WO2019131869A1 - Food sterilization method - Google Patents
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- WO2019131869A1 WO2019131869A1 PCT/JP2018/048121 JP2018048121W WO2019131869A1 WO 2019131869 A1 WO2019131869 A1 WO 2019131869A1 JP 2018048121 W JP2018048121 W JP 2018048121W WO 2019131869 A1 WO2019131869 A1 WO 2019131869A1
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- sugar
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- 238000000034 method Methods 0.000 title claims abstract description 74
- 235000013305 food Nutrition 0.000 title claims abstract description 43
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 42
- 238000004659 sterilization and disinfection Methods 0.000 title abstract description 28
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 153
- 239000000203 mixture Substances 0.000 claims abstract description 67
- 235000000346 sugar Nutrition 0.000 claims abstract description 22
- 150000007524 organic acids Chemical class 0.000 claims abstract description 18
- 235000015203 fruit juice Nutrition 0.000 claims abstract description 17
- 235000013399 edible fruits Nutrition 0.000 claims abstract description 12
- 235000013311 vegetables Nutrition 0.000 claims abstract description 4
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 81
- 229930006000 Sucrose Natural products 0.000 claims description 26
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 26
- 239000005720 sucrose Substances 0.000 claims description 26
- 229930091371 Fructose Natural products 0.000 claims description 7
- 239000005715 Fructose Substances 0.000 claims description 7
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 claims description 7
- 235000015165 citric acid Nutrition 0.000 description 26
- 230000014759 maintenance of location Effects 0.000 description 22
- 230000000844 anti-bacterial effect Effects 0.000 description 20
- 230000008569 process Effects 0.000 description 20
- 238000005259 measurement Methods 0.000 description 19
- 238000002156 mixing Methods 0.000 description 16
- 238000007710 freezing Methods 0.000 description 14
- 230000008014 freezing Effects 0.000 description 14
- 239000000523 sample Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 11
- 241000894006 Bacteria Species 0.000 description 10
- 244000005700 microbiome Species 0.000 description 10
- 239000000047 product Substances 0.000 description 9
- 238000011081 inoculation Methods 0.000 description 8
- 239000007791 liquid phase Substances 0.000 description 8
- 239000008223 sterile water Substances 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 6
- 235000013334 alcoholic beverage Nutrition 0.000 description 5
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 235000005979 Citrus limon Nutrition 0.000 description 4
- 244000131522 Citrus pyriformis Species 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 235000015201 grapefruit juice Nutrition 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012470 diluted sample Substances 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000002054 inoculum Substances 0.000 description 2
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- 235000005985 organic acids Nutrition 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 229920001817 Agar Polymers 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- 240000000560 Citrus x paradisi Species 0.000 description 1
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 206010016952 Food poisoning Diseases 0.000 description 1
- 208000019331 Foodborne disease Diseases 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000010233 benzoic acid Nutrition 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- RBHJBMIOOPYDBQ-UHFFFAOYSA-N carbon dioxide;propan-2-one Chemical compound O=C=O.CC(C)=O RBHJBMIOOPYDBQ-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000012488 sample solution Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000001384 succinic acid Substances 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B2/00—Preservation of foods or foodstuffs, in general
- A23B2/70—Preservation of foods or foodstuffs, in general by treatment with chemicals
- A23B2/725—Preservation of foods or foodstuffs, in general by treatment with chemicals in the form of liquids or solids
- A23B2/729—Organic compounds; Microorganisms; Enzymes
- A23B2/742—Organic compounds containing oxygen
- A23B2/746—Organic compounds containing oxygen with singly-bound oxygen
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof containing fruit or vegetable juices
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12G—WINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
- C12G3/00—Preparation of other alcoholic beverages
- C12G3/04—Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs
Definitions
- the present invention relates to a method of sterilizing food.
- Food and drink generally cause problems such as food poisoning due to the contamination of harmful microorganisms.
- unintended changes in the flavor and aroma of the product may occur due to the occurrence of unintended fermentation by the producer due to the action of microorganisms.
- the internal pressure of the container is increased by carbon dioxide generated during fermentation, which may lead to breakage of the container. Therefore, in the manufacture of products such as food and drink, a method of killing the microorganisms present in the food and drink and the like, that is, a sterilization method is required.
- Patent Document 1 Japanese Patent Application Laid-Open No. 5-328950 (Patent Document 1) is a sterilization method for food and drink subjected to pressure (high pressure) treatment in a temperature range from normal pressure antifreeze temperature to 15 ° C. It is disclosed. According to the said method, it can suppress that the quality of food-drinks changes by the heating for sterilization.
- Patent Document 2 discloses a method of sterilizing brewed liquor by rapid freezing. According to the said method, since microorganisms, such as a blight fungus, can be disinfected without being accompanied by a burning process, it can suppress that the original flavor which brewing liquor has changes.
- the method described in Patent Document 1 requires special equipment to pressurize, which may increase the cost required to install, operate, and maintain the equipment.
- the method described in Patent Document 2 exemplifies dry ice-acetone ( ⁇ 70 ° C.) and liquid nitrogen ( ⁇ 140 ° C.) as cooling means because it is rapidly frozen. That is, the implementation of the method requires special freezing equipment to achieve a cryogenic temperature of -70 ° C. or less, which may also increase the cost.
- the method for sterilizing food according to the present invention maintains a mixture containing food, organic acid, sugar and ethanol, or a food containing organic acid and sugar, and a mixture containing ethanol at -10 ° C or less Holding step, the content of ethanol in the mixture is 0.08 to 8% by weight, and the food is at least one food selected from fruits, fruit juices, and vegetables. I assume.
- a sterilizing method without heating can be realized without using a pressure device.
- sterilization can be performed using a general freezing storage or equipment used for freezing transportation. That is, neither pressure equipment nor cryogenic equipment is required.
- sterilization can be performed simultaneously while storing or transporting the food to be sterilized. Therefore, the new equipment for the sterilization process does not require a separate period, and both the equipment and the period are efficient, and sterilization can be performed at low cost.
- the holding step is preferably within 100 hours.
- the holding process can be performed for a relatively short time, power consumption for maintaining the low temperature can be reduced, and the cost can be reduced.
- the time required for the sterilization process can be made relatively short, the manufacturing process can be shortened.
- the content of the organic acid in the mixture is preferably 0.01 to 10% by weight.
- the bactericidal effect of the present invention can be further enhanced.
- the organic acid is citric acid.
- the bactericidal effect of the present invention can be further enhanced.
- the citric acid added for sterilization can be used as part of the product, so the citric acid is removed There is no need to provide
- the content of sugar in the mixture is preferably 1 to 10% by weight.
- the bactericidal effect of the present invention can be further enhanced.
- the sugar is preferably at least one sugar selected from sucrose and fructose.
- the bactericidal effect of the present invention can be further enhanced.
- sucrose or fructose added for sterilization is a product of Since it is available as a part, there is no need to provide a step for removing the sucrose or fructose.
- ADVANTAGE OF THE INVENTION is the sterilization method which does not accompany heating, Comprising:
- the sterilization method which can be implemented at low cost and in a short period of time is realized without requiring special equipment. According to this sterilizing method, there is no risk of impairing the flavor and aroma originally possessed by food and drink and the like, which contributes to the production of a food having both safety and high quality.
- the following embodiment demonstrates the example which applied the disinfection method of the foodstuff which concerns on this invention to the disinfection of the fruit juice 1 which is an example of the foodstuff used as a raw material of an alcoholic beverage.
- mixing step 11 in which ethanol 2 is added to fruit juice 1 and mixed, and holding step 12 in which mixture 3 obtained in mixing step 11 is held at low temperature And.
- the fruit juice 1 sterilized through these steps is sent to the subsequent step (not shown) of producing an alcoholic beverage.
- a mixing step 11 for obtaining a mixture 3 containing fruit juice 1 and ethanol 2 is performed.
- the fruit juice 1 contains citric acid, sucrose and water.
- a known mixing method can be used.
- it may be a method of charging the above-mentioned respective materials into a mixing tank provided with a stirring blade and rotating the stirring blade to mix these materials.
- the content rate of ethanol 2, a citric acid, and sucrose which are contained in the mixture 3 obtained by the mixing process 11 can be controlled by selecting the quantity of each raw material thrown in the mixing process 11 suitably.
- the content of ethanol 2 in the mixture 3 is preferably 0.08 to 8% by weight. When the content of ethanol 2 is in the above range, a good bactericidal effect can be obtained.
- the content of ethanol 2 is more preferably 0.8 to 8% by weight, and still more preferably 4 to 8% by weight.
- the mixture 3 contains the ethanol 2 and the water which fruit juice 1 contains, it has the property as an ethanol aqueous solution.
- the content of citric acid in the mixture 3 is preferably 0.01 to 10% by weight. When the content of citric acid is in the above range, the bactericidal effect can be further enhanced.
- the content of citric acid is more preferably 0.01 to 10% by weight, and still more preferably 1 to 10% by weight.
- citric acid may be mixed with the fruit juice 1 in the mixing step 11 so that the content of citric acid in the mixture 3 falls within a suitable range.
- it since it is an additive which brings about a bactericidal effect and is also a raw material of the alcoholic beverage manufactured, it is not necessary to provide the process which removes citric acid.
- the sucrose content in mixture 3 is preferably 1 to 10% by weight. When the sucrose content is in the above range, the bactericidal effect can be further enhanced.
- the sucrose content is more preferably 5 to 10% by weight, and still more preferably 8 to 10% by weight.
- sucrose may be mixed with the fruit juice 1 in the mixing step 11 so that the content of sucrose in the mixture 3 falls within a suitable range.
- sucrose is an additive which brings about a bactericidal effect and is also a raw material of manufactured alcoholic beverages, it is not necessary to provide the process of removing sucrose.
- the pH of the mixture 3 is not particularly limited, but may be less than 5.0, preferably less than 3.5, and more preferably less than 2.5.
- the holding step 12 of holding the mixture 3 obtained by the mixing step 11 at a low temperature is performed.
- a well-known thing can be used for the cooling installation which concerns on the holding process 12.
- FIG. For example, it may be a frozen storage facility or a frozen transportation facility.
- the holding temperature in the holding step 12 is preferably ⁇ 10 ° C. or less. When the holding temperature is ⁇ 10 ° C. or less, a good bactericidal effect can be obtained.
- the holding temperature is more preferably ⁇ 15 ° C. or less.
- the lower limit of the holding temperature is not particularly limited, but is preferably ⁇ 50 ° C. or higher, more preferably ⁇ 30 ° C. or higher, and still more preferably ⁇ 25 ° C. or higher. When the holding temperature is in the above range, sterilization can be performed at a temperature at which general freezing storage or freezing transportation is performed.
- the holding time of the holding step 12 is preferably within 100 hours. When the holding time is within 100 hours, the time required for the sterilization process can be made relatively short, so that the manufacturing process can be shortened.
- the holding time is more preferably 70 hours or less, further preferably 48 hours or less.
- the holding time is preferably 70 hours or more. When the holding time is 70 hours or more, a sufficient bactericidal effect can be obtained.
- the holding time is more preferably 80 hours or more.
- Aqueous ethanol solutions have different freezing points depending on their mixing ratio.
- the mixture 3 in this embodiment contains 8% by weight of ethanol 2, and its freezing point is approximately -10 ° C.
- holding step 12 when the mixture 3 is held under the environment of holding temperature -20 ° C. (holding step 12), as the temperature of the mixture 3 decreases, a solid phase in which only water is precipitated and a liquid phase which is a mixture To separate. Since only water precipitates on the solid phase and ethanol 2 does not precipitate and remains in the liquid phase, the ethanol content in the liquid phase increases. Finally, the ethanol content of the liquid phase reaches 16% by weight, which is the ethanol content with a freezing point of ⁇ 20 ° C. (ie consistent with the holding temperature).
- the microorganisms contained in the mixture 3 are extracted in the liquid phase. Therefore, concentrated ethanol 2 and microorganisms are present in the liquid phase, and the microorganisms are sterilized by the bactericidal effect of ethanol 2.
- the sterilizing effect by ethanol 2 becomes high, so that the ethanol content rate is high.
- the bactericidal effect in the liquid phase (ethanol content 16% by weight) kept at -20 ° C. is higher than the bactericidal effect in mixture 3 (ethanol content 8% by weight) before the holding step 12. In other words, it can be said that a higher bactericidal effect than expected from the amount of ethanol 2 originally contained in the mixture 3 is obtained by freezing.
- microorganisms targeted for sterilization in the method of sterilizing food according to the present embodiment are not particularly limited, but may be known microorganisms such as yeast, E. coli, staphylococcal bacteria, and lactic acid bacteria.
- the food to be sterilized is fruit juice 1
- the food to be sterilized is not limited to fruit juice, and may be, for example, fruits, vegetables, meats, fish and shellfish.
- the aspect of the fruit is not particularly limited, and the whole of the fruit, the peel of the fruit, the fruit of the fruit, the one obtained by cutting the fruit, the one obtained by crushing the fruit, or a mixture of two or more selected from these It may be.
- a known method can be used as a method of grinding the fruit, but freeze grinding is preferable.
- the food to be sterilized is fruit juice 1, ie, the case where the food contains citric acid and sucrose has been described as an example.
- the food to be sterilized may not contain at least one of the organic acid and the sugar. Regardless of whether the food contains an organic acid and a sugar, the food may be mixed with the organic acid and the sugar in the mixing step such that the content of the organic acid and the sugar in the mixture falls within a preferred range.
- the organic acid is not limited to citric acid, and may be an organic acid selected from the group consisting of citric acid, malic acid, tartaric acid and benzoic acid, and may be a mixture of a plurality of organic acids.
- the sugar is not limited to sucrose, and may be a sugar selected from the group consisting of sucrose, fructose, invert sugar and glucose, or may be a mixture of a plurality of sugars.
- the mixture may or may not further contain other optional components, such as preservatives, antioxidants, pH adjusters.
- water may be added to each of the components described above to adjust the concentration of the components in the mixture.
- the mixture 3 is obtained by the mixing step 11 which is a known mixing method has been described as an example.
- the mixture does not necessarily have to be obtained by the mixing process.
- brewing a mixture containing sugar may be used as a mixture as it results in a brewed product in which a portion of the sugar is converted to ethanol.
- Test bacteria Lactic acid bacteria were used as test bacteria in the tests shown in the following examples.
- ⁇ reagent ⁇ The following reagents were used in the tests shown in the following examples. Ethanol: Nacalai Tesque, Inc., Grade EP, Purity 99.5 Citric acid: Nacalai Tesque, Inc., grade EP, purity 9 99.0 Sucrose: Nacalai Tesque, grade EP
- the diluted sample was solidified using a sterile pipette and evenly spread on a surface-dried agar medium with a Conlage bar. This was cultured for 96 hours in an incubator maintained at 35 ° C. For the culture medium, the number of colonies formed was measured, and the obtained measurement value was multiplied by the dilution factor at the time of sample preparation to calculate the number N of bacteria per 1 g of the measurement sample.
- Example 1 0.1 g of citric acid, 1.0 g of sucrose and 0.8 g of ethanol are added to and mixed with 8.1 g of sterile water, and mixed, 1 wt% of citric acid, 10 wt% of sucrose and 8 wt% of ethanol To obtain a mixture containing. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Example 2 9.2 g of lemon juice and 0.8 g of ethanol were uniformly mixed to obtain a mixture containing 92% by weight of lemon juice and 8% by weight of ethanol. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Example 3 9.2 g of grapefruit juice and 0.8 g of ethanol were uniformly mixed to obtain a mixture containing 92 wt% of grapefruit juice and 8 wt% of ethanol. At this time, the pH of the mixture was 3.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Comparative Example 1 0.1 g of citric acid and 1.0 g of sucrose were added to 8.9 g of sterile water and mixed to obtain a mixture containing 1% by weight of citric acid and 10% by weight of sucrose. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Comparative Example 2 In the same manner as in Example 1 except that the temperature in the holding step was changed to 4 ⁇ 1 ° C., LRV (D) values at each holding time were obtained. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Comparative Example 3 0.1 g of citric acid and 0.8 g of ethanol were added to 9.1 g of sterile water and mixed to obtain a mixture containing 1% by weight of citric acid and 8% by weight of ethanol. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Comparative Example 5 To 9.2 g of sterile water, 0.8 g of ethanol was added and mixed to obtain a mixture containing 8 wt% of ethanol. At this time, the pH of the mixture was 6.9. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
- Example 3 when a mixture containing citric acid and sucrose is used (Example 1) or when juice containing citric acid and fructose is used (Examples 2 and 3), only citric acid is contained (Comparative Example) 3) A high bactericidal effect was shown as compared with the case where only sucrose was contained (comparative example 4) and the case where sterile water was used (comparative example 5).
- the present invention can be used, for example, to sterilize juice used as a raw material of alcoholic beverages.
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- Polymers & Plastics (AREA)
- Nutrition Science (AREA)
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- General Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
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- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
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Abstract
Description
本発明は、食品の殺菌方法に関する。 The present invention relates to a method of sterilizing food.
飲食品などは、一般に、有害な微生物の汚染により食中毒などの問題を引き起こすおそれがある。また、飲食品などの製品を保管および輸送するあいだに、微生物の働きによって生産者が意図しない発酵が起こることにより、製品の風味や香りに意図しない変化が起こるおそれがある。さらに、製品の包装形態が密封状態の場合は、発酵時に生じる二酸化炭素により容器の内圧が上昇し、容器の破損を招くおそれがある。したがって、飲食品などの製品の製造においては、飲食品などの中に存在する微生物を死滅させる方法、すなわち殺菌方法が必要とされる。 Food and drink generally cause problems such as food poisoning due to the contamination of harmful microorganisms. In addition, during storage and transportation of products such as food and drink, unintended changes in the flavor and aroma of the product may occur due to the occurrence of unintended fermentation by the producer due to the action of microorganisms. Furthermore, in the case where the product is packaged in a sealed state, the internal pressure of the container is increased by carbon dioxide generated during fermentation, which may lead to breakage of the container. Therefore, in the manufacture of products such as food and drink, a method of killing the microorganisms present in the food and drink and the like, that is, a sterilization method is required.
飲食品などの中に存在する微生物を殺菌する方法としては、加熱による方法や、殺菌作用のある食品添加物による方法が、従来用いられてきた。しかし、これらの方法は飲食品などが本来持つ風味や香りを損なうか、あるいは、変化させるおそれがある。そのため、加熱や多量の添加物を伴わない殺菌方法が検討されてきた。 As a method of sterilizing microorganisms present in food and drink and the like, a method by heating and a method by food additives having a bactericidal action have been used conventionally. However, these methods may impair or change the flavor and aroma originally possessed by foods and the like. Therefore, sterilization methods without heating and a large amount of additives have been studied.
このような殺菌方法として、たとえば、特開平5-328950号公報(特許文献1)には、常圧不凍温度から15℃までの温度範囲で加圧(高圧)処理する飲食品の殺菌方法が開示されている。当該方法によれば、殺菌のための加熱により飲食品の品質が変化することを抑制できる。 As such a sterilization method, for example, Japanese Patent Application Laid-Open No. 5-328950 (Patent Document 1) is a sterilization method for food and drink subjected to pressure (high pressure) treatment in a temperature range from normal pressure antifreeze temperature to 15 ° C. It is disclosed. According to the said method, it can suppress that the quality of food-drinks changes by the heating for sterilization.
また、特開昭58-170471号公報(特許文献2)には、急速冷凍による醸造酒の滅菌方法が開示されている。当該方法によれば、火入工程を伴わずに火落菌等の微生物を殺菌することができるため、醸造酒の持つ本来の香味が変化することを抑制できる。 Japanese Patent Application Laid-Open No. 58-170471 (Patent Document 2) discloses a method of sterilizing brewed liquor by rapid freezing. According to the said method, since microorganisms, such as a blight fungus, can be disinfected without being accompanied by a burning process, it can suppress that the original flavor which brewing liquor has changes.
しかし、加圧や極低温のための特殊な設備を要する方法を採用すると、製造コストが増大するおそれがある。たとえば、特許文献1に記載の方法は、加圧するための特殊な設備を要するため、当該設備を設置、運転、および、保守、するために必要な費用が高くなる場合がある。また、特許文献2に記載の方法は、急速に冷凍するため、その冷却手段としてドライアイス‐アセトン(-70℃)および液体窒素(-140℃)が例示されている。すなわち、当該方法を実施するに際しては-70℃以下の極低温を実現する特殊な凍結設備が必要となるため、やはり費用が高くなる場合がある。 However, adopting a method requiring special equipment for pressurization or cryogenic temperature may increase the manufacturing cost. For example, the method described in Patent Document 1 requires special equipment to pressurize, which may increase the cost required to install, operate, and maintain the equipment. Further, the method described in Patent Document 2 exemplifies dry ice-acetone (−70 ° C.) and liquid nitrogen (−140 ° C.) as cooling means because it is rapidly frozen. That is, the implementation of the method requires special freezing equipment to achieve a cryogenic temperature of -70 ° C. or less, which may also increase the cost.
上記課題に鑑み、加熱を伴わない殺菌方法であって、特殊な設備を必要とせず低コストで実施できる殺菌方法の実現が望まれる。 In view of the above problems, it is desired to realize a sterilization method that does not involve heating, and that can be implemented at low cost without requiring special equipment.
本発明の食品の殺菌方法は、食品、有機酸、糖、および、エタノール、を含む混合物、または、有機酸および糖を含む食品、ならびに、エタノール、を含む混合物、を、-10℃以下で保持する保持工程を有し、前記混合物中のエタノール含有率は0.08~8重量%であり、前記食品は、果実、果汁、および、野菜、から選ばれる少なくとも1種類の食品であることを特徴とする。 The method for sterilizing food according to the present invention maintains a mixture containing food, organic acid, sugar and ethanol, or a food containing organic acid and sugar, and a mixture containing ethanol at -10 ° C or less Holding step, the content of ethanol in the mixture is 0.08 to 8% by weight, and the food is at least one food selected from fruits, fruit juices, and vegetables. I assume.
この殺菌方法によれば、有機酸、糖、および、エタノール、による殺菌効果を相加的に用いることができるため、圧力装置を使用することなく、加熱を伴わない殺菌方法を実現することができる。また、保持工程の温度が上記の範囲であると、一般的な冷凍保管または冷凍輸送に用いられる設備を用いて殺菌を行うことができる。すなわち、圧力設備も、極低温設備も、必要としない。さらに、設備が共通することから、殺菌対象である食品を保管または輸送するあいだに同時に殺菌を行うことができる。したがって、殺菌工程のための新たな設備も、別途の期間も必要とせず、設備と期間との両面において効率的であり、低コストでの殺菌が可能である。 According to this sterilizing method, since the bactericidal effects of organic acids, sugars and ethanol can be used additively, a sterilizing method without heating can be realized without using a pressure device. . In addition, when the temperature of the holding step is in the above-mentioned range, sterilization can be performed using a general freezing storage or equipment used for freezing transportation. That is, neither pressure equipment nor cryogenic equipment is required. Furthermore, because the equipment is common, sterilization can be performed simultaneously while storing or transporting the food to be sterilized. Therefore, the new equipment for the sterilization process does not require a separate period, and both the equipment and the period are efficient, and sterilization can be performed at low cost.
以下、本発明の好適な態様について説明する。ただし、以下に記載する好適な態様の例によって、本発明の範囲が限定される訳ではない。 Hereinafter, preferred embodiments of the present invention will be described. However, the scope of the present invention is not limited by the examples of preferred embodiments described below.
1つの態様として、前記保持工程は100時間以内であると好適である。 In one aspect, the holding step is preferably within 100 hours.
この構成によれば、前記保持工程を比較的短期間にすることができるため、低温を維持するために消費する電力を低減し、コストを低減することができる。また、殺菌工程に要する期間を比較的短期間にすることができるため、製造工程を短縮することができる。 According to this configuration, since the holding process can be performed for a relatively short time, power consumption for maintaining the low temperature can be reduced, and the cost can be reduced. In addition, since the time required for the sterilization process can be made relatively short, the manufacturing process can be shortened.
1つの態様として、前記混合物中の有機酸の含有率は0.01~10重量%であると好適である。 In one embodiment, the content of the organic acid in the mixture is preferably 0.01 to 10% by weight.
この構成によれば、本発明の殺菌効果をさらに高めることができる。 According to this configuration, the bactericidal effect of the present invention can be further enhanced.
1つの態様として、前記有機酸はクエン酸であると好適である。 In one embodiment, it is preferred that the organic acid is citric acid.
この構成によれば、本発明の殺菌効果をさらに高めることができる。また、本発明の殺菌方法により殺菌される食品を原料とする製品がクエン酸を含む場合は、殺菌のために添加されたクエン酸を製品の一部として利用できるため、当該クエン酸を取り除く工程を設ける必要が無い。 According to this configuration, the bactericidal effect of the present invention can be further enhanced. In addition, when the food-based product to be sterilized by the sterilization method of the present invention contains citric acid, the citric acid added for sterilization can be used as part of the product, so the citric acid is removed There is no need to provide
1つの態様として、前記混合物中の糖の含有率は1~10重量%であると好適である。 In one embodiment, the content of sugar in the mixture is preferably 1 to 10% by weight.
この構成によれば、本発明の殺菌効果をさらに高めることができる。 According to this configuration, the bactericidal effect of the present invention can be further enhanced.
1つの態様として、前記糖はショ糖および果糖から選ばれる少なくとも1種類の糖であると好適である。 In one embodiment, the sugar is preferably at least one sugar selected from sucrose and fructose.
この構成によれば、本発明の殺菌効果をさらに高めることができる。また、本発明の殺菌方法により殺菌される食品と、当該食品を原料とする製品と、が、いずれもショ糖または果糖を含む場合は、殺菌のために添加されたショ糖または果糖を製品の一部としても利用できるため、当該ショ糖または果糖を取り除く工程を設ける必要が無い。 According to this configuration, the bactericidal effect of the present invention can be further enhanced. In addition, when the food sterilized by the sterilization method of the present invention and the product made from the food both contain sucrose or fructose, sucrose or fructose added for sterilization is a product of Since it is available as a part, there is no need to provide a step for removing the sucrose or fructose.
本発明によれば、加熱を伴わない殺菌方法であって、特殊な設備を必要とせず、低コストかつ短期間で実施できる殺菌方法が実現できる。この殺菌方法によれば、飲食品などが本来持つ風味や香りを損なうおそれがなく、安全性と高品質とを両立した食品の製造に寄与する。 ADVANTAGE OF THE INVENTION According to this invention, it is the sterilization method which does not accompany heating, Comprising: The sterilization method which can be implemented at low cost and in a short period of time is realized without requiring special equipment. According to this sterilizing method, there is no risk of impairing the flavor and aroma originally possessed by food and drink and the like, which contributes to the production of a food having both safety and high quality.
本発明のさらなる特徴と利点は、以下の例示的かつ非限定的な実施形態の説明によって、より明確になるだろう。 Further features and advantages of the invention will become more apparent from the following description of exemplary and non-limiting embodiments.
本発明に係る食品の殺菌方法の実施形態について、図面を参照して詳細に説明する。 Embodiments of the method of sterilizing food according to the present invention will be described in detail with reference to the drawings.
以下の実施形態では、本発明に係る食品の殺菌方法を、アルコール飲料の原料として用いられる食品の一例である果汁1の殺菌に適用した例について説明する。本実施形態の食品の殺菌方法は、図1に示すように、果汁1にエタノール2を加えて混合する混合工程11と、混合工程11で得られた混合物3を低温下で保持する保持工程12と、を含む。これらの工程を経て殺菌された果汁1は、以降のアルコール飲料の製造工程(図示せず)へと送られる。 The following embodiment demonstrates the example which applied the disinfection method of the foodstuff which concerns on this invention to the disinfection of the fruit juice 1 which is an example of the foodstuff used as a raw material of an alcoholic beverage. In the method of sterilizing food according to this embodiment, as shown in FIG. 1, mixing step 11 in which ethanol 2 is added to fruit juice 1 and mixed, and holding step 12 in which mixture 3 obtained in mixing step 11 is held at low temperature And. The fruit juice 1 sterilized through these steps is sent to the subsequent step (not shown) of producing an alcoholic beverage.
まず、果汁1とエタノール2とを含む混合物3を得るための混合工程11を行う。なお、果汁1は、クエン酸、ショ糖、および、水、を含有する。混合工程11としては、公知の混合方法を用いることができる。たとえば、撹拌翼を備える混合槽中に上記の各原料を投入し、撹拌翼を回転してこれらの原料を混合する方法であってよい。なお、混合工程11により得られる混合物3に含まれるエタノール2、クエン酸、および、ショ糖、の含有率は、混合工程11において投入する各原料の量を適宜選択することによって制御されうる。 First, a mixing step 11 for obtaining a mixture 3 containing fruit juice 1 and ethanol 2 is performed. The fruit juice 1 contains citric acid, sucrose and water. As the mixing step 11, a known mixing method can be used. For example, it may be a method of charging the above-mentioned respective materials into a mixing tank provided with a stirring blade and rotating the stirring blade to mix these materials. In addition, the content rate of ethanol 2, a citric acid, and sucrose which are contained in the mixture 3 obtained by the mixing process 11 can be controlled by selecting the quantity of each raw material thrown in the mixing process 11 suitably.
混合物3中のエタノール2の含有率は、0.08~8重量%であることが好ましい。エタノール2の含有率が上記の範囲であると、良好な殺菌効果が得られる。エタノール2の含有率は、0.8~8重量%であることがより好ましく、4~8重量%であることがさらに好ましい。なお、混合物3は、エタノール2と、果汁1が含有する水と、を含むことから、エタノール水溶液としての性質を有する。 The content of ethanol 2 in the mixture 3 is preferably 0.08 to 8% by weight. When the content of ethanol 2 is in the above range, a good bactericidal effect can be obtained. The content of ethanol 2 is more preferably 0.8 to 8% by weight, and still more preferably 4 to 8% by weight. In addition, since the mixture 3 contains the ethanol 2 and the water which fruit juice 1 contains, it has the property as an ethanol aqueous solution.
混合物3中のクエン酸の含有率は、0.01~10重量%であることが好ましい。クエン酸の含有率が上記の範囲であると、殺菌効果をさらに高めることができる。クエン酸の含有率は、0.01~10重量%であることがより好ましく、1~10重量%であることがさらに好ましい。このとき、混合物3中のクエン酸の含有率が好適な範囲となるように、混合工程11において果汁1にクエン酸を混合してもよい。なお、クエン酸は、殺菌効果をもたらす添加剤であるとともに、製造されるアルコール飲料の原料でもあるため、クエン酸を取り除く工程を設ける必要が無い。 The content of citric acid in the mixture 3 is preferably 0.01 to 10% by weight. When the content of citric acid is in the above range, the bactericidal effect can be further enhanced. The content of citric acid is more preferably 0.01 to 10% by weight, and still more preferably 1 to 10% by weight. At this time, citric acid may be mixed with the fruit juice 1 in the mixing step 11 so that the content of citric acid in the mixture 3 falls within a suitable range. In addition, since it is an additive which brings about a bactericidal effect and is also a raw material of the alcoholic beverage manufactured, it is not necessary to provide the process which removes citric acid.
混合物3中のショ糖の含有率は、1~10重量%であることが好ましい。ショ糖の含有率が上記の範囲であると、殺菌効果をさらに高めることができる。ショ糖の含有率は、5~10重量%であることがより好ましく、8~10重量%であることがさらに好ましい。
このとき、混合物3中のショ糖の含有率が好適な範囲となるように、混合工程11において果汁1にショ糖を混合してもよい。なお、ショ糖は、殺菌効果をもたらす添加剤であるとともに、製造されるアルコール飲料の原料でもあるため、ショ糖を取り除く工程を設ける必要が無い。
The sucrose content in mixture 3 is preferably 1 to 10% by weight. When the sucrose content is in the above range, the bactericidal effect can be further enhanced. The sucrose content is more preferably 5 to 10% by weight, and still more preferably 8 to 10% by weight.
At this time, sucrose may be mixed with the fruit juice 1 in the mixing step 11 so that the content of sucrose in the mixture 3 falls within a suitable range. In addition, since sucrose is an additive which brings about a bactericidal effect and is also a raw material of manufactured alcoholic beverages, it is not necessary to provide the process of removing sucrose.
混合物3のpHは特に限定されないが、5.0未満であってよく、3.5未満であることが好ましく、2.5未満であることがより好ましい。 The pH of the mixture 3 is not particularly limited, but may be less than 5.0, preferably less than 3.5, and more preferably less than 2.5.
次に、混合工程11により得られた混合物3を低温下で保持する保持工程12を行う。
保持工程12に係る冷却設備は公知のものを用いることができる。たとえば、冷凍保管設備であってよく、冷凍輸送設備であってよい。
Next, the holding step 12 of holding the mixture 3 obtained by the mixing step 11 at a low temperature is performed.
A well-known thing can be used for the cooling installation which concerns on the holding process 12. FIG. For example, it may be a frozen storage facility or a frozen transportation facility.
保持工程12における保持温度は、-10℃以下であることが好ましい。保持温度が-10℃以下であると、良好な殺菌効果が得られる。保持温度は、-15℃以下であることがより好ましい。保持温度の下限は特に限定されないが、-50℃以上であることが好ましく、-30℃以上であることがより好ましく、-25℃以上であることがさらに好ましい。保持温度が上記の範囲であると、一般的な冷凍保管または冷凍輸送が行われる温度において殺菌が可能である。 The holding temperature in the holding step 12 is preferably −10 ° C. or less. When the holding temperature is −10 ° C. or less, a good bactericidal effect can be obtained. The holding temperature is more preferably −15 ° C. or less. The lower limit of the holding temperature is not particularly limited, but is preferably −50 ° C. or higher, more preferably −30 ° C. or higher, and still more preferably −25 ° C. or higher. When the holding temperature is in the above range, sterilization can be performed at a temperature at which general freezing storage or freezing transportation is performed.
保持工程12の保持時間は、100時間以内であることが好ましい。保持時間が100時間以内であると、殺菌工程に要する期間を比較的短期間にすることができるため、製造工程を短縮することができる。保持時間は、70時間以内であることがより好ましく、48時間以内であることがさらに好ましい。
また、保持時間は、70時間以上であることが好ましい。保持時間が70時間以上であると、十分な殺菌効果が得られる。保持時間は、80時間以上であることがより好ましい。
The holding time of the holding step 12 is preferably within 100 hours. When the holding time is within 100 hours, the time required for the sterilization process can be made relatively short, so that the manufacturing process can be shortened. The holding time is more preferably 70 hours or less, further preferably 48 hours or less.
The holding time is preferably 70 hours or more. When the holding time is 70 hours or more, a sufficient bactericidal effect can be obtained. The holding time is more preferably 80 hours or more.
ここで、第一の実施形態の食品の殺菌方法において、効果的に殺菌が行われる原理について説明する。なお、以降の説明においては、混合物3中におけるエタノール2の含有率を8重量%とした場合を例として説明する。 Here, in the method of sterilizing food according to the first embodiment, the principle of effective sterilization will be described. In the following description, the case where the content of ethanol 2 in the mixture 3 is 8% by weight will be described as an example.
エタノール水溶液は、その混合比率により異なる凝固点を有する。本実施形態における混合物3は、エタノール2を8重量%含み、その凝固点はおよそ-10℃である。このとき混合物3を保持温度-20℃の環境下で保持する(保持工程12)と、混合物3の温度が低下するのにしたがって、水のみが析出した固相と、混合物である液相とに分離する。固相に水のみが析出し、エタノール2は析出せず液相に残るため、液相のエタノール含有率は上昇する。最終的に、液相のエタノール含有率が、凝固点が-20℃である(すなわち保持温度と一致する)エタノール含有率である16重量%に到達する。 Aqueous ethanol solutions have different freezing points depending on their mixing ratio. The mixture 3 in this embodiment contains 8% by weight of ethanol 2, and its freezing point is approximately -10 ° C. At this time, when the mixture 3 is held under the environment of holding temperature -20 ° C. (holding step 12), as the temperature of the mixture 3 decreases, a solid phase in which only water is precipitated and a liquid phase which is a mixture To separate. Since only water precipitates on the solid phase and ethanol 2 does not precipitate and remains in the liquid phase, the ethanol content in the liquid phase increases. Finally, the ethanol content of the liquid phase reaches 16% by weight, which is the ethanol content with a freezing point of −20 ° C. (ie consistent with the holding temperature).
このように、エタノールを含む混合物を、そのエタノール含有率により決定される凝固点より低い保持温度で保持すると、液相のエタノール含有率が上昇する。すなわち、凍結によりエタノールが濃縮される。 Thus, holding the mixture containing ethanol at a holding temperature below the freezing point determined by its ethanol content will increase the ethanol content of the liquid phase. That is, ethanol is concentrated by freezing.
このとき、水が析出する過程において、混合物3中に含まれる微生物は液相に抽出される。したがって、液相には、濃縮されたエタノール2と微生物とが存在することになり、エタノール2の殺菌効果により微生物が殺菌される。ところで、エタノール含有率が高いほど、エタノール2による殺菌効果が高くなる。したがって、-20℃に保持された液相(エタノール含有率16重量%)における殺菌効果は、保持工程12の前の混合物3(エタノール含有率8重量%)における殺菌効果より高い。言い換えれば、混合物3に本来含まれるエタノール2の量から期待されるよりも高い殺菌効果が、凍結することにより得られる、といえる。 At this time, in the process of water precipitation, the microorganisms contained in the mixture 3 are extracted in the liquid phase. Therefore, concentrated ethanol 2 and microorganisms are present in the liquid phase, and the microorganisms are sterilized by the bactericidal effect of ethanol 2. By the way, the sterilizing effect by ethanol 2 becomes high, so that the ethanol content rate is high. Thus, the bactericidal effect in the liquid phase (ethanol content 16% by weight) kept at -20 ° C. is higher than the bactericidal effect in mixture 3 (ethanol content 8% by weight) before the holding step 12. In other words, it can be said that a higher bactericidal effect than expected from the amount of ethanol 2 originally contained in the mixture 3 is obtained by freezing.
なお、本実施形態の食品の殺菌方法において殺菌の対象とする微生物類は、特に限定されないが、酵母、大腸菌、ブドウ球菌、および、乳酸菌など、公知の微生物類であってよい。 The microorganisms targeted for sterilization in the method of sterilizing food according to the present embodiment are not particularly limited, but may be known microorganisms such as yeast, E. coli, staphylococcal bacteria, and lactic acid bacteria.
〔その他の実施形態〕
次に、本発明に係る食品の殺菌方法のその他の実施形態について説明する。なお、以下のそれぞれの実施形態で開示される構成は、矛盾が生じない限り、他の実施形態で開示される構成と組み合わせて適用することも可能である。
Other Embodiments
Next, another embodiment of the method of sterilizing food according to the present invention will be described. The configurations disclosed in each of the following embodiments can be applied in combination with the configurations disclosed in the other embodiments as long as no contradiction arises.
上記の実施形態では、殺菌対象とする食品が果汁1である場合を例として説明した。しかし、殺菌対象とする食品は果汁に限定されず、たとえば果実、野菜、肉、魚介であってもよい。このとき、果実の態様は特に限定されず、果実の全体、果実の皮、果実の実、果実を切断したもの、果実を粉砕したもの、または、これらの中から選ばれる2つ以上の混合物、であってよい。果実を粉砕する場合の粉砕方法は公知の方法を用いることができるが、凍結粉砕することが好ましい。 In the above embodiment, the case where the food to be sterilized is fruit juice 1 has been described as an example. However, the food to be sterilized is not limited to fruit juice, and may be, for example, fruits, vegetables, meats, fish and shellfish. At this time, the aspect of the fruit is not particularly limited, and the whole of the fruit, the peel of the fruit, the fruit of the fruit, the one obtained by cutting the fruit, the one obtained by crushing the fruit, or a mixture of two or more selected from these It may be. A known method can be used as a method of grinding the fruit, but freeze grinding is preferable.
上記の実施形態では殺菌対象とする食品が果汁1であり、すなわち、食品がクエン酸およびショ糖を含有する場合を例として説明した。しかし、殺菌対象とする食品は有機酸または糖の少なくとも一方を含有しないものであってもよい。食品が有機酸および糖を含有するか否かに関わらず、混合物における有機酸および糖の含有率が好ましい範囲となるように、混合工程において食品に有機酸および糖を混合してよい。 In the above embodiment, the food to be sterilized is fruit juice 1, ie, the case where the food contains citric acid and sucrose has been described as an example. However, the food to be sterilized may not contain at least one of the organic acid and the sugar. Regardless of whether the food contains an organic acid and a sugar, the food may be mixed with the organic acid and the sugar in the mixing step such that the content of the organic acid and the sugar in the mixture falls within a preferred range.
上記の実施形態では、混合物3が果汁1およびエタノール2を含み、果汁1がクエン酸およびショ糖を含有する場合を例として説明した。しかし、有機酸はクエン酸に限定されず、クエン酸、リンゴ酸、酒石酸、安息香酸からなる群から選ばれる有機酸であってもよく、複数の有機酸の混合物であってもよい。また、糖はショ糖に限定されず、ショ糖、果糖、転化糖、ブドウ糖からなる群から選ばれる糖であってもよく、複数の糖の混合物であってもよい。混合物は、さらに、他の任意の成分、たとえば、防腐剤、酸化防止剤、pH調整剤を含んでいてもよく、あるいは、含んでいなくてもよい。また、上記の各成分に水を加えて混合物中の成分の濃度を調整してもよい。 In the above embodiment, the case where the mixture 3 contains fruit juice 1 and ethanol 2 and the fruit juice 1 contains citric acid and sucrose has been described as an example. However, the organic acid is not limited to citric acid, and may be an organic acid selected from the group consisting of citric acid, malic acid, tartaric acid and benzoic acid, and may be a mixture of a plurality of organic acids. The sugar is not limited to sucrose, and may be a sugar selected from the group consisting of sucrose, fructose, invert sugar and glucose, or may be a mixture of a plurality of sugars. The mixture may or may not further contain other optional components, such as preservatives, antioxidants, pH adjusters. In addition, water may be added to each of the components described above to adjust the concentration of the components in the mixture.
上記の実施形態では、公知の混合方法である混合工程11によって混合物3を得る場合を例として説明した。しかし、混合物は必ずしも混合工程によって得られる必要はない。たとえば、糖を含む混合物を醸造すると、糖の一部がエタノールに変換された醸造生成物が得られるので、これを混合物として用いてもよい。 In the above embodiment, the case where the mixture 3 is obtained by the mixing step 11 which is a known mixing method has been described as an example. However, the mixture does not necessarily have to be obtained by the mixing process. For example, brewing a mixture containing sugar may be used as a mixture as it results in a brewed product in which a portion of the sugar is converted to ethanol.
その他の構成に関しても、本明細書において開示された実施形態は全ての点で例示であって、本発明の範囲はそれらによって限定されることはないと理解されるべきである。当業者であれば、本発明の趣旨を逸脱しない範囲で、適宜改変が可能であることを容易に理解できるであろう。したがって、本発明の趣旨を逸脱しない範囲で改変された別の実施形態も、当然、本発明の範囲に含まれる。 With regard to the other configurations, it is to be understood that the embodiments disclosed herein are illustrative in all respects, and the scope of the present invention is not limited by them. Those skilled in the art will easily understand that appropriate modifications can be made without departing from the spirit of the present invention. Therefore, other embodiments modified within the scope of the present invention are naturally included in the scope of the present invention.
以下に実施例を挙げて本発明を説明するが、本発明は以下の実施例のみに限定されるものではない。 EXAMPLES The present invention will be described by way of examples, but the present invention is not limited to the following examples.
〔供試菌〕
以下の実施例に示す試験において、供試菌として乳酸菌を用いた。
[Test bacteria]
Lactic acid bacteria were used as test bacteria in the tests shown in the following examples.
〔試薬〕
以下の実施例に示す試験において、次の試薬を用いた。
エタノール :ナカライテスク社製、グレードEP、純度99.5
クエン酸 :ナカライテスク社製、グレードEP、純度≧99.0
ショ糖 :ナカライテスク社製、グレードEP
〔reagent〕
The following reagents were used in the tests shown in the following examples.
Ethanol: Nacalai Tesque, Inc., Grade EP, Purity 99.5
Citric acid: Nacalai Tesque, Inc., grade EP, purity 9 99.0
Sucrose: Nacalai Tesque, grade EP
〔果汁〕
市販のグレープフルーツおよびレモンをそれぞれ直接圧搾(スーパーハンドジューサー TW-001)により搾汁し、pH3.3のグレープフルーツ果汁、および、pH2.3のレモン果汁を得た。
[Fruit juice]
Commercially available grapefruit and lemon were respectively directly squeezed (super hand juicer TW-001) to obtain grapefruit juice of pH 3.3 and lemon juice of pH 2.3.
〔植菌工程〕
試料液を10mL採取し、乳酸菌を加えて均一に混合し、植菌液を得た。
[Inoculation step]
10 mL of the sample solution was collected, and lactic acid bacteria were added and uniformly mixed to obtain an inoculum.
〔保持工程〕
植菌液を、庫内の温度が-20±4℃に保たれた冷凍保管設備の庫内に保持した。保持工程の途中において、生菌数分析のための測定試料を採取した。このとき、保持開始から試料採取までの経過時間を保持時間として記録した。
[Holding process]
The inoculum was kept in the freezer storage facility in which the temperature inside the freezer was kept at -20. +-. 4.degree. During the holding step, a measurement sample for viable cell count analysis was collected. At this time, the elapsed time from the start of holding to sampling was recorded as the holding time.
〔生菌数分析〕
測定試料10mLを採取し、これを無菌水で希釈して希釈検体とした。滅菌ピペットを用いて当該希釈検体を固化させ、表面を乾燥させた寒天培地上にコンラージ棒で均等に塗抹した。これを35℃に保持したインキュベータで96時間の培養を行った。
培養後の培地について、生じたコロニーの数を測定し、得られた測定値に検体調製時の希釈倍率を乗じて測定試料1gあたりの菌数Nを算出した。殺菌工程前の試料について同様の方法で測定した検体1gあたりの菌数をN0とし、殺菌工程後の菌数の対数減少値LRV(D)を、以下の数式(I)に従って算出した。
LRV(D)=Log10(N0/N) (I)
Viable count analysis
10 mL of a measurement sample was collected and diluted with sterile water to obtain a diluted sample. The diluted sample was solidified using a sterile pipette and evenly spread on a surface-dried agar medium with a Conlage bar. This was cultured for 96 hours in an incubator maintained at 35 ° C.
For the culture medium, the number of colonies formed was measured, and the obtained measurement value was multiplied by the dilution factor at the time of sample preparation to calculate the number N of bacteria per 1 g of the measurement sample. Assuming that the number of bacteria per 1 g of a sample measured by the same method for the sample before the sterilization step is N 0 , the logarithmic reduction value LRV (D) of the number of bacteria after the sterilization step was calculated according to the following formula (I).
LRV (D) = Log 10 (N 0 / N) (I)
〔実施例1〕
無菌水8.1gに、クエン酸0.1g、ショ糖1.0g、および、エタノール0.8g、を加えて混合し、クエン酸1重量%、ショ糖10重量%、および、エタノール8重量%、を含む混合物を得た。このとき、当該混合物のpHは2.3だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Example 1
0.1 g of citric acid, 1.0 g of sucrose and 0.8 g of ethanol are added to and mixed with 8.1 g of sterile water, and mixed, 1 wt% of citric acid, 10 wt% of sucrose and 8 wt% of ethanol To obtain a mixture containing. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔実施例2〕
レモン果汁9.2gとエタノール0.8gとを均一に混合し、レモン果汁92重量%およびエタノール8重量%を含む混合物を得た。このとき、当該混合物のpHは2.3だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Example 2
9.2 g of lemon juice and 0.8 g of ethanol were uniformly mixed to obtain a mixture containing 92% by weight of lemon juice and 8% by weight of ethanol. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔実施例3〕
グレープフルーツ果汁9.2gとエタノール0.8gとを均一に混合し、グレープフルーツ果汁92重量%およびエタノール8重量%を含む混合物を得た。このとき、当該混合物のpHは3.3だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
[Example 3]
9.2 g of grapefruit juice and 0.8 g of ethanol were uniformly mixed to obtain a mixture containing 92 wt% of grapefruit juice and 8 wt% of ethanol. At this time, the pH of the mixture was 3.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔比較例1〕
無菌水8.9gにクエン酸0.1gおよびショ糖1.0gを加えて混合し、クエン酸1重量%およびショ糖10重量%を含む混合物を得た。このとき、当該混合物のpHは2.3だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Comparative Example 1
0.1 g of citric acid and 1.0 g of sucrose were added to 8.9 g of sterile water and mixed to obtain a mixture containing 1% by weight of citric acid and 10% by weight of sucrose. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔比較例2〕
保持工程における温度を4±1℃としたほかは、実施例1と同様の手順により、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Comparative Example 2
In the same manner as in Example 1 except that the temperature in the holding step was changed to 4 ± 1 ° C., LRV (D) values at each holding time were obtained. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔比較例3〕
無菌水9.1gにクエン酸0.1gおよびエタノール0.8gを加えて混合し、クエン酸1重量%およびエタノール8重量%を含む混合物を得た。このとき、当該混合物のpHは2.3だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。
保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Comparative Example 3
0.1 g of citric acid and 0.8 g of ethanol were added to 9.1 g of sterile water and mixed to obtain a mixture containing 1% by weight of citric acid and 8% by weight of ethanol. At this time, the pH of the mixture was 2.3. The said inoculation step and the said holding process were implemented in order with respect to the said mixture.
For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔比較例4〕
無菌水8.2gにショ酸1.0gおよびエタノール0.8gを加えて混合し、ショ糖10重量%およびエタノール8重量%を含む混合物を得た。このとき、当該混合物のpHは6.9だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Comparative Example 4
To 8.2 g of sterile water, 1.0 g of succinic acid and 0.8 g of ethanol were added and mixed to obtain a mixture containing 10 wt% of sucrose and 8 wt% of ethanol. At this time, the pH of the mixture was 6.9. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔比較例5〕
無菌水9.2gにエタノール0.8gを加えて混合し、エタノール8重量%を含む混合物を得た。このとき、当該混合物のpHは6.9だった。当該混合物に対し、前記植菌工程および前記保持工程を順に実施した。保持時間が異なる各測定試料について、前記の方法にしたがって生菌数分析を行い、各保持時間におけるLRV(D)値を得た。採取した測定試料の保持時間およびLRV(D)値を表1に示した。
Comparative Example 5
To 9.2 g of sterile water, 0.8 g of ethanol was added and mixed to obtain a mixture containing 8 wt% of ethanol. At this time, the pH of the mixture was 6.9. The said inoculation step and the said holding process were implemented in order with respect to the said mixture. For each measurement sample having different retention times, viable count analysis was performed according to the method described above to obtain LRV (D) values at each retention time. The retention times and LRV (D) values of the collected measurement samples are shown in Table 1.
〔供試菌に対する殺菌効果〕
実施例1~3および比較例1~5の、各保持時間におけるLRV(D)値を表1に示した。エタノールを含む混合物を凝固点以下で保持した場合(実施例1~3)について、エタノールを用いない場合(比較例1)や凝固点以上の温度で保持した場合(比較例2)に比べて高い殺菌効果が得られた。また、クエン酸およびショ糖を含む混合物を用いた場合(実施例1)や、クエン酸および果糖を含む果汁を用いた場合(実施例2、3)に、クエン酸のみを含む場合(比較例3)、ショ糖のみを含む場合(比較例4)、および、無菌水を用いた場合(比較例5)、に比べて高い殺菌効果を示した。
The LRV (D) values at each holding time of Examples 1 to 3 and Comparative Examples 1 to 5 are shown in Table 1. When a mixture containing ethanol is maintained at or below the freezing point (Examples 1 to 3), a bactericidal effect is higher than when ethanol is not used (Comparative Example 1) or at a temperature above the freezing point (Comparative Example 2) was gotten. In addition, when a mixture containing citric acid and sucrose is used (Example 1) or when juice containing citric acid and fructose is used (Examples 2 and 3), only citric acid is contained (Comparative Example) 3) A high bactericidal effect was shown as compared with the case where only sucrose was contained (comparative example 4) and the case where sterile water was used (comparative example 5).
本発明は、たとえば、アルコール飲料の原料とする果汁の殺菌に利用することができる。
The present invention can be used, for example, to sterilize juice used as a raw material of alcoholic beverages.
Claims (6)
有機酸および糖を含む食品、ならびに、エタノール、を含む混合物、を、
-10℃以下で保持する保持工程を有し、
前記混合物中のエタノール含有率は0.08~8重量%であり、
前記食品は、果実、果汁、および、野菜、から選ばれる少なくとも1種類の食品である食品の殺菌方法。 Food, organic acid, sugar, and a mixture containing ethanol, or
A food containing an organic acid and a sugar, and a mixture containing ethanol,
Having a holding step of holding at -10 ° C. or less,
The ethanol content in the mixture is 0.08-8% by weight,
The method for sterilizing a food, wherein the food is at least one food selected from fruits, fruit juices, and vegetables.
The method according to any one of claims 1 to 5, wherein the sugar is at least one sugar selected from sucrose and fructose.
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Non-Patent Citations (2)
Title |
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MATSUDA, TOSHIO ET AL.: "Antimicrobial Activities of Organic Acids Determined by Minimum Inhibitory Concentrations at Different pH Ranged from 4.0 to 7.0", NIPPON SHOKUHIN KOGYO GAKKAISHI, vol. 41, no. 10, 1994, pages 687 - 701, XP055624200 * |
TAKANO, MITSUO ET AL.: "Bactericidal Effect of Freezing with Alcohol", JAPANESE JOURNAL OF FREEZING AND DRYING, vol. 26, 1980, pages 169 - 175, XP055624195 * |
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