changes in production amount of IL-12 during the culture period in the culture shown in FIG. 10.

(12) FIG. 12 is a graph for showing temporal changes in IL-10/IL-12 production amount ratio during the culture period in the culture shown in FIG. 10.

DESCRIPTION OF EMBODIMENTS

(13) A method of producing a culture product of Lactobacillus plantarum of the present invention includes culturing Lactobacillus plantarum using a medium containing an unsaturated fatty acid ester until a time point at or before an end of a logarithmic growth phase, to thereby obtain a culture product of Lactobacillus plantarum.

(14) Any strain may be used as Lactobacillus plantarum (hereinafter sometimes abbreviated as L. plantarum).

(15) Examples of the strain of Lactobacillus plantarum include OLL2712 (accession number: FERM BP-11262) and OLL2770.

(16) In the present invention, the fatty acid ester to be used is one (i.e. unsaturated fatty acid ester) having a chemical structure having one or more double bonds (i.e. unsaturated structure) in the molecule. When a saturated fatty acid ester is used, a ratio between the production amounts of IL-10 and IL-12 (IL-10/IL-12) is decreased as compared to the case of using the unsaturated fatty acid ester.

(17) Examples of the unsaturated fatty acid ester include: an ester formed through a reaction between a monovalent or polyvalent unsaturated fatty acid and a polyhydric alcohol; and a derivative of the ester.

(18) Examples of the monovalent unsaturated fatty acid include a monovalent unsaturated fatty acid having 16 to 23 carbon atoms. Examples of the monovalent unsaturated fatty acid having 16 to 23 carbon atoms include oleic acid (carbon number: 16), vaccenic acid (carbon number: 16), palmitoleic acid (carbon number: 19), and nervonic acid (carbon number: 23).

(19) Examples of the polyvalent unsaturated fatty acid include a divalent to tetravalent unsaturated fatty acid having 16 to 23 carbon atoms. Examples of the divalent to tetravalent unsaturated fatty acid having 16 to 23 carbon atoms include linoleic acid (divalent, carbon number: 16), 8,11-eicosadienoic acid (divalent, carbon number: 19), linolenic acid (trivalent, carbon number: 16), eleostearic acid (trivalent, carbon number: 16), 5,8,11-eicosatrienoic acid (trivalent, carbon number: 18), and arachidonic acid (tetravalent, carbon number: 18).

(20) Examples of the polyhydric alcohol include polyglycerol and sorbitan. Examples of the polyglycerol include polyglycerol obtained by bonding 3 to 15 glycerols.

(21) Examples of the polyglycerol obtained by bonding 3 to 15 glycerols include triglycerol, tetraglycerol, pentaglycerol, hexaglycerol, heptaglycerol, octaglycerol, nonaglycerol, decaglycerol, undecaglycerol, and dodecaglycerol.

(22) Examples of the derivative of the ester formed through a reaction between a monovalent or polyvalent unsaturated fatty acid and a polyhydric alcohol include a polysorbate.

(23) The polysorbate is a product obtained by condensing ethylene oxide with a sorbitan fatty acid formed through a reaction between a monovalent or polyvalent unsaturated fatty acid and sorbitan. In this case, the number of ethylene oxide molecules to be condensed is, for example, from 15 to 25.

(24) In the present invention, a preferred example of the unsaturated fatty acid ester is a monooleic acid ester (e.g., one formed through a reaction between one molecule of oleic acid and one molecule of polyglycerol, sorbitan, or the polysorbate).

(25) From the viewpoint of increasing the ratio between the production amounts of IL-10 and IL-12 (IL-10/IL-12), the concentration of the unsaturated fatty acid ester in the medium is preferably 0.001 wt % or more, more preferably 0.01 wt % or more, still more preferably 0.02 wt % or more, still more preferably 0.03 wt % or more, still more preferably 0.04 wt % or more, particularly preferably 0.05 wt % or more.

(26) From the viewpoint of avoiding an increase in cost of the culture due to an increase in amount of the unsaturated fatty acid ester, the concentration of the unsaturated fatty acid ester in the medium is preferably 1 wt % or less, more preferably 0.5 wt % or less, still more preferably 0.3 wt % or less, still more preferably 0.1 wt % or less, particularly preferably 0.08 wt % or less.

(27) General components used in culture of lactic acid bacteria may be used as the components of the medium other than the unsaturated fatty acid ester.

(28) In the present invention, Lactobacillus plantarum is cultured until a time point at or before the end of the logarithmic growth phase. When the culture is performed until a time point beyond the end of the logarithmic growth phase, the production amount of IL-10 and the ratio between the production amounts of IL-10 and IL-12 (IL-10/IL-12) are decreased, with the result that the culture product of interest in the present invention cannot be obtained.

(29) The end of the logarithmic growth phase is represented by, for example, the following (a) or (b). (a) A time point at which a bacterial count during culture of the Lactobacillus plantarum reaches a bacterial count that is half as large as a highest attainable bacterial count (b) A time point at which a consumption amount of a neutralizer to be used during neutral culture of the Lactobacillus plantarum reaches an amount that is half as large as a total consumption amount

(30) In the (a), the highest attainable bacterial count refers to the highest (i.e. maximum) bacterial count that is presumed to be attainable when the culture is continued beyond the end of the logarithmic growth phase.

(31) In the (b), the neutral culture refers to (i.e. means) culture performed while a pH is kept to a certain range by adding a neutralizer (e.g., sodium hydroxide) to a culture broth in order to keep bacterial growth in an optimum state.

(32) In addition, the total consumption amount of the neutralizer to be used during the neutral culture refers to (i.e. means) the total amount of the neutralizer added in the case where the neutralizer is added so that the pH may fall within the certain range from the start of the culture until the highest attainable bacterial count is obtained.

(33) The “highest attainable bacterial count” in the (a) and the “total consumption amount” in the (b) may be determined in advance by, for example, performing culture under exactly the same conditions (e.g., the kind of the strain of Lactobacillus plantarum, the kinds of the unsaturated fatty acid ester and the other medium components, and the temperature during the culture) as those of an example of the production method of the present invention prior to carrying out the example.

(34) The count of L. plantarum may be represented, for example, as a measured value of the turbidity of a suspension containing the culture product of L. plantarum. Examples of means for measuring the turbidity include a spectrophotometer.

(35) The length of the logarithmic growth phase of L. plantarum varies depending on the temperature, the component composition of the medium, and the like, but is, for example, from 9 hours to 11 hours.

(36) The culture product of Lactobacillus plantarum produced by the production method of the present invention may be used, for example, as an active ingredient of an anti-inflammatory agent.

(37) The culture product can be distinguished from a culture product produced by a related-art production method (i.e. a related-art product or a conventional product) in that the ratio between the production amounts of IL-10 and IL-12 (IL-10/IL-12 production amount ratio) is larger than the ratio in the related-art product.

(38) In the culture product produced by the production method of the present invention, the IL-10/IL-12 production amount ratio is larger preferably by 20% or more, more preferably by 25% or more, particularly preferably by 30% or more than the ratio in the case of using a medium having (i.e. including) no unsaturated fatty acid ester blended therein.

(39) Next, a method of selecting a strain of Lactobacillus plantarum of the present invention is described.

(40) The method of selecting a strain of Lactobacillus plantarum of the present invention (hereinafter sometimes abbreviated as selection method of the present invention) includes: culturing each of a plurality of strains of Lactobacillus plantarum using a medium containing an unsaturated fatty acid ester (e.g., a monooleic acid ester) until a time point at or before an end of a logarithmic growth phase, to thereby obtain a culture product of each of the strains; subjecting the obtained culture product of each of the strains to an evaluation of production-inducing activity of interleukin-10; and selecting a strain having a large degree of an anti-inflammatory action from the plurality of strains based on a result of the evaluation.

(41) The selection method of the present invention may include subjecting the obtained culture product of each of the strains to an evaluation of production-inducing activity of interleukin-12 in addition to the evaluation of production-inducing activity of interleukin-10, in which selecting a strain having a large degree of an anti-inflammatory action from the plurality of strains is performed based on results of the evaluations.

(42) The production-inducing activity of each of interleukin-12 and interleukin-10 may be evaluated by, for example, an immunoassay (e.g., ELISA; Enzyme-linked immuno-sorbent assay).

EXAMPLES

(43) [1. Influence of Presence or Absence of Unsaturated Fatty Acid Ester in Medium on IL-10/IL-12 Production Amount Ratio]

(44) L. plantarum OLL2712 was cultured using media having (i.e. including) vitamins, minerals, saturated fatty acid esters, or unsaturated fatty acid esters (i.e. monooleic acid esters) blended therein, and the influence of each of those components on anti-inflammatory activity was investigated.

(45) [Experiment Method 1-1] Preparation Method for L. plantarum OLL2712

(46) L. plantarum OLL2712 was subjected to static culture (at 37° C. for 18 hours twice) using MRS medium (manufactured by Becton, Dickinson and Company) to prepare an activated culture broth of L. plantarum OLL2712. Then, with the use of whey degradation medium, the activated culture broth of L. plantarum OLL2712 was added in an amount of 1 wt % with respect to 100 wt % of the whey degradation medium, and then subjected to static culture (at 37° C. for 9 hours) to prepare a culture broth of L. plantarum OLL2712.

(47) In this case, the composition (weight basis) of the whey degradation medium contains: 6.25% of whey powder; whey protein concentrate (WPC80; protein content: 80%); 0.12% of protease; 0.50% of yeast extract; 0.50% of fish meat extract; 0.01% of manganese sulfate tetrahydrate; 0.05% (added later; details are described later) or 0% (for a control) of another auxiliary material; and 90.82% or 90.87% (for a control) of distilled water.

(48) After that, the culture broth of L. plantarum OLL2712 was subjected to centrifugal treatment (8,000×g, 15 minutes) to collect bacterial cells of L. plantarum OLL2712. Then, thebacterial cells of L. plantarum OLL2712 were washed twice with physiological saline, and then the bacterial cells of L. plantarum OLL2712 were washed once with distilled water. After that, the resultant bacterial cells were suspended in distilled water to prepare a suspension of L. plantarum OLL2712. Subsequently, the suspension of L. plantarum OLL2712 was subjected to heat treatment (at 75° C. for 60 minutes), and then subjected to freeze-drying treatment (FD) to prepare freeze-dried bacterial cells of L. plantarum OLL2712.

(49) After that, the freeze-dried bacterial cells of L. plantarum OLL2712 were suspended in phosphate buffered saline (PBS), and then diluted to 10 mg/mL with a medium for cell culture to prepare a dilution of L. plantarum OLL2712.

(50) Here, the above-mentioned whey degradation medium (without the above-mentioned auxiliary material) was blended with an auxiliary material shown below (any one of 18 kinds in total) in an amount of 0.05 wt % to prepare 18 kinds in total of whey degradation media. After that, through treatments under conditions similar to those described above, several kinds of dilutions of L. plantarum OLL2712 were prepared.

(51) [Kind of Auxiliary Material for Whey Degradation Medium]

(52) (a) Unsaturated fatty acid ester: 4 kinds (a-1) Decaglycerol monooleate: Sunsoft Q-17S (product name), hydrophilic, manufactured by Taiyo Kagaku Co., Ltd. (a-2) Pentaglycerol monooleate: Sunsoft A-171E (product name), hydrophilic, manufactured by Taiyo Kagaku Co., Ltd. (a-3) Sorbitan monooleate: Sunsoft No. 81S (product name), lipophilic, manufactured by Taiyo Kagaku Co., Ltd. (a-4) Polyoxyethylene sorbitan monooleate: Tween 80 (product name), hydrophilic, manufactured by Wako Pure Chemical Industries, Ltd. (b) Saturated fatty acid ester: 1 kind (b-1) Decaglycerol monostearate: Sunsoft Q-18S (product name), amphiphilic, manufactured by Taiyo Kagaku Co., Ltd. (c) Vitamin: 9 kinds (sodium ascorbate, thiamine hydrochloride, riboflavin, nicotinic acid, nicotinamide, calcium pantothenate, pyridoxine hydrochloride, biotin, and folic acid) (d) Mineral: 4 kinds (magnesium sulfate, calcium chloride, iron sulfate, and ferric ammonium sulfate)

(53) [Experiment Method 1-2] Evaluation Method for Production-Inducing Activity of IL-10 and IL-12 in Immune Cells

(54) Only undifferentiated dendritic cells were separated from the bone marrow of an 8-week-old male BALB/c mouse (Japan SLC, Inc.) using an automated magnetic cell separator (auto MACS; manufactured by Miltenyi Biotec). Then, the undifferentiated dendritic cells were cultured (at 37° C. under a CO.sub.2 (5%) environment for 8 days) using RPMI medium (manufactured by Invitrogen) containing Granulocyte Macrophage Colony-Stimulating Factor (hereinafter abbreviated as GM-CSF) to be sufficiently differentiated. Thus, bone marrow-derived dendritic cells (BMDC; immune cells) were prepared.

(55) After that, the dendritic cells (BMDC) were collected and seeded to a 48-well plate at a density of 2.5×10.sup.5 cells/well, and then the L. plantarum OLL2712 cultured in any of the various whey media described above was added at a dry weight of 50 μg/mL. Then, the 48-well plate was incubated (at 37° C. under a CO.sub.2 (5%) environment for 24 hours) using RPMI medium containing GM-CSF, and then the resultant culture supernatant was collected.

(56) Then, the IL-10 concentration of the culture supernatant was measured using “Mouse IL-10 ELISA Set” (manufactured by Becton, Dickinson and Company), and the IL-12 concentration of the culture supernatant was measured using “Mouse IL-12 (p70) ELISA Set” (manufactured by Becton, Dickinson and Company). Here, for the IL-12 concentration, an activated IL-12 (p70) concentration was measured.

(57) [Experimental Results 1] Evaluation Results of Production-inducing Activity of IL-10 and IL-12 in Immune Cells

(58) The results of the above-mentioned experiment (i.e. mean and standard deviation of four times of the experiment, and the like) are shown in Table 1 to Table 6 and FIG. 1 to FIG. 6.

(59) In Table 1 to Table 3 (FIG. 1 to FIG. 3), the results of the case of using an unsaturated fatty acid ester (any one of 4 kinds) or a saturated fatty acid ester (1 kind; Q-18S) as an auxiliary material, and the results of the case of using no auxiliary material (Control) are shown. In Table 4 to Table 6 (FIG. 4 to FIG. 6), the results of the case of using a vitamin (any one of 9 kinds) or a mineral (anyone of 4 kinds) as an auxiliary material, and the results of the case of using no auxiliary material (Control) are shown.

(60) TABLE-US-00001 TABLE 1 IL-10 production amount (unit: pg/mL) Product name Kind of auxiliary of auxiliary Standard Standard material material Mean deviation error Not used (Control) — 3,122 316 158 Unsaturated fatty Q-17S 2,880 158 79 acid ester Saturated fatty Q-18S 3,157 303 152 acid ester Unsaturated fatty A171E 3,128 95 48 acid ester Unsaturated fatty No. 81S 3,514 114 57 acid ester Unsaturated fatty Tween 80 3,146 277 139 acid ester

(61) TABLE-US-00002 TABLE 2 IL-12 (p70) production amount (unit: pg/mL) Product name Kind of auxiliary of auxiliary Standard Standard material material Mean deviation error Not used (Control) — 312 15 8 Unsaturated fatty Q-17S 91 8 4 acid ester Saturated fatty Q-18S 248 21 10 acid ester Unsaturated fatty A171E 106 11 6 acid ester Unsaturated fatty No. 81S 96 13 6 acid ester Unsaturated fatty Tween 80 104 7 4 acid ester

(62) TABLE-US-00003 TABLE 3 IL-10/IL-12 (p70) production amount ratio Product name Kind of auxiliary of auxiliary Standard Standard material material Mean deviation error Not used (Control) — 10 1 1 Unsaturated fatty Q-17S 32 2 1 acid ester Saturated fatty Q-18S 13 1 0 acid ester Unsaturated fatty A171E 30 3 1 acid ester Unsaturated fatty No. 81S 37 6 3 acid ester Unsaturated fatty Tween 80 30 4 2 acid ester

(63) It was able to be confirmed from Table 1 (FIG. 1) that, even when L. plantarum OLL2712 was cultured in the whey degradation medium having a fatty acid ester (unsaturated or saturated) blended therein, the production-inducing activity of IL-10 in the immune cells was not improved as compared to the control (Control).

(64) It was able to be confirmed from Table 2 (FIG. 2) that: when L. plantarum OLL2712 was cultured in the whey degradation medium having decaglycerol monostearate blended therein as a saturated fatty acid ester out of the fatty acid esters, the production-inducing activity of IL-12 in the immune cells was not significantly reduced as compared to the control (Control); and when L. plantarum OLL2712 was cultured in the whey degradation medium having an unsaturated fatty acid ester (any one of 4 kinds) blended therein out of the fatty acid esters, the production-inducing activity of IL-12 in the immune cells was significantly reduced as compared to the control (Control).

(65) It was able to be confirmed from Table 3 (FIG. 3) that, when L. plantarum OLL2712 was cultured in the whey degradation medium having an unsaturated fatty acid ester (any one of 4 kinds) blended therein, the IL-10/IL-12 production ratio of the immune cells was significantly increased as compared to the control (Control) or the saturated fatty acid ester.

(66) TABLE-US-00004 TABLE 4 IL-10 production amount (unit: pg/mL) Kind of auxiliary material Mean Standard deviation Not used (Control) 3,800 80 Sodium ascorbate 2,967 76 Thiamine hydrochloride 3,697 189 Riboflavin 3,683 244 Nicotinic acid 3,519 223 Nicotinamide 3,198 114 Calcium pantothenate 3,184 219 Pyridoxine hydrochloride 3,172 259 Biotin 3,257 236 Folic acid 3,091 97 Magnesium sulfate 3,810 105 Calcium chloride 3,057 150 Iron sulfate 2,751 169 Ferric ammonium sulfate 3,047 199

(67) TABLE-US-00005 TABLE 5 IL-12 (p70) production amount (unit: pg/mL) Kind of auxiliary material Mean Standard deviation Not used (Control) 160 9 Sodium ascorbate 113 7 Thiamine hydrochloride 185 3 Riboflavin 238 35 Nicotinic acid 245 16 Nicotinamide 166 4 Calcium pantothenate 194 15 Pyridoxine hydrochloride 173 6 Biotin 147 9 Folic acid 150 6 Magnesium sulfate 135 7 Calcium chloride 139 14 Iron sulfate 102 4 Ferric ammonium sulfate 112 13

(68) TABLE-US-00006 TABLE 6 IL-10/IL-12 (p70) production amount ratio Kind of auxiliary material Mean Standard deviation Not used (Control) 24 2 Sodium ascorbate 26 2 Thiamine hydrochloride 20 1 Riboflavin 16 3 Nicotinic acid 14 1 Nicotinamide 19 1 Calcium pantothenate 16 1 Pyridoxine hydrochloride 18 2 Biotin 22 2 Folic acid 21 1 Magnesium sulfate 28 1 Calcium chloride 22 2 Iron sulfate 27 1 Ferric ammonium sulfate 27 4

(69) It was able to be confirmed from Table 4 (FIG. 4) that, even when L. plantarum OLL2712 was cultured in the whey degradation medium having a vitamin or a mineral blended therein, the production-inducing activity of IL-10 in the immune cells was not significantly changed as compared to the control (Control).

(70) It was able to be confirmed from Table 5 (FIG. 5) that, even when L. plantarum OLL2712 was cultured in the whey degradation medium having a vitamin or a mineral blended therein, the production-inducing activity of IL-12 in the immune cells was not significantly changed as compared to the control (Control).

(71) It was able to be confirmed from Table 6 (FIG. 6) that, even when L. plantarum OLL2712 was cultured in the whey degradation medium having a vitamin or a mineral blended therein, the IL-10/IL-12 production ratio of the immune cells was not significantly changed as compared to the control (Control).

(72) It was able to be confirmed from the above-mentioned results that: when L. plantarum OLL2712 was cultured using the medium having the unsaturated fatty acid ester blended therein, the IL-10/IL-12 production ratio was remarkably increased, and hence, for example, an improvement in anti-inflammatory activity was likely to be achieved; and with a substance (i.e. saturated fatty acid ester, vitamin, or mineral) other than the unsaturated fatty acid ester, such effect (e.g., a remarkable increase in IL-10/IL-12 production ratio) was not likely to be achieved.

(73) [2. Influence of Change in Length of Culture Period on IL-10/IL-12 Production Amount Ratio (Case of using L. plantarum OLL2712)]

(74) [Experiment Method 2-1] Preparation Method for L. plantarum OLL2712

(75) An activated culture broth of L. plantarum OLL2712 was prepared in the same manner as in the experiment method 1-1. Then, with the use of the same medium as the whey degradation medium used in the experiment method 1-1, the activated culture broth of L. plantarum OLL2712 was added at 4 wt %, and then subjected to stirred culture (at 33° C., under ventilation with N.sub.2 at the upper surface, and at 200 rpm) while the pH was controlled to 5.8 using K.sub.2CO.sub.3 (40 wt %) as a neutralizer to prepare a high-density culture broth of L. plantarum OLL2712. Culture conditions for the stirred culture were investigated in advance, and set to culture conditions under which the highest bacterial cell density was obtained.

(76) After that, freeze-dried bacterial cells of L. plantarum OLL2712 were prepared in the same manner as in the experiment method 1-1.

(77) After that, the freeze-dried bacterial cells of L. plantarum OLL2712 were suspended in phosphate buffered saline (PBS), and then diluted to 10 mg/mL with a medium for cell culture to prepare a dilution of L. plantarum OLL2712.

(78) [Experiment Method 2-2] Evaluation Method for Production-Inducing Activity of IL-10 and IL-12 in Immune Cells

(79) Production-inducing activity of IL-10 and IL-12 in immune cells was evaluated in the same manner as in the experiment method 1-2 using the whey degradation medium prepared in the experiment method 1-1 that contained decaglycerol monooleate (Sunsoft Q-17S (product name)) as an auxiliary material or contained no auxiliary material.

(80) In this case, the production-inducing activity of IL-10 and IL-12 in the immune cells was evaluated at each of time points in the middle period of the logarithmic growth phase (4 hours after the starting point of the logarithmic growth phase), the latter period of the logarithmic growth phase (8 hours after the starting point of the logarithmic growth phase), the initial period of the stationary phase (12 hours after the starting point of the logarithmic growth phase), and the middle period of the stationary phase (16 hours after the starting point of the logarithmic growth phase).

(81) The end of the logarithmic growth phase in this culture was a time point after a lapse of 10 hours from the starting point of the logarithmic growth phase (i.e. time point at which a bacterial count that was half as large as the highest attainable bacterial count was attained).

(82) [Experimental Results 2] Evaluation Results of Production-Inducing Activity of IL-10 and IL-12 in Immune Cells

(83) The results of the above-mentioned experiment (i.e. mean and standard deviation of four times of the experiment) are shown in Table 7 to Table 9 and FIG. 7 to FIG. 9.

(84) TABLE-US-00007 TABLE 7 IL-10 production amount (unit: pg/mL) Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 7 growth phase (hr) Mean deviation Not containing Q-17S(−) 4 1,897 119 unsaturated) 8 1,938 171 fatty acid 12 965 13 ester (Q-17S) 16 1,159 142 Containing Q-17S(+) 4 2,276 60 unsaturated 8 2,276 145 fatty acid 12 557 17 ester (Q-17S) 16 709 29

(85) TABLE-US-00008 TABLE 8 IL-12 (p70) production amount (unit: pg/mL) Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 8 growth phase (hr) Mean deviation Not containing Q-17S(−) 4 62 5 unsaturated 8 63 4 fatty acid 12 60 2 ester (Q-17S) 16 54 5 Containing Q-17S(+) 4 45 4 unsaturated 8 45 1 fatty acid 12 61 2 ester (Q-17S) 16 51 5

(86) TABLE-US-00009 TABLE 9 IL-10/IL-12 (p70) production amount ratio Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 9 growth phase (hr) Mean deviation Not containing Q-17S(−) 4 31 2 unsaturated 8 31 2 fatty acid 12 16 1 ester (Q-17S) 16 21 2 Containing Q-17S(+) 4 51 4 unsaturated 8 50 5 fatty acid 12 9 0 ester (Q-17S) 16 14 2

(87) It was able to be confirmed from Table 7 (FIG. 7) that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours), the production-inducing activity of IL-10 in the immune cells was improved as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours).

(88) In addition, it was able to be confirmed that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours), the production-inducing activity of IL-10 in the immune cells was reduced as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours).

(89) It was able to be confirmed from Table 8 (FIG. 8) that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours), the production-inducing activity of IL-12 in the immune cells was reduced as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours).

(90) In addition, it was able to be confirmed that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours), the production-inducing activity of IL-12 in the immune cells was not changed as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours).

(91) It was able to be confirmed from Table 9 (FIG. 9) that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours), the IL-10/IL-12 production ratio of the immune cells was increased as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (4 hours, 8 hours).

(92) In addition, it was able to be confirmed that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours), the IL-10/IL-12 production ratio of the immune cells was reduced as compared to the case in which L. plantarum OLL2712 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (12 hours, 18 hours).

(93) It was able to be confirmed from the foregoing that, when L. plantarum OLL2712 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein and the culture was ended at a time point in the range of the logarithmic growth phase instead of being continued until a time point in the range of the stationary phase, the IL-10/IL-12 production ratio was remarkably increased, and hence an improvement in anti-inflammatory activity was likely to be achieved.

(94) [3. Influence of Change in Length of Culture Period on IL-10/IL-12 Production Amount Ratio (Case of using L. plantarum OLL2770)]

(95) An experiment was performed in the same manner as in the section “2. Influence of Change in Length of Culture Period on IL-10/IL-12 Production Amount Ratio (Case of using L. plantarum OLL2712)” except that: L. plantarum OLL2770 was used in place of L. plantarum OLL2712; and the time points at which the production-inducing activity of IL-10 and IL-12 in the immune cells was measured were changed from the four time points to two time points in the middle period of the logarithmic growth phase (i.e. 5 hours after the start of the culture) and the middle period of the stationary phase (i.e. 16 hours after the start of the culture).

(96) The end of the logarithmic growth phase in this culture was a time point after a lapse of 7 hours from the start of the culture (i.e. time point at which the consumption amount of the neutralizer reached an amount that was half as large as the total consumption amount).

(97) The results of the above-mentioned experiment (i.e. mean and standard deviation of four times of the experiment) are shown in Table 10 to Table 12 and FIG. 10 to FIG. 12.

(98) TABLE-US-00010 TABLE 10 IL-10 production amount (unit: pg/mL) Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 10 growth phase (hr) Mean deviation Not containing Q-17S(−) 5 1,304 127 unsaturated 16 745 43 fatty acid ester (Q-17S) Containing Q-17S(+) 5 1,909 49 unsaturated 16 641 30 fatty acid ester (Q-17S)

(99) TABLE-US-00011 TABLE 11 IL-12 (p70) production amount (unit: pg/mL) Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 11 growth phase (hr) Mean deviation Not containing Q-17S(−) 5 94 3 unsaturated 16 83 2 fatty acid ester (Q-17S) Containing Q-17S(+) 5 80 4 unsaturated 16 94 8 fatty acid ester (Q-17S)

(100) TABLE-US-00012 TABLE 12 IL-10/IL-12 (p70) production amount ratio Elapsed time from Represen- starting point of tation in logarithmic Standard FIG. 12 growth phase (hr) Mean deviation Not containing Q-17S(−) 5 14 1 unsaturated 16 9 0 fatty acid ester (Q-17S) Containing Q-17S(+) 5 24 2 unsaturated 16 7 0 fatty acid ester (Q-17S)

(101) It was able to be confirmed from Table 10 (FIG. 10) that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours), the production-inducing activity of IL-10 in the immune cells was improved as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours).

(102) In addition, it was able to be confirmed that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (16 hours), the production-inducing activity of IL-10 in the immune cells was not changed as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (16 hours).

(103) It was able to be confirmed from Table 11 (FIG. 11) that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours), the production-inducing activity of IL-12 in the immune cells was significantly reduced as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours).

(104) In addition, it was able to be confirmed that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (16 hours), the production-inducing activity of IL-12 in the immune cells was not changed as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (16 hours).

(105) It was able to be confirmed from Table 12 (FIG. 12) that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours), the IL-10/IL-12 production ratio of the immune cells was increased as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the logarithmic growth phase (5 hours).

(106) In addition, it was able to be confirmed that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein until the stationary phase (16 hours), the IL-10/IL-12 production ratio of the immune cells was significantly reduced as compared to the case in which L. plantarum OLL2770 was cultured in the whey degradation medium having no unsaturated fatty acid ester blended therein until the stationary phase (16 hours).

(107) It was able to be confirmed from the foregoing that, when L. plantarum OLL2770 was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein and the culture was ended at a time point in the range of the logarithmic growth phase (5 hours) instead of being continued until a time point in the range of the stationary phase (16 hours), the IL-10/IL-12 production ratio was increased, and hence an improvement in anti-inflammatory activity was likely to be achieved.

(108) Therefore, the following was able to be confirmed to be common to L. plantarum without the influence of the kind of L. plantarum: when L. plantarum was cultured in the whey degradation medium having the unsaturated fatty acid ester blended therein and the culture was ended at a time point in the range of the logarithmic growth phase instead of being continued until a time point in the range of the stationary phase, the IL-10/IL-12 production ratio was increased, and hence an improvement in anti-inflammatory activity was likely to be achieved.