JP7300116B2 - Content filling system and sterilization method - Google Patents

Description

The present disclosure relates to content filling systems and sterilization methods.

An aseptic filling system (aseptic filling system) that fills a sterilized container (PET bottle) with sterilized contents in an aseptic environment and then closes the container with a cap is known (see, for example, Patent Document 1). ).

Specifically, in an aseptic filling system, molded containers are fed into the aseptic filling system, and within the aseptic filling system, the containers are sprayed with an aqueous hydrogen peroxide solution as a sterilant. The container is then sterilized by drying the aqueous hydrogen peroxide solution. The container is then aseptically filled with the contents.

By the way, in recent years, for the purpose of reducing the environmental load, it is required to reduce the amount of emitted carbon dioxide.

Japanese Patent No. 4526820

The present disclosure has been made in consideration of such points, and aims to provide a content filling system and a sterilization method capable of reducing carbon dioxide emissions.

A first aspect of the present disclosure is connected to a water sterilization line for non-heat sterilization of water, a stock solution sterilization line for heat sterilizing a product stock solution, and the water sterilization line and the stock solution sterilization line, respectively, wherein the water and the product and a filling device for filling a container with a stock solution.

According to a second aspect of the present disclosure, in the content filling system according to the first aspect described above, the water sterilization line may sterilize the water with ultraviolet rays.

A third aspect of the present disclosure is the content filling system according to the above-described first aspect or the above-described second aspect, wherein in the water sterilization line, the water is selected from a low-pressure mercury lamp and a medium-pressure mercury lamp. It may be sterilized by ultraviolet light from at least one side.

A fourth aspect of the present disclosure is the content filling system according to the above-described second aspect or the above-described third aspect, wherein the content filling system further includes a control unit that controls the water sterilization line. Alternatively, the control unit may discharge the water to the outside of the water sterilization line when the irradiation amount or illuminance of the ultraviolet rays is equal to or less than a predetermined value.

（ただし、Ｔは任意の殺菌温度（℃）、１０＾｛（Ｔ－Ｔｒ）／Ｚ｝は任意の殺菌温度Ｔでの致死率、Ｔｒは基準温度（℃）、ＺはＺ値（１０℃）を表す。） A fifth aspect of the present disclosure is connected to a water sterilization line for sterilizing water, a stock solution sterilization line for heat sterilizing a product stock solution, and the water sterilization line and the stock solution sterilization line, respectively, to sterilize the water and the product stock solution. and a filling device for filling a container, and when the pH of the content prepared by diluting the product stock solution with the water is less than 4.5, the water sterilization line has an _F0 value of 0.00029 or more. The water is sterilized so that it is less than 3.1, and when the pH of the content is 4.5 or more, the water sterilization line is sterilized so that the F ₀ value is 3.1 or more and 100 or less. A content filling system that sterilizes water and wherein the _F0 value is the F value calculated by the following formula.

(However, T is an arbitrary sterilization temperature (° C.), 10^{(T-Tr)/Z} is the lethality rate at an arbitrary sterilization temperature T, Tr is the reference temperature (° C.), Z is the Z value (10° C. ) represents.)

（ただし、Ｔは任意の殺菌温度（℃）、１０＾｛（Ｔ－Ｔｒ）／Ｚ｝は任意の殺菌温度Ｔでの致死率、Ｔｒは基準温度（℃）、ＺはＺ値（１０℃）を表す。） A sixth aspect of the present disclosure is connected to a water sterilization line for sterilizing water, a stock solution sterilization line for heat sterilizing a product stock solution, and the water sterilization line and the stock solution sterilization line, respectively, to sterilize the water and the product stock solution. The water sterilization line sterilizes the water so that the F ₀ value is 3.1 or more and 100 or less, and the F ₀ value is calculated by the following formula. It is a content filling system that is an F value.

(However, T is an arbitrary sterilization temperature (° C.), 10^{(T-Tr)/Z} is the lethality rate at an arbitrary sterilization temperature T, Tr is the reference temperature (° C.), Z is the Z value (10° C. ) represents.)

A seventh aspect of the present disclosure is the content filling system according to each of the above-described first aspect to the above-described sixth aspect, wherein the water sterilization line filters the water with a sterile filter to may be sterilized.

An eighth aspect of the present disclosure is the contents filling system according to each of the first aspect to the seventh aspect described above, wherein the contents filling system further comprises a control unit that controls the water sterilization line. The water sterilization line may have at least a water sterilizer that sterilizes the water, the water sterilizer may include at least a sterile filter, and the control unit may include the sterile The water may be discharged outside the water sterilization line when the pressure difference between the pressure upstream and downstream of the filter exceeds a predetermined value.

A ninth aspect of the present disclosure is the contents filling system according to each of the first aspect to the eighth aspect described above, wherein the contents filling system further includes a control unit that controls the water sterilization line. The control unit discharges the water to the outside of the water sterilization line when at least one of the number of bacteria and fine particles in the water sampled from the water sterilization line reaches a predetermined value or more. You can

A tenth aspect of the present disclosure is the contents filling system according to each of the above-described first aspect to the above-described ninth aspect, wherein the product undiluted solution is diluted 1.1 times or more and 100 times or less with the water. May be.

An eleventh aspect of the present disclosure is the content filling system according to each of the above-described first to tenth aspects, wherein the filling device includes a water filling device connected to the water sterilization line; A concentrate filling device connected to a concentrate sterilization line may be provided, the water filling device may fill the container with the sterilized water, and the concentrate filling device may include the The container may be filled with the sterilized product concentrate.

A twelfth aspect of the present disclosure is the content filling system according to the eleventh aspect described above, wherein the water filling device may fill the empty container with the water, and the water filling device may fill the empty container with the water. A filling speed at which the water is filled into the container may be faster than a filling speed at which the concentrate filling device fills the container with the product concentrate.

A thirteenth aspect of the present disclosure is the content filling system according to each of the above-described first to ninth aspects, wherein the filling device includes a water filling device connected to the water sterilization line; and a concentrate filling device connected to a concentrate sterilization line, and only one of the water filling device and the concentrate filling device is used to fill the container with the water or the product concentrate. You can fill it.

A fourteenth aspect of the present disclosure is the content filling system according to each of the above-described eleventh to thirteenth aspects, wherein the water filling device includes a plurality of water filling nozzles for filling the water. Each of the water filling nozzles may be connected to a snift line for discharging gas inside the container, and the water filling device may be connected to the container through the snift line. The water may be pressurized and filled in a state in which the internal gas can be discharged.

A fifteenth aspect of the present disclosure is a content filling system according to the above-described fourteenth aspect, wherein a seal that suppresses leakage of gas inside the container is provided at the tip of the water filling nozzle by being in close contact with the container. A member may be provided, and the water filling device may pressure-fill the water while the sealing member is in close contact with the container.

A sixteenth aspect of the present disclosure is the content filling system according to the above-described fourteenth aspect or the above-described fifteenth aspect, wherein the concentrate filling device includes a plurality of concentrate filling nozzles for filling the product concentrate. Alternatively, the diameter of the water filling nozzle may be larger than the diameter of the undiluted solution filling nozzle.

A seventeenth aspect of the present disclosure is the contents filling system according to the sixteenth aspect described above, wherein the diameter of the water filling nozzle is 1.2 times or more and 1.5 times or less than the diameter of the undiluted solution filling nozzle, Also good.

According to an eighteenth aspect of the present disclosure, in the contents filling system according to each of the above-described eleventh to seventeenth aspects, the filling device may have a plurality of the undiluted solution filling devices.

A nineteenth aspect of the present disclosure is the contents filling system according to the eighteenth aspect described above, wherein the contents filling system may include a plurality of the undiluted solution sterilization lines, and the plurality of undiluted solution filling devices each include may be connected to the undiluted solution sterilization line of the above.

A twentieth aspect of the present disclosure is the content filling system according to the nineteenth aspect described above, wherein the filling device comprises a first concentrate filling device for filling the product concentrate not containing flavor, and the product concentrate containing flavor. You may have a 2nd concentrate filling device which fills.

A twenty-first aspect of the present disclosure is the content filling system according to the above-described twentieth aspect, wherein the first concentrate filling device may be housed in a space defined by a chamber wall, and the chamber wall may: A gap through which the container passes may be formed, and a first wheel including a first gripper for conveying the container may be arranged outside the space so as to be openable and closable. A second wheel including a second gripper for conveying the container may be disposed inside the wheel so as to be openable and closable. Two grippers may receive the container from the first gripper, and the second gripper is configured so as not to interfere with the first gripper when the container is not filled with the product concentrate by the first concentrate filling device. , the open position is good.

A twenty-second aspect of the present disclosure is the content filling system according to the twenty-first aspect described above, wherein the chamber wall may be provided with a shutter that opens and closes the gap, and the product is When the container is not filled with liquid concentrate, the gap may be closed by the shutter, and the second gripper may assume an open position so as not to interfere with the shutter closing the gap.

A twenty-third aspect of the present disclosure is the contents filling system according to each of the above-described first to tenth aspects, wherein between the water sterilization line and the undiluted solution sterilization line and the filling device, A mixing tank for mixing the water and the product stock solution may be interposed.

A twenty-fourth aspect of the present disclosure is the content filling system according to each of the above-described first to tenth aspects, wherein the filling device includes a plurality of filling nozzles for filling the water and the product concentrate. The water sterilization line and the concentrate sterilization line may be connected to each of the filling nozzles.

A twenty-fifth aspect of the present disclosure is the content filling system according to each of the above-described first to twenty-fourth aspects, wherein the water sterilization line includes a first water tank for storing the water, and the first It may have a water sterilizer that sterilizes the water stored in the water tank, and a second water tank that stores the water sterilized by the water sterilizer, and the undiluted solution sterilization line is the product A first concentrate tank for storing a concentrate, a product concentrate sterilizer for heat sterilizing the product concentrate stored in the first concentrate tank, and a second concentrate for storing the product concentrate sterilized by the product concentrate sterilizer. You may have a tank.

According to a twenty-sixth aspect of the present disclosure, in the content filling system according to the twenty-fifth aspect described above, the water sterilization line may have a plurality of the water sterilizers.

A twenty-seventh aspect of the present disclosure is the content filling system according to the above-described twenty-fifth aspect or the above-described twenty-sixth aspect, wherein the content filling system is attached to the container filled with the water and the product concentrate. A cap sterilization device that sterilizes the cap may be further provided, and a bypass line that connects the water sterilization line and the cap sterilization device to each other may be provided downstream of the second water tank.

A twenty-eighth aspect of the present disclosure is the content filling system according to each of the above-described twenty-fifth aspect to the above-described twenty-seventh aspect, wherein solids are added to the product concentrate downstream of the second concentrate tank. The addition unit to be added may be connected.

A twenty-ninth aspect of the present disclosure is a content filling system according to each of the above-described first aspect to the above-described twenty-eighth aspect, comprising a preform sterilization device for sterilizing a preform, and forming the container from the preform. and a container sterilizing device for sterilizing the container, and the container forming device may form the container without adjusting the temperature of the container with hot water.

A thirtieth aspect of the present disclosure is a sterilization method for sterilizing a content filling system according to each of the above-described first to twenty-ninth aspects, wherein the water sterilization line includes at least a water sterilizer, The water sterilizer has at least one sterile filter and at least one sterilizer, the method of sterilizing comprising subjecting at least one of the sterile filters to a first integrity test; A method of sterilization comprising the steps of sterilizing a filter and subjecting at least one of said sterile filters to a second integrity test.

According to a thirty-first aspect of the present disclosure, in the sterilization method according to the thirtieth aspect described above, the sterilization method may further include a step of sterilizing the sterilizer.

A thirty-second aspect of the present disclosure is the sterilization method according to the above-described thirtieth aspect or the above-described thirty-first aspect, wherein the step of sterilizing the sterilizer comprises supplying hot water to the water sterilizer; A step of circulating the hot water in a circulation system including the sterilizer and a step of cooling the circulation system may be provided.

A thirty-third aspect of the present disclosure is the sterilization method according to each of the above-described thirtieth aspect to the above-described thirty-second aspect, wherein the step of sterilizing the sterilizer comprises supplying a chemical to the water sterilizer; A step of circulating the drug in a circulation system including the sterilizer and a step of rinsing the circulation system may be included.

A thirty-fourth aspect of the present disclosure is the sterilization method according to each of the above-described thirtieth aspect to the above-described thirty-third aspect, wherein the step of sterilizing the sterile filter includes a step of sterilizing the sterilizer. It may be done in between.

According to the present disclosure, the amount of carbon dioxide emitted by the content filling system can be reduced.

FIG. 1 is a schematic plan view showing a content filling system according to one embodiment. Figure 2A is a schematic diagram showing a water disinfection line according to one embodiment. FIG. 2B is a schematic diagram showing another example of a water disinfection line according to one embodiment. FIG. 2C is a schematic diagram showing another example of a water disinfection line according to one embodiment. Figure 2D is a schematic diagram showing another example of a water disinfection line according to one embodiment. FIG. 2E is a schematic diagram showing another example of a water disinfection line according to one embodiment. FIG. 2F is a schematic diagram showing another example of a water disinfection line according to one embodiment. FIG. 3 is a plan view showing the first sterilizer of the water sterilizer according to one embodiment. FIG. 4 is a cross-sectional view (cross-sectional view taken along line IV-IV in FIG. 3) showing the first sterilizer of the water sterilizer according to one embodiment. FIG. 5A is a plan view showing another example of the first sterilizer of the water sterilizer according to one embodiment. FIG. 5B is a cross-sectional view (cross-sectional view taken along line VB-VB in FIG. 5A) showing another example of the first water sterilizer of the water sterilizer according to one embodiment. FIG. 6A is a front view showing another example of the first sterilizer of the water sterilizer according to one embodiment. 6B is a cross-sectional view (cross-sectional view taken along line VIB-VIB in FIG. 6A) showing another example of the first water sterilizer of the water sterilizer according to one embodiment. FIG. 7 is a schematic diagram showing a concentrate pasteurization line according to one embodiment. FIG. 8 is a flow chart showing a content filling method using the content filling system according to one embodiment. FIG. 9 is a flow chart showing a chamber sterilization method of a filling system sterilization method according to one embodiment. FIG. 10A is a flow chart showing a method of sterilizing a content filling system according to one embodiment, which is a method of sterilizing a water sterilizer. FIG. 10B1 is a flow chart showing a method of sterilizing a content filling system according to one embodiment, which is a method of sterilizing a water sterilizer. FIG. 10B2 is a flow chart showing another example of a water sterilization method, which is a content filling system sterilization method according to one embodiment. FIG. 10C is a flow chart showing still another example of the method of sterilizing the content filling system according to the embodiment, which is the method of sterilizing the water sterilizer. FIG. 10D is a flow chart showing still another example of the method of sterilizing the content filling system according to the embodiment, which is the method of sterilizing the water sterilizer. FIG. 10E is a flow chart showing still another example of the method of sterilizing the content filling system according to the embodiment, which is the method of sterilizing the water sterilizer. FIG. 11 is a schematic plan view showing a second modification of the content filling system according to one embodiment. FIG. 12A is a schematic plan view showing a fourth modification of the content filling system according to one embodiment; FIG. 12B is a schematic plan view showing an enlarged second aseptic chamber and an outlet chamber of a fourth modification of the content filling system according to one embodiment; FIG. 12C is a schematic plan view showing a content filling method using the fourth modification of the content filling system according to one embodiment. FIG. 12D is a schematic plan view showing a content filling method using the fourth modification of the content filling system according to one embodiment. FIG. 12E is a schematic plan view showing another example (first example) of the fourth modification of the content filling system according to one embodiment. FIG. 12F is a schematic plan view showing another example (second example) of the fourth modification of the content filling system according to one embodiment. FIG. 12G is a schematic plan view showing another example (third example) of the fourth modification of the content filling system according to one embodiment. FIG. 12H is a schematic plan view showing another example (fourth example) of the fourth modification of the content filling system according to one embodiment. FIG. 12I is a schematic plan view showing another example (fifth example) of the fourth modification of the content filling system according to one embodiment. FIG. 13 is a schematic plan view showing a fifth modification of the content filling system according to one embodiment. FIG. 14 is a schematic plan view showing another example of the fifth modified example of the content filling system according to one embodiment. FIG. 15 is a schematic cross-sectional view showing a filling nozzle of a filling device in another example of the fifth modified example of the contents filling system according to one embodiment. FIG. 16A is a schematic plan view showing a sixth modification of the content filling system according to one embodiment; FIG. 16B is a schematic cross-sectional view showing the water filling nozzle of the water filling device in the sixth modification of the content filling system according to one embodiment. FIG. 16C is a schematic cross-sectional view showing the undiluted solution filling nozzle of the undiluted solution filling device in the sixth modification of the contents filling system according to one embodiment. FIG. 17 is a schematic diagram showing a water sterilization line in a seventh modification of the contents filling system according to one embodiment. FIG. 18A is a schematic diagram showing a concentrate sterilization line in a ninth modification of the content filling system according to one embodiment. FIG. 18B is a schematic plan view showing an eleventh modification of the content filling system according to one embodiment. FIG. 18C is a schematic perspective view showing another example of the eleventh modification of the content filling system according to one embodiment. FIG. 19 is a flow chart showing a first modification of the content filling system sterilization method according to the embodiment. FIG. 20 is a flow chart showing another example of the first modification of the sterilization method for the content filling system according to the embodiment. FIG. 21 is a flow chart showing a second modification of the content filling system sterilization method according to the embodiment.

Embodiments of the present disclosure will be described below with reference to the drawings. 1 to 10E are diagrams illustrating one embodiment.

(content filling system)
First, a content filling system (aseptic filling system) according to an embodiment will be described with reference to FIG.

A content filling system 10 shown in FIG. 1 is a system for filling a bottle (container) 100 with content such as a beverage. Contents may be made by diluting the product stock solution with water. In this case, the undiluted product solution may be diluted with water by a factor of 1.1 to 100, preferably by a factor of 2 to 10. In addition, the undiluted product solution may be diluted with water by 10 to 80 times, may be diluted by 20 to 70 times, or may be diluted by 30 to 50 times. The bottle 100 can be produced by biaxially stretching blow molding a preform 100a produced by injection molding a synthetic resin material. Note that the bottle 100 may be produced by direct blow molding. As the material of the bottle 100, it is preferable to use a thermoplastic resin, particularly PE (polyethylene), PP (polypropylene), PET (polyethylene terephthalate), or PEN (polyethylene naphthalate). In addition, the container may be glass, can, paper, pouch, cup, or composite container thereof. In this embodiment, a case where a synthetic resin bottle is used as a container will be described as an example.

As shown in FIG. 1, the content filling system 10 includes a water sterilization line 50 for sterilizing water, a concentrate sterilization line 70 for sterilizing a product concentrate, and a filling line connected to the water sterilization line 50 and the concentrate sterilization line 70, respectively. A device (filler) 20 is provided. The content filling system 10 also includes a control section 90 that controls the filling device 20 . Furthermore, the content filling system 10 includes a bottle molding unit 30, a sterilization device (container sterilization device) 11, an air rinse device 14, the filling device 20 described above, and a cap mounting device (capper, seaming and capping machine). 16 and a product bottle unloading section 25 . The bottle forming section 30, the sterilizing device 11, the air rinsing device 14, the filling device 20, the cap attaching device 16, and the product bottle unloading section 25 are arranged in this order from the upstream side to the downstream side along the bottle 100 conveying direction. is set. A plurality of transport wheels 12 are provided between the air rinse device 14, the filling device 20, the cap attaching device 16, and the like to transport the bottles 100 between these devices. First, the bottle forming section 30, the sterilizing device 11, the air rinsing device 14, the filling device 20, the cap attaching device 16, and the product bottle unloading section 25 will be described.

The bottle molding section 30 is configured to receive the preform 100 a from the outside and to mold the bottle 100 . The bottle molding section 30 is configured to convey the molded bottle 100 toward the sterilization device 11 . As a result, in the content filling system 10, the steps from supplying the preform 100a to molding the bottle 100, filling the bottle 100 with the content, and closing the bottle can be performed continuously. In this case, a preform 100a with a small volume is transported from outside to the filling system 10 instead of a bottle 100 with a large volume. Therefore, transportation costs can be reduced.

The bottle molding section 30 includes a preform conveying section 31 that conveys the preform 100a, and a blow molding section (container molding apparatus) 32 that molds the bottle 100 from the preform 100a by subjecting the preform 100a to blow molding. and a bottle conveying section 33 for conveying the molded bottle 100 .

Among them, the preform conveying section 31 includes a receiving section 34 , a heating section 35 and a delivery section 36 . Of these, the receiving section 34 is configured to receive the preforms 100 a supplied from the preform supply device 1 via the preform supply conveyor 2 . The receiving section 34 is provided with a preform sterilizing device 34a for sterilizing the preform 100a and a preform air rinsing device 34b for air rinsing the preform 100a. In the illustrated example, the receiving section 34 is provided with one preform sterilization device 34a and one preform air rinse device 34b. The number of preform sterilization devices 34a and preform air rinse devices 34b is not limited to this.

In the receiving section 34, the preform sterilizer 34a sprays the gas or mist of the aqueous hydrogen peroxide solution onto the preform 100a to sterilize the preform 100a (preliminary sterilization).

The sterilizing agent for sterilizing the preform 100a may have the property of inactivating microorganisms. Alcohols such as sodium oxide, potassium hydroxide, ethyl alcohol and isopropyl alcohol, chlorine dioxide, ozone water, acidic water, and surfactants may be used alone, or two or more of these may be used in combination. .

By sterilizing the preform 100a in advance (preliminary sterilization) by the preform sterilizing device 34a in this way, the bacteria adhering to the bottle 100 produced from the preform 100a can be reduced. Therefore, the amount of hydrogen peroxide used in the sterilizer 11 for sterilizing the bottles 100 can be reduced, and the sterilization time can be shortened. Here, in general, the amount of sterilant used to sterilize the small-volume preform 100 a may be less than the amount of sterilant used to sterilize the bottle 100 . Therefore, by pre-sterilizing the preform 100a, the total amount of disinfectant used can be reduced.

In addition, since the amount of hydrogen peroxide used in the sterilization device 11 can be reduced and the sterilization time can be shortened, the size of the sterilization device 11 can be reduced. Moreover, since the sterilization time for sterilizing the bottle 100 can be shortened, the thermal load on the bottle 100 can be reduced. Therefore, deformation of the bottle 100 due to the heat of the sterilizing agent can be suppressed even if the bottle 100 is made of lightweight or recycled PET.

Furthermore, since pre-sterilization of the preform 100a can reduce bacteria adhering to the bottle 100, the sterilization conditions in the sterilization device 11 may be weakened. Here, in general, in order to improve the sterilization effect in the sterilization device 11, the body of the bottle 100 is cooled by supplying hot water from a mold temperature controller (not shown) to the mold in the blow molding unit 32. It's heat set. As a result, the sterilization effect of the sterilization device 11 can be improved, and shrinkage of the bottles 100 in the sterilization device 11 can be reduced. However, in the present embodiment, as described above, by pre-sterilizing the preform 100a, the amount of bacteria adhering to the bottle 100 can be reduced. Therefore, the blow molding section (container molding device) 32 may mold the bottle 100 without adjusting the temperature of the bottle 100 with hot water. That is, in the blow molding section 32, the hot water that has been supplied to the mold for improving the sterilization effect does not have to be supplied to the mold. As a result, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Moreover, since hot water need not be supplied to the mold of the blow molding section 32, the blow molding section 32 can be simplified. Moreover, since the blow molding part 32 can be simplified, the amount of heat applied to the bottle 100 can be reduced. Therefore, shrinkage of the bottle 100 in the sterilization device 11 can be reduced even when the hot water described above is not supplied to the mold.

Note that such a sterilization process may be performed not only in the receiving section 34 but also in the heating section 35 or the delivery section 36 . Also, the sterilization process may be performed between the bottle conveying section 33 and the filling device 20 after the bottle 100 is molded. Furthermore, sterilization may be performed at multiple locations. In the sterilization treatment, bacteria may be inactivated by ultraviolet irradiation, electron beam irradiation, or the like without using a sterilizing agent.

Referring to FIG. 1, the preform air rinsing device 34b described above is provided downstream of the preform sterilizing device 34a. The preform 100a sprayed with the disinfectant is dried with hot air in the preform air rinsing device 34b. At this time, the hot air is preferably supplied to the preform 100a with the mouth of the preform 100a facing downward. As a result, foreign matter can be effectively removed from inside the preform 100a. Therefore, the step of washing the preform 100a with sterile water can be omitted, and the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Note that the preform air-rinsing device 34b may not be provided in the receiving section 34 . Further, in the receiving section 34, a foreign matter removing device (not shown) for removing foreign matter adhering to the preform 100a may be provided on the upstream side of the preform sterilizing device 34a.

The heating unit 35 is configured to receive the preform 100a from the receiving unit 34 and heat the preform 100a while conveying it. The heating unit 35 is provided with a heater 35a for heating the preform 100a. This heater 35a may be, for example, an infrared heater. The heater 35a heats the preform 100a to, for example, about 90° C. or higher and 130° C. or lower. In addition, the temperature of the mouth portion of the preform 100a is suppressed to 70° C. or less in order to prevent deformation or the like.

The delivery section 36 is configured to receive the preform 100 a heated by the heating section 35 and deliver it to the blow molding section 32 .

The blow molding section 32 includes a mold (not shown). The bottle 100 is formed by subjecting the preform 100a to blow molding using this mold. Then, the molded bottle 100 is conveyed downstream by the bottle conveying section 33 .

Here, between the bottle molding section 30 and the sterilization device 11, an adjustment conveying section 5 that receives the bottles 100 from the bottle conveying section 33 and transfers the bottles 100 to the sterilization device 11 is provided. At least a portion of the adjustment transport section 5 is housed inside an atmosphere shielding chamber 70c (described later) provided upstream of a sterilant spray chamber 70d (described later). In the illustrated example, the adjustment transport section 5 is arranged so as to straddle a molding section chamber 70b (described later) that houses the bottle molding section 30 and an atmosphere shielding chamber 70c. Since at least a portion of the adjustment conveying unit 5 is housed inside the atmosphere shielding chamber 70c in this way, the sterilant gas or mist generated in the sterilant spray chamber 70d or a mixture thereof is formed. It is possible to suppress the flow into the partial chamber 70b.

In the example shown, a single transport wheel 12 is provided between the conditioning transport 5 and the bottle transport 33 of the bottle forming station 30 . That is, between the blow molding section 32 of the bottle molding section 30 and the sterilization device 11, the bottle conveying section 33 of the bottle molding section 30, the single conveying wheel 12 and the adjustment conveying section 5 are provided. As a result, the content filling system 10 can be made more compact than when a plurality of conveying wheels 12 are provided between the adjusting conveying section 5 and the bottle conveying section 33 of the bottle molding section 30 . Although not shown, only the adjusting/conveying section 5 may be provided between the blow molding section 32 of the bottle molding section 30 and the sterilization device 11 . In this case, the content filling system 10 can be made more compact.

The sterilization device 11 is a device that sterilizes the bottles 100 by injecting a sterilizing agent onto the bottles 100 . This sterilizes the bottle 100 with a sterilizing agent before filling with contents. As the disinfectant, for example, an aqueous hydrogen peroxide solution is used. In the sterilization device 11 , gas or mist of the aqueous hydrogen peroxide solution is generated, and the gas or mist is sprayed on the inner and outer surfaces of the bottle 100 . Since the bottle 100 is sterilized by the gas or mist of the aqueous hydrogen peroxide solution in this manner, the inner and outer surfaces of the bottle 100 are sterilized evenly.

The air rinsing device 14 is a device that removes foreign substances, hydrogen peroxide, etc. from the inside of the bottle 100 while activating the hydrogen peroxide by supplying sterile heated air or normal temperature air to the bottle 100 . At this time, it is preferable that aseptic air is supplied to the bottle 100 with the mouth portion of the bottle 100 facing downward. As a result, foreign matter can be effectively removed from inside the bottle 100 . Therefore, the step of washing the bottle 100 with sterile water can be omitted, and the amount of carbon dioxide emitted by the content filling system 10 can be reduced. If necessary, sterilized air at room temperature may be mixed with condensed mist of low-concentration hydrogen peroxide to gasify the hydrogen peroxide and supply it to the bottle 100 .

The filling device 20 is a device that fills the bottle 100 with water and product concentrate. That is, the filling device 20 fills the bottle 100 with pre-sterilized water and product concentrate from the mouth of the bottle 100 . As a result, the empty bottle 100 is filled with the content prepared by diluting the undiluted product in the filling device 20 . In the filling device 20, the contents are filled into the bottles 100 while the bottles 100 are rotationally conveyed.

The filling device 20 may have a water filling device 21 connected to the water sterilization line 50 and a concentrate filling device 22 connected to the concentrate sterilization line 70 . The water filling device 21 and the concentrate filling device 22 are arranged in this order from the upstream side to the downstream side along the transport direction of the bottle 100 . The water filling device 21 is arranged inside a first aseptic chamber 70f, which will be described later. The undiluted solution filling device 22 is arranged inside a second aseptic chamber 70h, which will be described later. The water filling device 21 and the undiluted solution filling device 22 may each be a so-called rotary filler.

The water filling device 21 fills the bottle 100 with sterilized water. In this case, the water filling device 21 fills the empty bottle 100 with sterilized water. On the other hand, the concentrate filling device 22 fills a bottle filled with water with a sterilized product concentrate. In this way, since the filling device 20 has the water filling device 21 and the concentrate filling device 22, the product concentrate or the contents can be The size of the touching filling device (that is, the concentrate filling device 22) can be reduced. Therefore, as will be described later, the area for cleaning and sterilizing the filling device 20 can be narrowed.

The filling speed at which the water filling device 21 fills the bottle 100 with water may be faster than the filling speed at which the concentrate filling device 22 fills the bottle 100 with the product concentrate. That is, the water filling device 21 fills the empty bottle 100 with water, so that the water filling speed can be increased. Here, when the bottle 100 is vigorously filled with the contents, for example, foaming in the bottle 100 may cause a part of the contents to scatter outside from the mouth of the bottle 100 . Then, there is a possibility that the surroundings of the bottle 100 will be stained by the contents due to the contents scattered to the outside. On the other hand, when the empty bottle 100 is filled with water, even if the water scatters outside from the mouth of the bottle 100, the periphery of the bottle 100 will not be stained. Therefore, the filling speed of water can be increased. As a result, the number of water filling nozzles (for example, see FIG. 16B described later) of the water filling device 21 can be reduced. Therefore, the size of the water filling device 21 can be reduced.

In the water filling device 21, the water filling speed may be 100 mL/sec or more and 500 mL/sec or less, preferably 200 mL/sec or more and 400 mL/sec or less. Since the water filling speed is 100 mL/sec or more, the number of water filling nozzles of the water filling device 21 can be further reduced. Therefore, the size of the water filling device 21 can be made smaller. Further, since the water filling speed is 500 mL/sec or less, it is possible to prevent the water from splashing outside from the mouth of the bottle 100 when the bottle 100 is filled with water. For this reason, it is possible to suppress variations in the volume of the contents and the ratio of dilution of the undiluted product between the product bottles 101 . In addition, in the undiluted solution filling device 22, the filling speed of the undiluted product may be 30 mL/sec or more and 200 mL/sec or less.

The capping device 16 is a device that caps the bottle 100 by attaching a cap 88 to the bottle 100 . In the capping device 16, the bottle 100 filled with water and the product concentrate (contents) is closed with a cap 88, and the inside of the bottle 100 is sealed so that outside air and microorganisms do not enter. In the cap attaching device 16, caps 88 are attached to the mouths of the plurality of bottles 100 filled with contents while they are being rotated (revolved). By attaching the cap 88 to the bottle 100 in this manner, the product bottle 101 is obtained.

The cap 88 is sterilized in advance by the cap sterilizer 18 . The cap sterilizer 18 is located outside the second sterile chamber 70h (described below) and near the capping device 16, for example. In the cap sterilizing device 18 , a large number of caps 88 brought in from outside the contents filling system 10 are collected in advance and conveyed in a line toward the cap attaching device 16 . On its way to the capping device 16, the cap 88 is blown with hydrogen peroxide gas or mist against the inner and outer surfaces of the cap 88, then dried with hot air and sterilized.

The product bottle unloading section 25 continuously unloads the product bottles 101 attached with the caps 88 by the cap attaching device 16 to the outside of the content filling system 10 .

The contents filling system 10 includes a preform sterilization chamber 70a, a molding section chamber 70b, an atmosphere isolation chamber 70c, a sterilant spray chamber 70d, an air rinse chamber (fourth aseptic chamber) 70e, and a first aseptic chamber. It has a chamber 70f, an intermediate area chamber (third sterile chamber) 70g, a second sterile chamber 70h and an exit chamber 70i. Between the first aseptic chamber 70f and the second aseptic chamber 70h, an intermediate area chamber (third aseptic chamber) 70g connecting the first aseptic chamber 70f and the second aseptic chamber 70h is provided. . An air rinse chamber (fourth aseptic chamber) 70e is provided upstream of the first aseptic chamber 70f. preform sterilization chamber 70a, molding section chamber 70b, atmosphere isolation chamber 70c, sterilant spray chamber 70d, air rinse chamber 70e, first aseptic chamber 70f, intermediate area chamber 70g, second aseptic chamber 70h, and exit chamber 70i. are arranged in this order from the upstream side to the downstream side along the conveying direction of the preform 100 a and the bottle 100 .

Each chamber 70a-70i is separated by a partition wall. The partition prevents the sterilant or the like from flowing in an unintended direction between the chambers 70a to 70i, and serves to stabilize the pressure in each chamber 70a to 70i. In addition, the partition wall is formed with a gap through which the preform 100a or the bottle 100 can pass. This gap is formed to be at least as large as, for example, one preform 100a or bottle 100 so that the pressure in each of the chambers 70a to 70i does not change. Moreover, the partition wall may be provided with a shutter that closes the gap described above. This shutter may be configured to automatically open and close in response to a signal from the control section 90, for example.

Among the chambers 70a to 70i, the preform sterilization chamber 70a accommodates the preform sterilizer 34a and the like.

The blow molding section 32 of the bottle molding section 30 and the like are housed inside the molding section chamber 70b.

At least a portion of the adjustment transfer section 5 is accommodated inside the atmosphere cutoff chamber 70c. Also, a camera may be provided inside the atmosphere cutoff chamber 70c. Then, by using a camera, it may be inspected whether or not the bottle 100 has any problem in molding. Furthermore, a thermometer may be provided inside the atmosphere shielded chamber 70c. Then, the temperature of the bottle 100 before sterilization may be measured by this thermometer. Here, the temperature of the bottle 100 is one of the important factors that affect the sterilization efficiency of the bottle 100 . That is, by keeping the temperature of the bottle 100 at an appropriate temperature, the sterilization efficiency of the bottle 100 can be improved. Therefore, by measuring the temperature of the bottle 100 before sterilization with a thermometer, the temperature of the bottle 100 during sterilization can be kept at an appropriate temperature, and the sterilization efficiency of the bottle 100 can be improved.

The sterilizer 11 is housed inside the sterilant spray chamber 70d. Further, the air rinse device 14 is housed inside the air rinse chamber 70e.

The water filling device 21 of the filling device 20 is housed inside the first aseptic chamber 70f. Further, the undiluted solution filling device 22 and the cap attaching device 16 of the filling device 20 described above are housed inside the second aseptic chamber 70h. Furthermore, the product bottle unloading section 25 is housed inside the outlet chamber 70i. Note that only the transport wheels 12 may be housed inside the intermediate area chamber 70g.

Inside the preform sterilization chamber 70a, the sterilant spray chamber 70d, the air rinse chamber 70e, the first aseptic chamber 70f, the intermediate area chamber 70g, the second aseptic chamber 70h and the exit chamber 70i described above, the pressure in each chamber is A pressure gauge (not shown) is attached to measure. A pressure gauge for measuring the pressure in each chamber may also be attached to the molding section chamber 70b and/or the atmosphere shielding chamber 70c.

Here, as described above, the contents filling system 10 includes the control section 90 that controls the filling device 20 . The controller 90 is electrically connected to the filling device 20 and controls the water filling device 21 and the concentrate filling device 22 of the filling device 20 . In addition, the control unit 90 is electrically connected to the water sterilization line 50, the undiluted solution sterilization line 70, the bottle molding unit 30, the sterilization device 11, the air rinse device 14, the cap mounting device 16, the product bottle unloading unit 25, and the cap sterilization device 18. Alternatively, the controller 90 may control the water sterilization line 50 and the like.

This control unit 90 may clean and sterilize the inside of each chamber, and may clean and sterilize a water sterilizer 60 and the like of the water sterilization line 50, which will be described later. In the present embodiment, the control unit 90 cleans the inside of the second aseptic chamber 70h (hereinafter, the cleaning inside each chamber is also referred to as COP) while the inside of the first aseptic chamber 70f is maintained in a sterile state. In addition, the control unit 90 cleans the undiluted solution filling device 22 while maintaining the inside of the first aseptic chamber 70f in a sterile state (hereinafter, cleaning of the inside of the filling device 20 such as the undiluted solution filling device 22 is called CIP (Cleaning in Place). ) is also written). That is, when cleaning the inside of the second aseptic chamber 70h and the undiluted solution filling device 22, the control unit 90 sterilizes the inside of the first aseptic chamber 70f without cleaning (COP) the inside of the first aseptic chamber 70f. keep maintained. In addition, the control unit 90 maintains the inside of the first aseptic chamber 70f in a sterile state without cleaning (CIP) the water filling device 21 when cleaning the inside of the second aseptic chamber 70h and the undiluted solution filling device 22. keep state.

As described above, the first aseptic chamber 70f accommodates the water filling device 21 for filling sterilized water. The periphery of the water filling device 21 and the water flow path in the water filling device 21 are free from contamination due to the contents. Therefore, even if the first sterile chamber 70f is not cleaned (COP) or sterilized (hereinafter, sterilization in each chamber is also referred to as SOP) when switching the type of contents, the first sterile Hygiene in the chamber 70f can be maintained. Also, at this time, even if the water filling device 21 housed in the first aseptic chamber 70f is not cleaned (CIP) or sterilized (SIP (Sterilization in Place)), the sanitation of the water filling device 21 can be maintained, and the previous content can be prevented from being mixed with the next content. In this way, when the inside of the first aseptic chamber 70f is not washed when the inside of the second aseptic chamber 70h is washed, the number of times of washing the inside of the first aseptic chamber 70f can be reduced, and in the contents filling system 10, washing The area to be processed can be narrowed. Therefore, the amount of water, steam, electricity and cleaning agent used can be reduced. Moreover, since the area to be cleaned can be narrowed, the cleaning time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Further, the controller 90 sterilizes (SOP) the inside of the second aseptic chamber 70h while maintaining the inside of the first aseptic chamber 70f in an aseptic state. In addition, the control unit 90 sterilizes (SIP) the undiluted solution filling device 22 while maintaining the inside of the first sterile chamber 70f in a sterile state. That is, when sterilizing the inside of the second aseptic chamber 70h and the stock solution filling device 22, the control unit 90 sterilizes the inside of the first aseptic chamber 70f without sterilizing (SOP) the inside of the first aseptic chamber 70f. keep maintained. In addition, when sterilizing the inside of the second aseptic chamber 70h and the undiluted solution filling device 22, the control unit 90 did not sterilize (SIP) the water filling device 21, and maintained the inside of the first aseptic chamber 70f in a sterile state. keep state. Thereby, the area to be sterilized can be narrowed. Therefore, the amount of steam used can be reduced. Moreover, sterilization time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Preferably, the pressure in the first sterile chamber 70f mentioned above is higher than the pressure in the second sterile chamber 70h. This can prevent the air in the second sterile chamber 70h from entering the first sterile chamber 70f. Therefore, the sterile condition inside the first sterile chamber 70f can be favorably maintained.

When cleaning and sterilizing the inside of the second aseptic chamber 70h, the pressure inside the first aseptic chamber 70f is preferably 40 Pa or more and 100 Pa or less, and the pressure inside the second aseptic chamber 70h is preferably 0 Pa or more and 20 Pa or less. is preferred. Also, when cleaning and sterilizing the undiluted solution filling device 22, the pressure in the first aseptic chamber 70f is preferably 40 Pa or more and 100 Pa or less, and the pressure in the second aseptic chamber 70h is preferably 0 Pa or more and 20 Pa or less. is preferred. As a result, it is possible to effectively prevent the air in the second aseptic chamber 70h from entering the first aseptic chamber 70f, and the aseptic state inside the first aseptic chamber 70f can be maintained even better. When producing the product bottle 101, the pressure in the first aseptic chamber 70f is preferably 30 Pa or more and 60 Pa or less, and the pressure in the second aseptic chamber 70h is preferably 10 Pa or more and 40 Pa or less. preferable.

Also, the pressure in the intermediate area chamber (third aseptic chamber) 70g is preferably lower than the pressure in the first aseptic chamber 70f and greater than or equal to the pressure in the second aseptic chamber 70h. Since the pressure in the intermediate area chamber 70g is lower than the pressure in the first aseptic chamber 70f, it is possible to suppress the air in the intermediate area chamber 70g from entering the first aseptic chamber 70f. Further, since the pressure in the intermediate area chamber 70g is equal to or higher than the pressure in the second aseptic chamber 70h, it is possible to suppress the air in the second aseptic chamber 70h from entering the intermediate area chamber 70g. Therefore, the air in the second aseptic chamber 70h can be prevented from entering the first aseptic chamber 70f via the intermediate area chamber 70g. As a result, the sterile condition inside the first sterile chamber 70f can be maintained well.

When cleaning and sterilizing the inside of the second aseptic chamber 70h, the pressure inside the intermediate area chamber 70g is preferably 10 Pa or more and 40 Pa or less. Moreover, when cleaning and sterilizing the undiluted solution filling device 22, the pressure in the intermediate area chamber 70g is preferably 10 Pa or more and 40 Pa or less. As a result, the air in the second sterile chamber 70h can be prevented from entering the intermediate area chamber 70g, and the sterile condition inside the first sterile chamber 70f can be maintained even better. In addition, when producing the product bottle 101, the pressure in the intermediate area chamber 70g is preferably 20 Pa or more and 50 Pa or less.

Also, the pressure in the air rinse chamber (fourth sterile chamber) 70e is preferably lower than the pressure in the first sterile chamber 70f. This can prevent the air in the air rinse chamber 70e from entering the first aseptic chamber 70f. Therefore, the sterile condition inside the first sterile chamber 70f can be favorably maintained.

When cleaning and sterilizing the inside of the second aseptic chamber 70h, the pressure inside the air rinse chamber 70e is preferably 10 Pa or more and 40 Pa or less. Further, when cleaning and sterilizing the undiluted solution filling device 22, the pressure in the air rinse chamber 70e is preferably 10 Pa or more and 40 Pa or less. As a result, the air in the air rinse chamber 70e can be prevented from entering the first aseptic chamber 70f, and the aseptic state inside the first aseptic chamber 70f can be maintained even better. In addition, when producing the product bottle 101, the pressure in the air rinse chamber 70e is preferably 10 Pa or more and 30 Pa or less.

Also, the pressure in the sterilant spray chamber 70d is preferably less than or equal to the pressure in the atmosphere isolation chamber 70c. As a result, the air inside the sterilant spraying chamber 70d can be prevented from entering the atmosphere shielding chamber 70c and the forming section chamber 70b. Here, by being able to suppress the air in the sterilant spraying chamber 70d from entering the molding section chamber 70b, it is possible to suppress an increase in humidity in the molding section chamber 70b. As described above, the blow molding section 32 of the bottle molding section 30 is housed inside the molding section chamber 70b. Therefore, by suppressing an increase in humidity in the molding section chamber 70b, it is possible to suppress corrosion of the machine that constitutes the blow molding section 32. FIG.

When cleaning and sterilizing the inside of the second aseptic chamber 70h, the pressure inside the sterilant spraying chamber 70d is preferably 0 Pa or more and 20 Pa or less. Moreover, when cleaning and sterilizing the undiluted solution filling device 22, the pressure in the sterilant spraying chamber 70d is preferably 0 Pa or more and 20 Pa or less. As a result, the air in the sterilant spraying chamber 70d can be prevented from entering the atmosphere shut-off chamber 70c and the molding section chamber 70b, and an increase in humidity within the molding section chamber 70b can be suppressed. When producing the product bottle 101, the pressure inside the sterilant spraying chamber 70d is preferably -10 Pa or more and 10 Pa or less.

When cleaning and sterilizing the inside of the second aseptic chamber 70h, the pressure inside the outlet chamber 70i is preferably 0 Pa or more and 20 Pa or less. Moreover, when cleaning and sterilizing the undiluted solution filling device 22, the pressure in the outlet chamber 70i is preferably 0 Pa or more and 20 Pa or less. As a result, the air in the exit chamber 70i can be prevented from entering the first aseptic chamber 70f via the second aseptic chamber 70h, etc., and the aseptic state inside the first aseptic chamber 70f can be maintained even better. In addition, when producing the product bottle 101, the pressure in the outlet chamber 70i is preferably 10 Pa or more and 20 Pa or less.

In summary, the pressure in the sterilant spray chamber 70d through the exit chamber 70i may be as shown in Table 1 below.

At this time, the pressures in the preform sterilization chambers 70a to 70c may be set as shown in Table 2 below.

Such a content filling system 10 may comprise, for example, an aseptic filling system. In this case, the interiors of the disinfectant spray chamber 70d, the air rinse chamber 70e, the first sterile chamber 70f, the intermediate area chamber 70g, the second sterile chamber 70h and the outlet chamber 70i are kept sterile. A chamber (not shown) may be provided downstream of the exit chamber 70i to connect the sterile zone in a sterile state and the non-sterile zone in a non-sterile state.

Next, the water sterilization line 50 and the concentrate sterilization line 70 of the content filling system 10 will be described. Here, first, the water sterilization line 50 will be explained.

Water Sterilization Line The water sterilization line 50 is a sterilization line for non-heat sterilization of water. This water sterilization line 50 may sterilize water with ultraviolet rays. In this case, in the water sterilization line 50, water may be sterilized by ultraviolet light from at least one of the low pressure mercury lamp and the medium pressure mercury lamp. Moreover, the water sterilization line 50 may sterilize water by filtering the water through a sterile filter (first sterile filter 63 or the like, which will be described later). In this specification, the term "non-heat sterilization" refers to sterilizing water without using thermal energy such as an electric heater or steam.

As shown in FIG. 2A, the water sterilization line 50 has at least a water sterilizer 60 for sterilizing water. In the example shown in FIG. 2A, the water sterilization line 50 has a first water tank 51, a water sterilizer 60 and a second water tank 52. In the example shown in FIG. The water sterilization line 50 is provided on the upstream side of the first water tank 51, and includes a pure water manufacturing device 50a that manufactures water (pure water) and water (pure water) supplied from the pure water manufacturing device 50a. It may further have a pure water tank 50c for storing. The pure water production device 50a, the pure water tank 50c, the first water tank 51, the water sterilizer 60, and the second water tank 52 are arranged in this order from the upstream side to the downstream side along the water conveying direction. ing.

Of these, the pure water tank 50c is a tank that stores water (pure water) supplied from the pure water manufacturing device 50a, which is a water supply source. Here, as raw water for soft drinks, it is obligatory to use water for food manufacturing as stipulated by the Food Sanitation Law. The food manufacturing water is pure water produced by a pure water production device 50a equipped with activated carbon, a reverse osmosis membrane, an ion exchange resin (including EDI), or the like. Pure water is water from which impurities such as calcium, magnesium, chlorine, iron or minerals have been removed. In this case, the evaporation residue of pure water is 20 mg/L or less. Furthermore, pure water has an electric conductivity of 0.1 μS/cm or more and 20 μS/cm or less. As will be described later, in this embodiment, water is sterilized by ultraviolet light. Therefore, by setting the electrical conductivity of the water to be sterilized to 20 μS/cm or less, it is possible to suppress the adhesion of inorganic substances (oxides such as calcium) and the like to the surfaces of the first ultraviolet lamp 67a and the like, which will be described later. Therefore, it is possible to prevent deterioration of the ultraviolet transmittance.

This pure water tank 50c plays a role of facilitating the flow of water by storing water. The volume of the pure water tank 50c may be 50 m ³ or more and 100 m ³ or less, and may be 50 m ³ as an example.

Also, the number of bacteria in the pure water tank 50c is preferably 0.001 CFU/mL or more and 20 CFU/mL or less. The pure water supplied to the pure water tank 50c is produced by removing chlorine from tap water with activated carbon or the like. As a result, bacteria easily grow in the pure water supplied to the pure water tank 50c. Therefore, it is preferable to install a UV lamp in the pure water tank 50c to suppress the growth of bacteria. When the number of bacteria in the pure water tank 50c exceeds 20 CFU/mL, it is preferable to sterilize the pure water tank 50c with chlorine, hot water, steam, or the like. The number of bacteria in the pure water tank 50c may be constantly monitored and controlled to be within the above range. As a result, sterilized water can be produced without providing additional equipment. Therefore, the amount of carbon dioxide emitted by the water sterilizer 60 can be reduced without increasing the cost of the water sterilizer 60 .

A pre-stage sterilizer 62A and a first water tank 51 are provided downstream of the pure water tank 50c.

Here, when the bacteria count concentration supplied from the pure water production apparatus 50a is high (for example, 1 CFU/ml or more), and the foreign matter removal filter 61 described later has a pore size of a bacteria elimination filter (0.1 μm or more and 1 μm or less), If there is, the foreign matter removal filter 61 can be contaminated with bacteria in a short period of time. When a large amount of bacteria are captured by the foreign matter removal filter 61 and grow, the quality of water may be affected. Therefore, as shown in FIG. 2A, it is preferable that a pre-stage sterilizer 62A is installed upstream of the foreign matter removing filter 61. As shown in FIG. This makes it possible to produce sterile water of good quality for a long period of time. In the example shown in FIG. 2A, two pre-stage sterilizers 62A are provided on the upstream side of the foreign matter removal filter 61 . Specifically, the pre-stage sterilizer 62A is provided on the upstream side of the foreign matter removing filter 61 and on the upstream side and the downstream side of the first water tank 51, respectively. In addition, the number of pre-stage sterilizers 62A may be one, and may be provided only on one of the upstream side and the downstream side of the first water tank 51 . In this case, the cost for sterilizing water can be reduced.

The first water tank 51 is a so-called balance tank, and serves to smooth the flow of water by storing water. The volume of the first water tank 51 may be 30 m ³ or more and 100 m ³ or less, and may be 50 m ³ as an example.

A pump P<b>1 for conveying water and a flow meter F for measuring the flow rate of water may be provided downstream of the first water tank 51 . The pump P1 and the flowmeter F may be provided in this order from the upstream side toward the downstream side along the water transport direction. Note that the installation location of the flowmeter F may be changed as appropriate as long as it is downstream of the pump P1 and upstream of a valve V1, which will be described later. Further, downstream of the flowmeter F, the water sterilizer 60 described above is provided.

The water sterilizer 60 is a sterilizer that sterilizes water stored in the first water tank 51 . Details of the water sterilizer 60 will be described later.

The second water tank 52 is a tank (so-called aseptic tank) that stores water sterilized by the water sterilizer 60 . This second water tank 52 plays a role of facilitating the flow of water by storing sterilized water. The volume of the second water tank 52 may be 5 m ³ or more and 50 m ³ or less, and may be 10 m ³ as an example.

Further, an auxiliary filter 53 for filtering sterilized water and a third water tank 54 for storing water that has passed through the auxiliary filter 53 may be provided downstream of the second water tank 52 . In this case, the third water tank 54 may be a so-called filling machine tank, and may be installed vertically above the water filling device 21 in order to improve the filling accuracy of the water filling device 21 . The third water tank 54 may serve as a so-called cushion tank that ensures a smooth flow of water even when the amount of water used on the downstream side of the third water tank 54 changes. The volume of the third water tank 54 may be 0.1 m ³ or more and 1 m ³ or less, and may be 0.3 m ³ as an example.

Further, even if a first bypass line (bypass line) 55 (see FIGS. 1 and 2A, etc.) that connects the water sterilization line 50 and the cap sterilization device 18 to each other is provided on the downstream side of the second water tank 52 good. As a result, the water sterilized by the water sterilizer 60 can be used for washing the cap 88 . Here, the cap 88 can be washed with sterile water after being sterilized with a disinfectant. As a result, the cap 88 is cooled, and the foreign matter adhering to the cap 88 is removed. Also, by washing the cap 88 with sterile water, the sterile water adhering to the cap 88 can reduce the friction between the cap 88 and a transport chute (not shown) that transports the cap 88 . Therefore, it is possible to prevent the cap 88 from being scraped by the transport chute when the cap 88 is transported.

As described above, since the first bypass line 55 is provided downstream of the second water tank 52 , the water sterilized by the water sterilizer 60 can be used for washing the cap 88 . Therefore, compared to the case where the cap 88 is washed with sterile water produced using a sterilizer that heats and sterilizes water, the amount of carbon dioxide emitted by the content filling system 10 can be further reduced. . Incidentally, by appropriately setting the sterilization conditions, the conveying speed and/or the material of the cap 88, the cap 88 can be conveyed without being scraped off. Thus, if the cap 88 is not scraped, the cap 88 does not have to be washed with sterile water.

Furthermore, a second bypass line 56 may be provided downstream of the second water tank 52 to connect the water sterilization line 50 and the second aseptic chamber 70h to each other. When cleaning the inside of the second aseptic chamber 70h, the controller 90 may supply the water sterilized by the water sterilization line 50 to the second aseptic chamber 70h via the second bypass line 56. Further, when cleaning the undiluted solution filling device 22, the controller 90 may supply the water sterilized by the water sterilization line 50 to the second aseptic chamber 70h via the second bypass line 56. As a result, compared to the case where the inside of the second aseptic chamber 70h is washed with aseptic water produced using a sterilizer that heats and sterilizes water, the amount of carbon dioxide emitted by the content filling system 10 can be further reduced.

In the second aseptic chamber 70h, the undiluted product filling device 22 fills the bottle 100 with the undiluted product. Here, after filling the bottle 100 with the product concentrate (content), the mouth of the bottle 100 can be washed. When washing the mouth of the bottle 100 in this manner, water supplied to the second aseptic chamber 70h through the second bypass line 56 may be used. This reduces the amount of carbon dioxide emitted by the content filling system 10 compared to washing the mouth of the bottle 100 with sterile water produced using a sterilizer that heats and sterilizes water. can be further reduced. In addition, when the product concentrate (contents) does not adhere to the mouth of the bottle 100, the mouth of the bottle 100 does not have to be washed. Moreover, even if the product undiluted solution adheres to the mouth of the bottle 100, the mouth of the bottle 100 does not have to be washed if there is no possibility of bacterial growth.

The second bypass line 56 may connect the water sterilization line 50 and each of the chambers 70a to 70i with each other. When cleaning the chambers 70a to 70i, the water sterilized by the water sterilization line 50 may be supplied to the chambers 70a to 70i through the second bypass line 56. FIG. Also, water that has been sterilized in the water sterilization line 50 may be supplied to each chamber 70a to 70i through the second bypass line 56 when cleaning the machines arranged in each chamber 70a to 70i.

Further, as shown in FIG. 2A, a circulation line (first circulation line) 59 may be connected to the water sterilization line 50 upstream of the second water tank 52 . One end of the circulation line 59 may be connected to the water sterilization line 50 via a valve V1 provided on the water sterilization line 50 . The other end of the circulation line 59 may be connected to the first water tank 51 of the water sterilization line 50 . As a result, a circulation system ( 1st circulation system) 59A may be comprised. Further, a thermometer T may be provided in the circulation line 59 . Further, the circulation line 59 may be provided with a densitometer 59c for measuring the concentration of the disinfectant or cleaning agent when the water sterilizer 60 is sterilized. Furthermore, the circulation line 59 may be provided with a temperature raising device (heat exchanger, heater, etc.) for warming the sterilant or the like when cleaning and/or sterilizing the circulation line 59 . The valve V<b>1 may be electrically connected to the controller 90 or controlled by the controller 90 .

Moreover, as shown in FIG. 2B, a circulation line (second circulation line) 95 may be connected between the first water tank 51 of the water sterilization line 50 and the water sterilizer 60 . One end of this circulation line 95 may be connected to a sampling line SL connected to a sampling point SP5, which will be described later. The other end of the circulation line 95 may be connected, for example, between the pump P1 provided downstream of the first water tank 51 and the pre-stage sterilizer 62A. Also, the other end of the circulation line 95 may be connected to, for example, the upstream side of the pump P1 (for example, between the first water tank 51 and the pump P1). As a result, a circulation system (second 2 circulation system) 95A may be configured. In addition, the circulation line 95 may be provided with a sterilant supply unit 96 including a tank, pump, heater, concentration meter and the like (not shown). A heat exchanger 97 may be provided in the circulation line 95 . A circulation system 95A including such a circulation line 95 may be used to circulate a sterilant or cleaning agent when sterilizing the water sterilizer 60, as described later.

Furthermore, one end of the circulation line 95 may be connected between the second sterilizer 64 and the first sterile filter 63, for example, as shown in FIG. 2C. Thereby, the circulation system (second circulation system) 95A may be configured by the pre-stage sterilizer 62A, the third bypass line 95a described later, the first sterilizer 62, the second sterilizer 64, and the circulation line 95. .

<Water sterilizer>
Next, the water sterilizer 60 will be explained. This water sterilizer 60 is a sterilizer that sterilizes water used in the content filling system 10 . In this embodiment, the water sterilizer 60 sterilizes water without heating. As described above, the water sterilizer 60 sterilizes water (pure water) stored in the first water tank 51 . Therefore, the water sterilizer 60 sterilizes water whose electric conductivity is 0.1 μS/cm or more and 20 μS/cm or less.

As shown in FIGS. 2A and 2B, the water sterilizer 60 includes at least one sterile filter (first sterile filter 63 and second sterile filter 65). Also, the water sterilizer 60 includes at least one sterilizer (first sterilizer 62 and second sterilizer 64). In the example shown in FIGS. 2A and 2B, the water sterilizer 60 includes a foreign matter removal filter 61, a first sterilizer 62, a first sterile filter 63, a second sterilizer 64, and a second sterile filter 65. It has The foreign substance removing filter 61, the first sterilizer 62, the first sterile filter 63, the second sterilizer 64, and the second sterile filter 65 are arranged in this order from the upstream side to the downstream side along the water transport direction. It is At this time, as shown in FIG. 2C, the foreign matter removing filter 61, the first sterilizer 62, the second sterilizer 64, the first sterile filter 63, and the second sterile filter 65 are arranged upstream along the water conveying direction. to the downstream side in this order.

Further, as shown in FIG. 2D, the water sterilizer 60 may include a foreign matter removal filter 61, a first sterilizer 62, a first sterile filter 63, and a second sterile filter 65. The foreign matter removing filter 61, the first sterilizer 62, the first sterile filter 63, and the second sterile filter 65 may be arranged in this order from the upstream side to the downstream side along the water transport direction. In this case, the water sterilizer 60 may further include a second sterilizer 64 provided between the first sterile filter 63 and the second sterile filter 65 .

The water sterilizer 60 may also include a first sterilizer 62, a first sterile filter 63, and a second sterile filter 65, as shown in FIG. 2E. The first sterilizer 62, the first sterile filter 63, and the second sterile filter 65 may be arranged in this order from the upstream side toward the downstream side along the water conveying direction. In this case, the water sterilizer 60 may further include a second sterilizer 64 provided between the first sterile filter 63 and the second sterile filter 65 .

Further, the water sterilizer 60 may comprise a first sterilizer 62 and a first sterile filter 63, as shown in FIG. 2F. The first sterilizer 62 and the first sterile filter 63 may be arranged in this order from the upstream side to the downstream side along the water transport direction. In this case, the water sterilizer 60 may further include a second sterilizer 64 provided between the first sterile filter 63 and a valve V1, which will be described later.

Next, the foreign substance removing filter 61, the first sterilizer 62, the first sterile filter 63, the second sterilizer 64 and the second sterile filter 65 will be described. First, the foreign matter removing filter 61 will be described.

The foreign matter removing filter 61 is a filter that removes foreign matter in water. The mesh size (filtering accuracy) of the foreign matter removing filter 61 may be, for example, 0.45 μm or more and 10 μm or less. Moreover, it is preferable that the mesh size of the foreign matter removing filter 61 is large enough to remove fungi (mold, yeast, etc.). As will be described later, in the first sterilizer 62 and the like provided downstream of the foreign matter removing filter 61, water is irradiated with ultraviolet rays. For this reason, the mesh size of the foreign matter removing filter 61 is preferably large enough to remove molds that are resistant to ultraviolet rays, and is preferably 0.45 μm or more and 1.0 μm or less. In order to improve the sterility of the water that has passed through the foreign matter removing filter 61 , a sterile grade filter with an opening of 0.1 μm or more and 0.22 μm or less may be used as the foreign matter removing filter 61 .

The first sterilizer 62 is provided downstream of the foreign matter removing filter 61 . Also, the first sterilizer 62 is provided upstream of the first sterile filter 63 . The first sterilizer 62 is a sterilizer that sterilizes water with ultraviolet rays. As a result, bacteria (bacteria other than mold and yeast) that have passed through the foreign matter removal filter 61 can be sterilized. In addition, since the first sterilizer 62 sterilizes water with ultraviolet light, the amount of carbon dioxide emitted by the content filling system can be reduced compared to the case where water is sterilized by heating. In particular, as described above, when making the contents, the product stock solution can be diluted with water by a factor of 1.1 to 100, preferably by a factor of 2 to 10. When the undiluted product solution is diluted with water to 2 to 10 times, 50 to 90% of the content is water. Therefore, by sterilizing the water without heating, the amount of carbon dioxide emitted during preparation of the contents can be greatly reduced.

As described above, in this embodiment, the first sterilizer 62 sterilizes water with ultraviolet rays. In this case, as shown in FIGS. 3 and 4, the first sterilizer 62 may have a body portion 66 and an ultraviolet irradiation portion 67 provided inside the body portion 66 .

Among them, the body portion 66 is formed in a hollow shape. Moreover, the shape of the main-body part 66 is a truncated cone shape. Specifically, the main body portion 66 has a truncated cone-shaped inner surface, and is oriented so that the end on the small diameter side is positioned higher than the end on the large diameter side. An introduction portion 68 for introducing water into the interior of the body portion 66 is formed in the lower portion of the body portion 66, and a discharge portion 69 for discharging sterilized water from the body portion 66 is formed in the upper portion of the body portion 66. can be An introduction pipe 68a may be connected to the introduction portion 68 formed in the main body portion 66, and the introduction pipe 68a may be provided so as to extend in the tangential direction of the inner surface of the main body portion 66 in plan view. good. In this case, the tangential direction of the inner surface is the tangent line at the portion of the circle formed by the inner surface of the main body 66 in the horizontal cross section including the introduction part 68, where the introduced water collides with the inner surface of the main body 66. is the direction.

The water introduced into the body portion 66 through the introduction portion 68 is guided along the inner surface of the body portion 66 and swirls in the circumferential direction. Then, the water moves upward while swirling and is discharged from the discharge portion 69 . As a result, unevenness in the flow of water introduced into the body portion 66 can be suppressed. Therefore, it is possible to prevent part of the water introduced into the body portion 66 from being discharged from the discharge portion 69 in a short period of time (so-called short pass).

As shown in FIG. 4, a baffle plate 66a may be provided inside the main body 66 to regulate the flow of water. The baffle plate 66a may radially protrude from the inner surface of the body portion 66 so as to spirally go around. By providing such a baffle plate 66a in the body portion 66, it is possible to suppress upward movement of water introduced into the body portion 66 through the introduction portion 68 without turning in the circumferential direction. . Therefore, so-called short pass can be prevented more reliably. Although not shown, the baffle plate 66a does not have to be helically wound inside the main body 66. As shown in FIG. In this case, for example, a plurality of baffle plates 66a each having an annular shape in plan view may be provided in the main body 66, and are configured so that water passes through the central opening. Also good.

A fixing member 66b for fixing a first ultraviolet lamp 67a and a second ultraviolet lamp 67b, which will be described later, of the ultraviolet irradiation portion 67 may be provided in the body portion 66 . The shape of the fixing member 66b may be, for example, a cross shape in plan view. Accordingly, it is possible to prevent the upward movement of water from being hindered by the fixing member 66b. Alternatively, the shape of the fixing member 66b may be, for example, a disc shape, or a circular shape in plan view. In this case, a through hole (not shown) may be formed in the fixing member 66b, and water may pass through the through hole.

Furthermore, an illuminance meter 66 c for measuring the illuminance of the ultraviolet rays emitted from the ultraviolet irradiation section 67 may be installed in the body section 66 . At least one illuminance meter 66 c is preferably installed near the ultraviolet irradiation section 67 . An output meter for measuring outputs of the first ultraviolet lamp 67a and the second ultraviolet lamp 67b, which will be described later, of the ultraviolet irradiation unit 67 may be installed. Further, the flow meter F described above may be used to constantly monitor the time (residence time) for the water to pass through the inside of the body portion 66 . Furthermore, the temperature, transmittance (turbidity) and/or chromaticity of the water passing through the main body 66 may be constantly or appropriately measured to constantly confirm that there is no abnormality in the irradiation amount of ultraviolet rays.

Next, the ultraviolet irradiation section 67 will be described. The ultraviolet irradiation section 67 may include a first ultraviolet lamp 67a provided in the radial center of the body portion 66 and a plurality of second ultraviolet lamps 67b provided around the first ultraviolet lamp 67a. In the illustrated example, four second ultraviolet lamps 67b are provided around one first ultraviolet lamp 67a.

Each second ultraviolet lamp 67 b is arranged along the inner surface of the body portion 66 . That is, each second ultraviolet lamp 67b is provided so as to be inclined radially inward as it goes upward. In this case, the second ultraviolet lamps 67b are preferably arranged at regular intervals along the circumferential direction. Thereby, it is possible to suppress the occurrence of variations in the cumulative irradiation dose (mJ/cm ² ) of ultraviolet rays. Each of the first ultraviolet lamp 67a and the second ultraviolet lamp 67b may be an ultraviolet lamp that emits ultraviolet rays having a wavelength of 200 nm or more and 450 nm or less.

Such first ultraviolet lamp 67a and second ultraviolet lamp 67b may be low-pressure mercury lamps, medium-pressure mercury lamps, or UV-LEDs, respectively. In this case, the first ultraviolet lamp 67a and the second ultraviolet lamp 67b are preferably low-pressure mercury lamps or medium-pressure mercury lamps, respectively.

Moreover, the first ultraviolet lamp 67a and the second ultraviolet lamp 67b may have different wavelengths and/or output powers of irradiated ultraviolet rays. That is, the first ultraviolet lamp 67a and the second ultraviolet lamp 67b may be different ultraviolet lamps. As an example, if the first ultraviolet lamp 67a is a low pressure mercury lamp, the second ultraviolet lamp 67b may be a medium pressure mercury lamp (or UV-LED). Furthermore, the plurality of second ultraviolet lamps 67b may have different wavelengths and/or outputs of ultraviolet rays to be emitted. That is, the plurality of second ultraviolet lamps 67b may be different ultraviolet lamps. For example, if one second ultraviolet lamp 67b is a low-pressure mercury lamp, the other second ultraviolet lamp 67b may be a medium-pressure mercury lamp (or UV-LED). As will be described later, the low-pressure mercury lamp can efficiently irradiate ultraviolet rays with a wavelength (253.7 nm) having a high sterilizing effect. Also, as will be described later, the medium-pressure mercury lamp is a mercury lamp with a higher output than the low-pressure mercury lamp. Therefore, when the first ultraviolet lamp 67a and the second ultraviolet lamp 67b are different ultraviolet lamps, the sterilization effect in the first sterilizer 62 can be improved, and the first sterilizer 62 can sterilize a large amount of water. . Further, as described above, even when the plurality of second ultraviolet lamps 67b are different ultraviolet lamps, the sterilization effect in the first sterilizer 62 can be improved, and the first sterilizer 62 can supply a large amount of water. Can be sterilized.

A low-pressure mercury lamp is a mercury lamp with a mercury vapor pressure of less than 10 Pa during lighting. This low-pressure mercury lamp can efficiently irradiate ultraviolet rays with a wavelength (253.7 nm) having a high sterilizing effect. Therefore, when the first ultraviolet lamp 67a and the second ultraviolet lamp 67b are low-pressure mercury lamps, respectively, the sterilization effect in the first sterilizer 62 (and the second sterilizer 64) can be improved. The low-pressure mercury lamp may be an amalgam lamp (low-pressure high-power amalgam lamp) in which an amalgam, which is an alloy of mercury and other metals, is sealed in the arc tube.

A medium-pressure mercury lamp is a mercury lamp with a mercury vapor pressure of 40 kPa or higher during lighting. The wavelength of ultraviolet rays emitted by a medium-pressure mercury lamp has a dominant wavelength of 365 nm and peaks at 254 nm, 302 nm, 313 nm, 405 nm, 436 nm, and the like. In general, medium pressure mercury lamps are high output mercury lamps compared to low pressure mercury lamps. Therefore, when the first ultraviolet lamp 67a and the second ultraviolet lamp 67b are medium-pressure mercury lamps, the first sterilizer 62 (and the second sterilizer 64) can sterilize a large amount of water. Further, since the medium-pressure mercury lamp is a high-output mercury lamp, when the first ultraviolet lamp 67a and the second ultraviolet lamp 67b are medium-pressure mercury lamps, the first sterilizer 62 (and the second sterilizer 64 ) can be miniaturized.

Further, the ultraviolet irradiation unit 67 of the first sterilizer 62 may be composed only of a low-pressure mercury lamp (including a low-pressure high-output amalgam lamp), and the ultraviolet irradiation unit 67 of the second sterilizer 64 may be composed of a medium-pressure mercury lamp. It may be composed only of Thus, when the water sterilization line 50 has a plurality of sterilizers (for example, the first sterilizer 62 and the second sterilizer 64), the low-pressure mercury lamp (including the low-pressure high-power amalgam lamp) and the medium-pressure mercury lamp It is preferable to use together with a lamp. Low-pressure mercury lamps (including low-pressure high-power amalgam lamps) and medium-pressure mercury lamps have different sterilization wavelengths. Therefore, by using a low-pressure mercury lamp (including a low-pressure high-output amalgam lamp) and a medium-pressure mercury lamp in combination, a high sterilization effect can be obtained.

In addition, since the medium-pressure mercury lamp has higher heat resistance than the low-pressure mercury lamp, it can be lit at high temperatures. Therefore, as will be described later, by circulating hot water or a disinfectant in the circulation system 95A (see FIGS. 2B and 2C), when sterilizing the first sterilizer 62 and the second sterilizer 64, the first The first sterilizer 62 and the like can be sterilized while the ultraviolet lamp 67a and the like are turned on. When a low-pressure mercury lamp (including a low-pressure high-output amalgam lamp) and an ultraviolet lamp that irradiates ultraviolet light with a wavelength different from that of the low-pressure mercury lamp are installed in series, the low-pressure mercury lamp is used in combination with the pure water tank 50c that does not perform sterilization. It may be used in the pre-stage sterilizer 62A between the 1 water tank 51.

Here, the effect of sterilizing bacteria by ultraviolet rays varies depending on the cumulative irradiation dose (mJ/cm ² ) of ultraviolet rays. That is, the greater the cumulative irradiation dose of ultraviolet rays, the higher the bactericidal effect of ultraviolet rays. This cumulative irradiation amount is obtained by multiplying the illuminance (mW/cm ² ) and the irradiation time (s). Therefore, in order to enhance the sterilization effect of ultraviolet rays, it is possible to shorten the distance between the light sources (the first ultraviolet lamp 67a and the second ultraviolet lamp 67b) and the water and lengthen the irradiation time of the ultraviolet rays. Desired. Among other things, the illuminance is inversely proportional to the square of the distance from the light source that emits ultraviolet light. For example, if the distance from the light source is doubled, the illuminance will be 1/4, and if the distance from the light source is tripled, the illuminance will be 1/9. Therefore, by passing water near the light source, the sterilization effect of ultraviolet rays can be enhanced.

As described above, in the present embodiment, the lower portion of the body portion 66 is formed with the introduction portion 68 for introducing water into the interior of the body portion 66, and the upper portion of the body portion 66 is formed with sterilized water. A discharge portion 69 for discharging from is formed. As a result, a short pass can be prevented, and the time during which water stays inside the body portion 66 can be lengthened. For this reason, it is possible to lengthen the irradiation time of the ultraviolet rays to the water and increase the cumulative amount of the ultraviolet rays. Further, by introducing water from the lower part of the main body part 66, even if the water is introduced into the main body part 66 in an empty state, even if the water is introduced into the main body part 66 in an empty state, enough time to stay inside. For this reason, it is possible to lengthen the irradiation time of the ultraviolet rays to the water.

Moreover, the shape of the main-body part 66 is a truncated cone shape. Thereby, in the upper part of the main-body part 66, the distance between the 1st ultraviolet lamp 67a and the 2nd ultraviolet lamp 67b and water can be shortened. Therefore, the effect of sterilizing bacteria by ultraviolet rays can be enhanced. Further, the ultraviolet irradiation section 67 includes a first ultraviolet lamp 67a provided in the radial center of the body portion 66 and a plurality of second ultraviolet lamps 67b provided around the first ultraviolet lamp 67a. This makes it possible to irradiate ultraviolet rays evenly to the water moving upward while turning in the circumferential direction. Therefore, it is possible to suppress the occurrence of variations in the cumulative irradiation amount of ultraviolet rays.

Here, the cumulative irradiation dose of ultraviolet rays to water is preferably 10 mJ/cm ² or more and 10000 mJ/cm ² or less, more preferably 100 mJ/cm ² or more and 10000 mJ/cm ² or less. That is, when passing through the main body portion 66, the cumulative irradiation amount of ultraviolet rays to water is preferably 10 mJ/cm ² or more and 10000 mJ/cm ² or less, and more preferably 100 mJ/cm ² or more and 10000 mJ/cm ² or less. more preferred. Since the cumulative irradiation dose of ultraviolet rays is 10 mJ/cm ² or more, aquatic bacteria (Gram-negative bacteria such as Pseudomonas ) that may pass through the second sterile filter 65 can be effectively sterilized. Moreover, bacterial spores can also be sterilized by setting the cumulative irradiation dose of ultraviolet rays to be 100 mJ/cm ² or more. Further, by setting the cumulative irradiation amount of ultraviolet rays to 10000 mJ/cm ² or less, the amount of electricity consumption can be reduced, and the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Here, the wavelength of the ultraviolet rays may be 250 nm or more and 260 nm or less, and may be 253.7 nm as an example. When the wavelength of the ultraviolet rays is 250 nm or more and 260 nm or less, particularly 253.7 nm, the effect of sterilizing bacteria by ultraviolet rays can be enhanced.

Such a first sterilizer 62 is preferably capable of sterilization (SIP). Thereby, the first sterilizer 62 can be sterilized periodically. When sterilizing the first sterilizer 62, the control section 90 described above may sterilize the first sterilizer 62 with steam or hot water. Alternatively, if the first sterilizer 62 is vulnerable to heat, the control unit 90 circulates a sterilant containing, for example, peracetic acid in the circulation system 59A including the water sterilizer 60, thereby activating the first sterilizer 62. You can sterilize it. In this case, the controller 90 may circulate the disinfectant in the circulation system 59A for at least 10 seconds or more and 60 minutes or less.

In addition, as shown in FIGS. 5A and 5B, the shape of the main body 66 of the first sterilizer 62 may be cylindrical. In this case, a discharge pipe 69a may be connected to the discharge portion 69 formed in the main body portion 66, and the discharge pipe 69a is provided so as to extend in the tangential direction of the inner surface of the main body portion 66 in plan view. It's okay to be there. In this case, the tangential direction of the inner surface refers to the tangential line of the circle formed by the inner surface of the main body 66 in the horizontal cross section including the discharge part 69. tangential to the part. When the body portion 66 has a cylindrical shape, the time for which water stays inside the body portion 66 can be lengthened. For this reason, it is possible to lengthen the irradiation time of the ultraviolet rays to the water and increase the cumulative amount of the ultraviolet rays. In this case, although not shown, the plurality of second ultraviolet lamps 67b may be provided so as to be inclined radially inward as they go upward.

In addition, as shown in FIGS. 6A and 6B, the main body portion 66 has a substantially cylindrical shape, and an introduction portion 68 for introducing water into the main body portion 66 is formed at one end of the main body portion 66. It's okay to be. Also, a discharge portion 69 for discharging sterilized water from the body portion 66 may be formed at the other end portion of the body portion 66 . In this case, the main body portion 66 may be arranged so that the longitudinal direction of the main body portion 66 (the traveling direction of the water) is parallel to the horizontal direction, and the longitudinal direction of the main body portion 66 (the traveling direction of the water) is the vertical direction. The body portion 66 may be arranged so as to be parallel to the . In the illustrated example, the main body portion 66 has a so-called reducer shape in which the diameter decreases toward one end and decreases toward the other end. However, the shape of the body portion 66 is not limited to this, and may be a cylindrical shape having a substantially uniform diameter from the introduction portion 68 to the discharge portion 69 .

In this modified example, the ultraviolet irradiation section 67 may include a plurality of third ultraviolet lamps 67c arranged along the traveling direction of water. This makes it possible to evenly irradiate water with UV rays. Therefore, it is possible to suppress the occurrence of variations in the cumulative irradiation amount of ultraviolet rays. In the illustrated example, the ultraviolet irradiation section 67 includes eight third ultraviolet lamps 67c.

Also, the third ultraviolet lamps 67c that are adjacent to each other in the water traveling direction may extend in different directions when viewed from the water traveling direction. As a result, it is possible to more effectively suppress variations in the cumulative irradiation amount of ultraviolet rays. In the illustrated example, each third ultraviolet lamp 67c is regularly arranged. That is, when viewed from the upstream side (left side in FIG. 6B) in the traveling direction of water, each of the third ultraviolet lamps 67c moves toward the downstream side in the traveling direction of water (right side in FIG. 6B). It rotates clockwise about the central axis X by 45 degrees. Note that the rotation angle of each third ultraviolet lamp 67c may be changed as appropriate. For example, when viewed from the upstream side in the water traveling direction, each third ultraviolet lamp 67c rotates clockwise by 90° around the central axis X toward the downstream side in the water traveling direction. can be Further, when the ultraviolet irradiation section 67 includes three or more third ultraviolet lamps 67c, each of the third ultraviolet lamps 67c is located on the downstream side in the traveling direction of the water when viewed from the upstream side in the traveling direction of the water. It may be rotated clockwise by 60° around the central axis X as it goes toward In addition, each 3rd ultraviolet lamp 67c may be arranged irregularly.

The third ultraviolet lamp 67c may be an ultraviolet lamp similar to the first ultraviolet lamp 67a and the second ultraviolet lamp 67b. That is, the third ultraviolet lamp 67c may be an ultraviolet lamp that emits ultraviolet rays having a wavelength of 200 nm or more and 450 nm or less. Also, the third ultraviolet lamp 67c may be a low-pressure mercury lamp (including a low-pressure high-power amalgam lamp), a medium-pressure mercury lamp, or a UV-LED. Further, the plurality of third ultraviolet lamps 67c may have different wavelengths and/or outputs of ultraviolet rays to be irradiated. That is, the plurality of third ultraviolet lamps 67c may be different ultraviolet lamps. For example, if one third ultraviolet lamp 67c is a low-pressure mercury lamp, the other third ultraviolet lamp 67c may be a medium-pressure mercury lamp (or UV-LED). In this case as well, the sterilization effect of the first sterilizer 62 can be improved, and a large amount of water can be sterilized by the first sterilizer 62 . Although not shown, a baffle plate 66a may be provided inside the main body 66 to regulate the flow of water.

Referring again to FIG. 2A, the first sterile filter 63 is provided downstream of the first sterilizer 62 . This first sterile filter 63 is a filter that sterilizes water by collecting bacteria remaining in the water. The mesh size of the first sterile filter 63 may be 0.1 μm or more and 0.45 μm or less, preferably 0.1 μm or more and 0.22 μm or less. Since the opening of the first sterile filter 63 is 0.1 μm or more, it is possible to suppress a decrease in water sterilization efficiency. Moreover, since the mesh size of the first sterile filter 63 is 0.45 μm or less, bacteria remaining in the water can be effectively collected by the first sterile filter 63 .

This first sterile filter 63 is preferably sterilizable (SIP) capable. Thereby, the first sterile filter 63 can be sterilized periodically. Here, as described above, the first sterile filter 63 passes through the first sterilizer 62 and collects bacteria remaining in the water. Therefore, if water sterilization is continued in the water sterilizer 60 for a long period of time, the trapped bacteria may grow inside the first sterile filter 63 . In addition, when the corpses of bacteria, which are organic matter, adhere to the first sterile filter 63 or the like, the corpses of bacteria can become the substrate. In this case, germs can grow further inside the first sterile filter 63 . In this way, if it breeds within the first sterile filter 63 , it may enter the water passing through the first sterile filter 63 . On the other hand, since the first sterile filter 63 can be sterilized, bacteria adhering to the first sterile filter 63 can be prevented from entering water passing through the first sterile filter 63 . As a result, deterioration of the filtering performance of the first sterile filter 63 can be suppressed. When sterilizing the first sterile filter 63, sterilizing steam or the like may be supplied to the first sterile filter 63 from a sterile air supply port 60a, which will be described later.

Here, the degree of sterilization of the first sterile filter 63 may be managed by the F value. In other words, when the water sterilizer 60 having the first sterile filter 63 is sterilized, the degree of sterilization of the water sterilizer 60 may be controlled by the F value. At this time, for example, the control unit 90 measures the temperature of the heated steam (fluid) or hot water (fluid) flowing through the flow path of the first sterile filter 63, and determines the F value based on the measured temperature. You can calculate. Then, the control unit 90 may terminate the sterilization of the first sterile filter 63 when the F value becomes equal to or greater than the target value. When measuring the temperature of heated steam or hot water, the control unit 90 is arranged at various locations in the flow path where the temperature does not easily rise while flowing the heated steam or hot water in the flow path of the first sterile filter 63. A temperature sensor may be used to measure the temperature. Then, the control unit 90 may terminate the heating of the flow path by the heating steam or the like when the temperature from each temperature sensor reaches a predetermined temperature for a predetermined time or longer. As a result, the first sterile filter 63 can be sterilized without applying excessive heat to the first sterile filter 63 . Here, the F value is the heating time required to kill all the bacteria when the bacteria are heated for a certain period of time. .

（ただし、Ｔは任意の殺菌温度（℃）、１０＾｛（Ｔ－Ｔｒ）／Ｚ｝は任意の殺菌温度Ｔでの致死率、Ｔｒは基準温度（℃）、ＺはＺ値（℃）を表す。）

(However, T is an arbitrary sterilization temperature (° C.), 10^{(T−Tr)/Z} is the lethality rate at an arbitrary sterilization temperature T, Tr is the reference temperature (° C.), Z is the Z value (° C.) represents.)

In addition, it is preferable that the first sterile filter 63 be able to perform an integrity test on the opening of the first sterile filter 63 . Here, the integrity test can be performed as follows. For example, first, by supplying water to a housing (not shown) in the first sterile filter 63, the filter (not shown) of the first sterile filter 63 is covered with water. Next, the water supply is stopped and the water in the first sterile filter 63 is discharged. Then, sterile air is injected from, for example, the sterile air supply port 60a into the first sterile filter 63 whose filter is covered with water. Next, the pressure of sterile air is increased until the sterile air escapes from the first sterile filter 63 . Then, based on the pressure of sterile air when the sterile air escapes from the first sterile filter 63, the size of the opening of the first sterile filter 63 is determined. Since the first sterile filter 63 can perform an integrity test on the opening of the first sterile filter 63 in this manner, the degree of deterioration of the first sterile filter 63 can be easily determined. In order to measure the pressure inside the first sterile filter 63, a pressure gauge P2 may be provided near the sterile air supply port 60a.

The second sterilizer 64 is provided downstream of the first sterile filter 63 . The configuration of the second sterilizer 64 may be substantially the same as that of the first sterilizer 62 shown in FIGS. 3 to 6B. That is, the second sterilizer 64 may be a sterilizer that sterilizes water with ultraviolet light.

The second sterile filter 65 is provided downstream of the second sterilizer 64 . This second aseptic filter 65 is a filter that sterilizes water by passing through the second sterilizer 64 and collecting bacteria remaining in the water. The mesh size of the second sterile filter 65 is preferably less than or equal to the mesh size of the first sterile filter 63 . As a result, even if bacteria in the water pass through the first sterile filter 63 , the bacteria can be captured by the second sterile filter 65 . Therefore, the sterility of water can be sufficiently ensured. Further, when the mesh size of the second sterile filter 65 is the same as the mesh size of the first sterile filter 63, two sets of sterilization sets composed of a sterilizer and a sterile filter are arranged along the water conveying direction. can be placed. That is, a first sterilization set composed of the first sterilizer 62 and the first aseptic filter 63 and a second sterilization set composed of the second sterilizer 64 and the second aseptic filter 65 are combined with water. can be arranged in series along the conveying direction of the Therefore, even if one of the sterilization sets has some kind of abnormality, the sterility of the water can be guaranteed. A plurality of sterilization sets may be provided according to the sterility assurance level (SAL (Sterility Assurance Level)) of the water or the final product (contents) (see FIGS. 2A to 2E). Also, as shown in FIG. 2F, the number of sterilization sets may be one.

The mesh size of the second sterile filter 65 may be 0.1 μm or more and 0.45 μm or less, preferably 0.1 μm or more and 0.22 μm or less. Since the mesh size of the second sterile filter 65 is 0.1 μm or more, a decrease in water sterilization efficiency can be suppressed. Further, since the mesh size of the second sterile filter 65 is 0.45 μm or less, bacteria remaining in the water can be more effectively collected by the second sterile filter 65 .

Other configurations of the second sterile filter 65 may be substantially the same as those of the first sterile filter 63 . That is, the second sterile filter 65 may be sterilizable (SIP) capable. Also, the second sterile filter 65 may be capable of performing an integrity test on the opening of the second sterile filter 65 .

Here, in the water sterilizer 60, the water sterilization strength may be adjusted based on the target value of the bacteria count level (FSO (Food Safety Objective/ISO13409-1996) (=log N)).

In this case, for example, let H ₀ (=logN ₀ ) be the initial bacterial count level in the water before entering the filter (for example, the first sterile filter 63). In this case, the initial bacteria count level H ₀ of the filter is the sterilization effect of the filter (for example, the first sterile filter 63) (bacteria reduction level in water: ΣR ₁ (=log(N ₀ /NR ₁ )>0 ), where “N ₀ ” means the initial number of germs in the water, and “NR ₁ ” means the number of germs in the water after being sterilized by a filter (for example, the first sterile filter 63). means number.

On the other hand, it is conceivable that bacteria in the water may increase at a certain rate while passing through the filter (increased number of bacteria in water: ΣI (=log(N _I )≧0)). “N _I ” means the number of bacteria increased while passing through the filter.

In addition, the bacteria in the water are reduced again by the sterilization effect of the sterilizer (for example, the second sterilizer 64) (the level of bacteria reduction in the water: ΣR ₂ (=log (N _I /NR ₂ )>0)). do. If the bacteria count level in the water after passing through the water sterilizer 60 is below the target value (FSO (Food Safety Objective/ISO13409-1996) (=log N)), the water sterilized by the water sterilization line 50 is sterilized. You can think that sex is not a problem. In addition, "NR ₂ " means the number of bacteria in the water after being sterilized by the sterilizer (e.g., the second sterilizer 64), and "N" is the sterilizer (e.g., the second sterilizer 64). means the target number of bacteria in water after being sterilized by

The relationships among H ₀ , ΣR ₁ , ΣI, ΣR ₂ and FSO described above are expressed as formulas as follows.
H ₀ −ΣR ₁ +ΣI−ΣR ₂ ≦FSO (Formula 1)
Therefore, by setting the sterilization capacity of the sterilizer (for example, the second sterilizer 64) so that the value of ΣR ₂ is (H ₀ - ΣR ₁ + ΣI) - FSO or more, the sterilization of water is targeted. value (FSO) or less.

In addition, as shown in FIGS. 2A to 2F, the inlet of the water sterilizer 60, the outlet of the water sterilizer 60, the space between the foreign substance removal filter 61 and the first sterilizer 62, etc. are sterilely filled with water. Sampling points SP1 to SP6 (SP) may be provided for sampling. A sampling line SL may be connected to at least some of the sampling points SP1 to SP6 via valves (not shown). As a result, by aseptically sampling water from the sampling points SP1 to SP6 or the sampling line SL, the number of bacteria or fine particles in the water can be easily measured, and changes in the state of the water such as the propagation of bacteria can be easily detected. can be confirmed. When measuring the number of bacteria in water and/or when confirming a change in state such as breeding of bacteria, for example, the number of bacteria may be counted using a plate medium. Further, for example, the number of bacteria in water and/or changes in the state of bacteria may be measured and/or confirmed using a microbe measuring instrument or a particle measuring instrument (liquid particle counter) or the like. Here, the microbial measuring instrument is a measuring instrument that counts microorganisms by detecting fluorescence emitted when particles are irradiated with a laser beam and distinguishing between non-living organisms and microorganisms based on the MIE scattering theory. Examples of such a microbial measuring instrument include: Biological particle counter manufactured by Rion Co., Ltd., Microbial Detection Analyzer 7000RMS manufactured by Mettler Toledo Co., Ltd., Real-time Microbial Detector manufactured by Azbil Corporation, IMD-W (registered trademark), etc. are mentioned. In addition, when aseptically sampling water from the sampling line SL, the sampling line SL is preferably sterilized in advance. In this case, for example, the sampling line SL may be sterilized with a sterilizing agent such as peracetic acid or hot water. Also, the sampling line SL sterilized with a sterilant may be rinsed with pure water sterilized by the first sterile filter 63 and the second sterile filter 65 .

A thermometer T may be provided in the sampling line SL, and the temperature of the steam is monitored by the thermometer T when the first sterile filter 63 and the second sterile filter 65 are sterilized with steam. Also good.

A third bypass line 95a may be provided between the pre-sterilizer 62A and the first sterilizer 62, as shown in FIGS. 2B and 2C. Thereby, when the water sterilization line 50 is sterilized with a sterilizing agent or a cleaning agent, it is possible to prevent the sterilizing agent or the cleaning agent from passing through the foreign matter removing filter 61 . A first drain pipe 95c may be connected to the upstream side of the foreign matter removing filter 61, and rinsing water or the like, which will be described later, may be discharged from the first drain pipe 95c. Note that the first drain pipe 95c may be connected to the third bypass line 95a.

Furthermore, a fourth bypass line 95b may be provided between the first sterilizer 62 and the second sterilizer 64, as shown in FIG. 2B. Thereby, when the water sterilization line 50 is sterilized with a sterilizing agent or a cleaning agent, it is possible to prevent the sterilizing agent or the cleaning agent from passing through the first sterile filter 63 . Further, as shown in FIGS. 2B and 2C, a second drain pipe 95d may be connected to the upstream side of the first sterile filter 63, and rinsing water or the like, which will be described later, is discharged from the second drain pipe 95d. May be. The second drain pipe 95d may be connected to the fourth bypass line 95b.

The processing capacity of such a water sterilizer 60 is preferably 105% or more of the maximum processing capacity required during production of the product bottles 101, and 110% of the maximum processing capacity required during production of the product bottles 101. % or more is more preferable. For example, the processing capacity of the water sterilizer 60 may be 5 m ³ /h or more and 50 m ³ /h or less, and may be 24 m ³ /h as an example. Further, if the processing capacity of the water sterilizer 60 is 105% or more of the maximum processing capacity required during production of the product bottles 101, a predetermined amount of Water can also be stored. In this case, by appropriately designing the volume of the second water tank 52, the product bottle 101 can be supplied without running out of water even during the sterilization (SIP) or integrity test of the above-described first sterile filter 63 or the like. and sterilization (SIP) or integrity testing of the first sterile filter 63 and the like. The time required for the sterilization (SIP) of the first sterile filter 63 and the like and the time required for the integrity test are approximately 30 minutes or more and approximately 1 hour or less, respectively. Therefore, the volume of the second water tank 52 may be greater than or equal to the amount of water used in the content filling system 10 when the product bottle 101 is produced for one hour.

Also, the processing capacity of the water sterilizer 60 may be controlled by the controller 90 . For example, the control unit 90 determines the amount of water to be used for cleaning and sterilizing the contents filling system 10, and based on the determined amount of water, the water sterilizer 60 in the water sterilization line 50 is used to produce the product. The amount of water to be sterilized during production of bottle 101 may be determined. Here, the amount of sterilized water required for cleaning and/or sterilizing the inside of each chamber or the like after production of the product bottle 101 can be grasped for each chamber or the like. Therefore, the processing capacity of the water sterilizer 60 may be controlled by the control unit 90 so that sterile water to be used after the production of the product bottles 101 is stored while one lot of the product bottles 101 is produced. As a result, the inside of each chamber or the like can be cleaned and/or sterilized immediately after the product bottle 101 is produced. Therefore, downtime can be shortened.

Further, the control unit 90 may discharge water to the outside of the water sterilization line 50 when the irradiation amount or illuminance of the ultraviolet rays is equal to or less than a predetermined value. Here, the predetermined value is a reference value (threshold value) for determining whether or not water should be discharged to the outside of the water sterilization line 50 . Such a predetermined value can be arbitrarily set according to the volume of the body portion 66, the flow rate of water, or the like. For example, the predetermined value may be the dose or intensity of illumination that ensures that the sterility assurance level of the water or final product (contents) is not exceeded. The predetermined value may be 10 mJ/cm ^{2 or more and 10000 mJ/cm 2 or less, and may be 100 mJ/cm 2 as} an example, although it depends on the volume of the main body 66 and the like. The irradiation dose of ultraviolet rays irradiated by the ultraviolet irradiation unit 67 may be set based on RED (Reduction Equivalent UV Dose) obtained by an actual chemical dosimeter or biological dosimeter. For more information, see ULTRAVIOLET DISINFECTION GUIDANCE MANUAL FOR THE FINAL LONG TERM 2 ENHANCED SURFACE WATER TREATMENT RULE, United States Environmental Protection Agency, EPA 815-R-06-007, November 2006.

When the controller 90 discharges water to the outside of the water sterilization line 50 , the controller 90 may discharge water to the outside of the water sterilization line 50 via the circulation line 59 . In this case, the control unit 90 may switch the valve V1 when the value of the illuminance meter 66c becomes equal to or less than a predetermined value while the water sterilizer 60 is sterilizing water with ultraviolet rays. Water may be supplied to the circulation line 59 by the controller 90 switching the valve V1. As a result, sterility can be maintained downstream of the valve V1. The water supplied to the circulation line 59 may be discharged from the circulation line 59 without being supplied to the first water tank 51 . Alternatively, the water supplied to the circulation line 59 may be supplied to the first water tank 51 . In this case, water may be circulated in the circulation system 59A until the value of the illuminance meter 66c becomes a sufficient value. Water in the circulation system 59A may be supplied to the second water tank 52 by the controller 90 switching the valve V1 after the value of the illuminance meter 66c reaches a sufficient value.

In addition, the control unit 90 determines that the pressure difference (differential pressure) between the pressure on the upstream side and the pressure on the downstream side of the sterile filter (the first sterile filter 63 or the second sterile filter 65) becomes equal to or greater than a predetermined value. In some cases, the water may be discharged outside the water sterilization line 50 . That is, even when an abnormality is recognized in the pressure difference (differential pressure) between the pressure on the upstream side and the pressure on the downstream side of the first sterile filter 63 (or the second sterile filter 65), the control unit 90 Similarly, water may be discharged outside the water disinfection line 50 . Even in this case, for example, the sterility of the downstream side of the valve V1 can be maintained.

Furthermore, the control unit 90 may discharge water to the outside of the water sterilization line 50 when at least one of the number of bacteria and fine particles in the water sampled from the water sterilization line 50 reaches or exceeds a predetermined value. . That is, the control unit 90 may similarly discharge water to the outside of the water sterilization line 50 even when there is an abnormality in the number of bacteria and/or fine particles in the water sampled from the sampling line SL. Even in this case, for example, the sterility of the downstream side of the valve V1 can be maintained.

In these cases, after the problem of the water sterilizer 60 is resolved, the water sterilizer 60 is sterilized with a sterilizing agent such as peracetic acid, hot water, or steam, as will be described later. Thereafter, water sterilization by the water sterilizer 60 is resumed.

Such a water sterilizer 60 continues to sterilize water without stopping water sterilization while producing product bottles 101 by filling the contents into the bottles 100 in the contents filling system 10. is preferred. Accordingly, it is possible to suppress the propagation of bacteria inside the first sterile filter 63 and the second sterile filter 65 . That is, when the water flow is stopped in the water sterilizer 60 , bacteria may grow inside the first sterile filter 63 and the second sterile filter 65 . On the other hand, by continuing to sterilize the water without stopping the pump P1 while the product bottle 101 is being produced in the contents filling system 10, the water inside the first sterile filter 63 and the second sterile filter 65 can prevent the spread of bacteria. If the second water tank 52 becomes full while the product bottle 101 is being produced in the contents filling system 10, sterilized water is circulated in the circulation system 59A (see FIG. 2A, etc.). You can let me. As a result, even when the second water tank 52 is full, it is possible to prevent the flow of water from stopping in the water sterilizer 60 . Therefore, it is possible to suppress the propagation of bacteria in the first sterile filter 63 and the second sterile filter 65 . Note that when the circulation time of the sterilized water is long, the temperature of the sterilized water may rise due to the irradiation energy of the ultraviolet rays emitted from the ultraviolet irradiation section 67 . In this case, the water flowing through the circulation line 59 may be discharged from the circulation line 59 without being supplied to the first water tank 51 . Then, by supplying new pure water from the pure water production device 50a to the first water tank 51, the temperature rise of the circulating water may be suppressed. For example, when sterilized water is circulated in the circulation system 59A, about 3% or more and 30% or less of the water remaining inside the circulation line 59 is discharged once an hour, and the pure water production device 50a Alternatively, fresh pure water may be supplied from the first water tank 51 to the first water tank 51 . This makes it possible to always supply water of a constant temperature to the second water tank 52 . The proportion of water to be discharged may be appropriately changed depending on the irradiation dose or the number of the first ultraviolet lamps 67a and the like.

Next, the undiluted solution sterilization line 70 will be described. The concentrate sterilization line 70 is a sterilization line for heat sterilizing the product concentrate.

As shown in FIG. 7 , the concentrate sterilization line 70 has a first concentrate tank 71 , a product concentrate sterilizer 80 , and a second concentrate tank 72 . The first undiluted solution tank 71, the product undiluted solution sterilizer 80, and the second undiluted solution tank 72 are arranged in this order from the upstream side toward the downstream side along the conveying direction of the undiluted product solution. A circulation line (third circulation line) 89 may be connected to the concentrate sterilization line 70 between a third stage cooling section 86 and a second concentrate tank 72, which will be described later. The product concentrate that has passed through the third stage cooling section 86 may be configured to be returned to the first concentrate tank 71 via the circulation line 89 .

The first undiluted solution tank 71 is a tank that stores a product undiluted solution supplied from a supply source (not shown). This first liquid concentrate tank 71 stores the product liquid concentrate, thereby playing a role of facilitating the flow of the product liquid concentrate. The volume of the first concentrate tank 71 may be 0.3 m ³ or more and 3 m ³ or less, and may be 1 m ³ as an example.

A pump P3 for conveying the product concentrate may be provided downstream of the first concentrate tank 71 . Further, the product concentrate sterilizer 80 described above is provided on the downstream side of the pump P3.

The product concentrate sterilizer 80 is a sterilizer that thermally sterilizes the product concentrate stored in the first concentrate tank 71 . In the present embodiment, the product concentrate sterilizer 80 may be a sterilizer (Ultra High-temperature, hereinafter simply referred to as UHT) that sterilizes the product concentrate by an ultra-high temperature heat treatment method. The UHT 80 has a first stage heating section 81, a second stage heating section 82, a holding tube 83, a first stage cooling section 84, a second stage cooling section 85, and a third stage cooling section 86. ing. The product concentrate supplied to the UHT 80 is gradually heated by the first stage heating section 81 and the second stage heating section 82 and heated to the target temperature within the holding tube 83 . In this case, for example, the product concentrate may be heated to 60° C. or higher and 80° C. or lower by the first stage heating section 81 and heated to 80° C. or higher and 150° C. or lower by the second stage heating section 82 . In addition, the temperature of the undiluted product solution is maintained within the holding tube 83 for a certain period of time. The product concentrate that has passed through the holding tube 83 is gradually cooled by the first stage cooling section 84 , the second stage cooling section 85 and the third stage cooling section 86 . Note that the number of stages of the heating section and the cooling section may be increased or decreased as necessary. In addition, the pressure loss of the product stock solution may increase between the first stage heating section 81 and the second stage heating section 82 . Therefore, an additional pump (not shown) may be provided between the first stage heating section 81 and the second stage heating section 82 . Further, a homogenizer for homogenizing the product stock solution is provided between the first-stage heating section 81 and the second-stage heating section 82, or between the first-stage cooling section 84 and the second-stage cooling section 85. It's okay to be

The throughput of such UHT 80 may be 3 m ³ /h or more and 30 m ³ /h or less, and may be 6 m ³ /h as an example.

Also, by monitoring the temperature of a portion of the UHT 80 where the temperature is the highest (for example, the second-stage heating section 82), scale (deposits such as calcium) adhering to the UHT 80 may be monitored. Then, when cleaning (CIP) the UHT 80, the scale removal state may be monitored. As a result, the cleaning process for cleaning the UHT 80 can be optimized. Therefore, the cleaning time can be shortened, and the amount of water, steam, and cleaning agent used for cleaning can be reduced. As a result, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Note that the UHT 80 may be of the injection type or the infusion type. The heat exchanger used for heat exchange in the filling system 10, such as the UHT 80 heat exchanger, may be a plate type, shell and tube type, or scraped heat exchanger.

The second undiluted solution tank 72 is a tank (so-called aseptic tank) that stores the undiluted product sterilized by the undiluted product sterilizer 80 . The second liquid concentrate tank 72 stores the sterilized liquid concentrate, thereby facilitating the flow of the liquid concentrate. The volume of the second concentrate tank 72 may be 1 m ³ or more and 20 m ³ or less, and may be 2 m ³ as an example.

Further, an auxiliary filter 73 for filtering the sterilized product concentrate and a third concentrate tank 74 for storing the product concentrate that has passed through the auxiliary filter 73 may be provided downstream of the second concentrate tank 72. In this case, the third concentrate tank 74 may be a so-called filling machine tank, and may be installed vertically above the concentrate filling device 22 in order to improve the filling accuracy of the concentrate filling device 22 . The third concentrate tank 74 may serve as a so-called cushion tank that ensures smooth flow of the product concentrate even when the amount of product concentrate used on the downstream side of the third concentrate tank 74 changes. . The volume of the third concentrate tank 74 may be 0.1 m ³ or more and 1 m ³ or less, and may be 0.3 m ³ as an example. Incidentally, the auxiliary filter 73 may be provided inside or at the tip of all the concentrate filling nozzles of the concentrate filling device 22 (for example, see FIG. 16C described later).

Furthermore, an addition unit 75 for adding solid matter to the product concentrate may be connected to the downstream side of the second concentrate tank 72 . As a result, the content filling system 10 can fill the bottle 100 with the solid content. In this case, the solid matter added by the addition unit 75 to the product stock solution may be, for example, sandalwood, nata de coco, tapioca, aloe, or the like. Alternatively, the solid may be a pre-sterilized aseptic solid.

(Content filling method)
Next, FIG. 8 demonstrates the content filling method using the content filling system 10 (FIG. 1) mentioned above.

First, the preform supply device 1 sequentially supplies a plurality of preforms 100a to the receiving section 34 of the preform transport section 31 via the preform supply conveyor 2 (preform supply step, symbol S1 in FIG. 8). ). At this time, the preform 100a is sterilized by spraying hydrogen peroxide gas or mist onto the preform 100a in the preform sterilizer 34a, and then dried with hot air.

Next, the preform 100a is sent to the heating unit 35 and heated to, for example, about 90° C. or higher and 130° C. or lower by the heater 35a. Then, the preform 100a heated by the heating section 35 is sent to the delivery section 36. As shown in FIG. Then, the preform 100 a is sent from the delivery section 36 to the blow molding section 32 .

Next, the preform 100a sent to the blow molding section 32 is subjected to blow molding using a mold (not shown), thereby blow molding the bottle 100 (bottle molding step, symbol S2 in FIG. 8). Then, the blow-molded bottle 100 is sent to the bottle conveying section 33 .

Next, in the sterilization device 11, the bottle 100 is sterilized using an aqueous hydrogen peroxide solution as a sterilant (container sterilization step, symbol S3 in FIG. 8). At this time, the sterilizing agent may be gas or mist obtained by once vaporizing an aqueous hydrogen peroxide solution at a boiling point or higher. The gas or mist of the aqueous hydrogen peroxide solution adheres to the inner and outer surfaces of the bottle 100 and sterilizes the inner and outer surfaces of the bottle 100 .

The bottle 100 is then sent to the air rinse device 14 . In the air rinsing device 14, aseptic heated air or normal temperature air is supplied to the bottle 100 to activate the hydrogen peroxide and remove foreign matter, hydrogen peroxide, etc. from the bottle 100 ( Air rinse step, symbol S4 in FIG. 8). In the air rinsing step, the sterilized heated air or room-temperature sterilized air may be mixed with a low-concentration condensed mist of hydrogen peroxide, if necessary. In this case hydrogen peroxide is gasified by sterile air. Then, gasified hydrogen peroxide may be supplied to the bottle 100 in the air rinse step.

Bottle 100 is then transported to filling device 20 . At this time, water is first filled into the bottle 100 in the water filling device 21 of the filling device 20 (water filling step, symbol S5 in FIG. 8). In the water filling device 21, water is filled into the bottle 100 from the mouth thereof while the bottle 100 is rotated (revolved). The water is previously sterilized in the water sterilization line 50 before being filled into the bottle 100 by the water filling device 21 .

In the water filling device 21, the sterilized bottle 100 is filled with sterilized water at room temperature. The temperature of water at the time of filling is, for example, about 3° C. or higher and 40° C. or lower. Further, the filling speed at which the water filling device 21 fills the bottle 100 with water may be faster than the filling speed at which the concentrate filling device 22 fills the bottle 100 with the product concentrate. In the water filling device 21, the water filling speed may be 100 mL/sec or more and 500 mL/sec or less.

Next, in the undiluted solution filling device 22 of the filling device 20, the product undiluted solution is filled into the bottle 100 filled with water (product undiluted solution filling step, symbol S6 in FIG. 8). In the concentrate filling device 22, the product concentrate is filled into the bottle 100 through its mouth while the bottle 100 is being rotated (revolved). The product concentrate is heat-sterilized in the concentrate sterilization line 70 in advance before being filled into the bottle 100 by the concentrate filling device 22 . The heating temperature for heating the product stock solution may generally be about 60° C. or more and 120° C. or less when the acidity of the content is less than pH 4.5, and the heating time is about 30 seconds or more and 120 seconds or less. It can be. Moreover, when the acidity of the content is pH 4.5 or higher, the heating temperature for heating the product stock solution may be about 115° C. or higher and 150° C. or lower. Also, the heating time may be about 30 seconds or more and 120 seconds or less. As a result, among the microorganisms in the undiluted product liquid before filling, all microorganisms that can grow in the product bottle 101 are sterilized. The heat-sterilized product stock solution is cooled to a temperature of about 3°C or higher and 40°C or lower.

In the concentrate filling device 22, the bottle 100 filled with water is filled with the product concentrate that has been sterilized and cooled to room temperature at room temperature. The temperature of the product stock solution at the time of filling is, for example, about 3° C. or higher and 40° C. or lower. In the undiluted solution filling device 22, the undiluted product filling speed may be 30 mL/sec or more and 200 mL/sec or less.

Subsequently, the bottle 100 filled with contents is transported to the capping device 16 by the transport wheel 12 .

On the other hand, the cap 88 is previously sterilized by the cap sterilizer 18 (cap sterilization step, symbol S7 in FIG. 8). During this time, the cap 88 is first carried into the cap sterilizer 18 from the outside of the contents filling system 10 . Subsequently, the cap 88 is sprayed with hydrogen peroxide gas or mist in the cap sterilizer 18 to sterilize its inner and outer surfaces, dried with hot air, and sent to the cap attaching device 16 .

Next, in the cap attaching device 16, a sterilized cap 88 is attached to the mouth of the bottle 100 conveyed from the filling device 20, so that the bottle 100 is closed and the product bottle 101 is obtained (cap attaching step, FIG. 8 sign S8).

After that, the product bottle 101 is conveyed from the cap attaching device 16 to the product bottle unloading section 25, and unloaded toward the outside of the content filling system 10 (bottle ejection step, symbol S9 in FIG. 8). The product bottle 101 is then transported to a packaging line (not shown) and packaged.

The container sterilization process, the air rinse process, the water filling process, the product concentrate filling process, the cap attaching process, and the bottle discharging process include the disinfectant spraying chamber 70d, the air rinse chamber 70e, the first aseptic chamber 70f, the intermediate area chamber 70g, It takes place in a sterile atmosphere, ie in a sterile environment, enclosed by the second sterile chamber 70h and the exit chamber 70i. Also, the cap sterilization step is performed by the cap sterilizer 18 . In this case, the sterilant spray chamber 70d, the air rinse chamber 70e, the first aseptic chamber 70f, the intermediate area chamber 70g, the second aseptic chamber 70h, the exit chamber 70i and the cap sterilizer 18 are previously sprayed with hydrogen peroxide or peracetic acid. or sterilized by spraying hot water or the like.

After the sterilization of each chamber, the sterile air is always directed outside the sterilant spray chamber 70d, the air rinse chamber 70e, the first sterile chamber 70f, the intermediate area chamber 70g, the second sterile chamber 70h, and the exit chamber 70i. Positive pressure sterile air is supplied into the sterilant spray chamber 70d, the air rinse chamber 70e, the first sterile chamber 70f, the intermediate area chamber 70g, the second sterile chamber 70h and the exit chamber 70i. In addition, positive pressure aseptic air is supplied into the cap sterilizer 18 so that the aseptic air is always blown out of the cap sterilizer 18 .

Thus, when positive pressure sterile air is supplied in each chamber 70d-70i, the atmosphere isolation chamber 70c, the sterilant spray chamber 70d and the exit chamber 70i use sterile air in each chamber and bottle sterilization. Vent the sterilant used. At that time, the pressure in each chamber is adjusted so that the pressure in each of the sterilant spray chamber 70d, the air rinse chamber 70e, the first sterile chamber 70f, the intermediate area chamber 70g, the second sterile chamber 70h, and the outlet chamber 70i becomes a positive pressure. Pressure may be regulated. In this case, as described above, the pressure in the sterilant spray chamber 70d may be -10 Pa or more and 10 Pa or less. The pressure in the air rinse chamber 70e may be 10 Pa or more and 30 Pa or less. The pressure inside the first sterile chamber 70f may be 30 Pa or more and 60 Pa or less. The pressure in the intermediate area chamber 70g may be 20 Pa or more and 50 Pa or less. The pressure inside the second aseptic chamber 70h may be 10 Pa or more and 40 Pa or less. The pressure in the exit chamber 70i may be 10 Pa or more and 20 Pa or less.

The production (conveyance) speed of the bottles 100 in the contents filling system 10 is preferably 100 bpm or more and 1500 bpm or less. Here, bpm (bottle per minute) refers to the transport speed of the bottle 100 per minute.

(Method for sterilizing content filling system)
Next, a sterilization method for the content filling system 10 (FIG. 1) described above will be described. Here, first, the method of sterilizing the first aseptic chamber 70f, the intermediate area chamber 70g and the second aseptic chamber 70h (hereinafter simply referred to as the chamber sterilization method) will be described with reference to FIG.

Chamber Sterilization Method First, after the filling of the beverage in the content filling system 10 is completed, for example, the operation button of the control section 90 is operated. As a result, the water filling nozzle of the water filling device 21 is covered with a CIP cup (not shown). By covering the water filling nozzle of the water filling device 21 with a CIP cup (not shown) in this way, the inside of the water filling device 21 is kept sterile. That is, the water filling device 21 is physically protected so that bacteria do not enter the water filling device 21 from the tip of the water filling nozzle. In addition, by operating the operation button of the control unit 90, partitions are formed to separate the disinfectant spray chamber 70d, the air rinse chamber 70e, the first aseptic chamber 70f, the intermediate area chamber 70g, and the second aseptic chamber 70h, respectively. The gap is closed by a shutter (not shown).

Next, the pressure in the first sterile chamber 70f is increased. At this time, aseptic air is supplied from an aseptic air supply device (not shown) into the first aseptic chamber 70f, the pressure in the first aseptic chamber 70f rises. Also, at this time, the air supply amount and/or exhaust amount in each chamber is adjusted so that the pressure in the first aseptic chamber 70f becomes a predetermined pressure. At this time, the pressure in the first aseptic chamber 70f, which was 30 Pa, for example, is increased to 40 Pa, for example. This prevents air in the sterilant spray chamber 70d and air in the intermediate area chamber 70g from entering the first sterile chamber 70f.

In this case, as described above, the pressure in the sterilant spray chamber 70d may be 0 Pa or more and 20 Pa or less. The pressure in the air rinse chamber 70e may be 10 Pa or more and 40 Pa or less. The pressure inside the first sterile chamber 70f may be 40 Pa or more and 100 Pa or less. The pressure in the intermediate area chamber 70g may be 10 Pa or more and 40 Pa or less. The pressure inside the second aseptic chamber 70h may be 0 Pa or more and 20 Pa or less. The pressure in the exit chamber 70i may be 0 Pa or more and 20 Pa or less.

Next, sterile water is supplied into the intermediate area chamber 70g and the second sterile chamber 70h (rinsing step, symbol S11 in FIG. 9). As a result, the contents adhering to the intermediate area chamber 70g and the second sterile chamber 70h are washed away with the sterile water. At this time, the sterile water may be water sterilized by the water sterilizer 60 . It should be noted that the contents may have flowed from inside the second aseptic chamber 70h into the first aseptic chamber 70f via the intermediate area chamber 70g. Therefore, by supplying sterile water into the first aseptic chamber 70f, the contents adhering to the inside of the first aseptic chamber 70f may be washed away. Also, if there is a cap 88 or bottle 100 that has fallen into the second aseptic chamber 70h, it is collected. Further, the shape of the conveying wheel 12 provided downstream of the cap attaching device 16 may be changed according to the shape of the bottle 100 to be used next. Furthermore, the chuck (not shown) of the capper head may be exchanged in the cap mounting device 16 according to the size of the cap 88 to be used next.

Next, the inside of the second aseptic chamber 70h is washed while the inside of the first aseptic chamber 70f is maintained in an aseptic state. At this time, first, the interior of the intermediate area chamber 70g and the interior of the second aseptic chamber 70h are cleaned (COP) (COP step, symbol S12 in FIG. 9). At this time, cleaning agents such as alkaline agents, water, etc. are injected into the intermediate area chamber 70g and the second aseptic chamber 70h from injection nozzles (not shown) arranged in the intermediate area chamber 70g and the second aseptic chamber 70h. Injected within 70 hours. As a result, the inner wall surfaces of the intermediate area chamber 70g and the surfaces of equipment such as the filling device 20 are cleaned. At this time, the water may be sterile water sterilized by the water sterilizer 60 .

Here, when cleaning (COP) the inside of the second aseptic chamber 70h, at least the second bypass line 56 out of the first bypass line 55 and the second bypass line 56 is cleaned (CIP) and sterilized (SIP). preferably. When cleaning (CIP) or sterilizing (SIP) the second bypass line 56, for example, a cleaning agent or A sterilant may be supplied to the second bypass line 56 . Cleaning agents and disinfectants may be, for example, peracetic acid, hydrogen peroxide, alkaline agents, acidic agents, sodium hypochlorite, and the like. Thereafter, the second bypass line 56 may be rinsed with sterile water by supplying sterile water to the second bypass line 56 from the second water tank 52 in which sterile water is stored in advance. In addition, when cleaning (CIP) or sterilizing (SIP) the first bypass line 55, for example, from the connection point CP2 (see FIGS. 1 and 2A etc.) that connects the first bypass line 55 to the water sterilization line 50, cleaning A chemical or disinfectant may be supplied to the first bypass line 55 .

Next, while the inside of the first aseptic chamber 70f is kept aseptic, the undiluted solution filling device 22 is cleaned (CIP) (CIP step, symbol S13 in FIG. 9). At this time, first, the concentrate filling nozzle of the concentrate filling device 22 is covered with a CIP cup (not shown). Next, while rinsing the channel of the content in the stock solution filling device 22 with water, a cleaning agent obtained by adding an alkaline chemical such as caustic soda or an acidic chemical such as nitric acid to water, for example, is supplied to the channel. As a result, the residue of the previous beverage adhering to the flow path of the content inside the concentrate filling device 22 is removed. At this time, the water may be sterile water sterilized by the water sterilizer 60 .

Next, the inside of the second aseptic chamber 70h is sterilized while the inside of the first aseptic chamber 70f is kept aseptic. At this time, first, the undiluted solution filling device 22 is sterilized (SIP) (SIP step, symbol S14 in FIG. 9). At this time, heated steam or hot water is supplied to the flow path of the contents in the undiluted solution filling device 22 . As a result, the flow path of the content inside the undiluted solution filling device 22 is sterilized. At this time, the water may be sterile water sterilized by the water sterilizer 60 .

Next, the inside of the intermediate area chamber 70g and the inside of the second aseptic chamber 70h are sterilized (SOP) (SOP step, symbol S15 in FIG. 9). At this time, a sterilizing agent such as peracetic acid or hydrogen peroxide is injected into the intermediate area chamber 70g and the second aseptic chamber 70h from injection nozzles (not shown) arranged in the intermediate area chamber 70g and the second aseptic chamber 70h. It is injected into the chamber 70h. Thereafter, sterile water is injected into the intermediate area chamber 70g and the second sterile chamber 70h from the injection nozzle (not shown). As a result, the inner wall surfaces of the intermediate area chamber 70g and the surfaces of the devices such as the filling device 20 are sterilized. At this time, sterile water that has been sterilized by the water sterilizer 60 may be used. As a result, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. In addition, before or after sterilizing the inside of the second aseptic chamber 70h with the sterilant, or at the same time, at least the inside of the first aseptic chamber 70f, the air rinse chamber 70e, and the sterilant spray chamber 70d are also cleaned with peracetic acid detergent, It may be rinsed with sterile water that has been sterilized by water sterilizer 60 . This makes it possible to maintain stable sterility for a long period of time and raise the sterility level.

Also, every corner in the first aseptic chamber 70f may be re-sterilized while the second aseptic chamber 70h is being sterilized. At this time, for example, a sterilizing agent such as hydrogen peroxide solution is sprayed into the first aseptic chamber 70f, and then the inside of the first aseptic chamber 70f is dried with hot air, thereby cleaning every corner of the first aseptic chamber 70f. May be resterilized.

In this manner, the content filling system 10 is sterilized.

A CIP cup (not shown) covering the water filling nozzle of the water filling device 21 is then removed. Then, the water kept sterile in the water filling nozzle of the water filling device 21 is discharged into the first sterile chamber 70f. This prevents the bottle 100 from being filled with the sterilant or the like, even if the sterilant or the like enters the water filling nozzle from the outside of the CIP cup. In addition, as described above, when the inside of the first aseptic chamber 70f is re-sterilized, the sterilant is not completely removed from the CIP cup covering the water filling nozzle, and the sterilant is attached to the CIP cup. Even if it is closed, it is possible to prevent the bottle 100 from being filled with a sterilizing agent or the like. The amount of water discharged into the first aseptic chamber 70f is preferably an amount equal to or greater than one bottle 100 to be used in the next production. After that, after the gap closed by the shutter is opened, the next filling of contents is started.

Next, the sterilization method of the water sterilizer 60 will be described with reference to FIGS. 10A to 10E.

Sterilization Method of Water Sterilizer First, after the filling of the beverage in the content filling system 10 is completed, for example, the operation button of the control section 90 is operated. As a result, sterilization (SIP) of the water sterilizer 60 is started. Note that sterilization by the water sterilizer 60 may be performed during production of the product bottles 101 . In this case, even if the water sterilization by the water sterilizer 60 is stopped, the sterile water stored in the second water tank 52 can be used to produce the product bottles 101 .

At the time of sterilization by the water sterilizer 60, first, filling (production) of contents by the contents filling system 10 is finished ("production finished" in FIG. 10A).

After that, at least one of the sterile filters (the first sterile filter 63 and the second sterile filter 65) of the water sterilizer 60 is subjected to a post-production integrity test (first integrity test) (Fig. 10A Reference S20A). That is, at least one of the first sterile filter 63 and the second sterile filter 65 of the water sterilizer 60 undergoes a post-production integrity test. If the foreign matter removing filter 61 is also a sterile filter, at least one of the three filters is subjected to the integrity test. The sterilization of water is confirmed by passing the integrity test results before and after the start of production (no leaks are observed) and by ensuring that the amount of UV irradiation during production was greater than or equal to a specified value or within a specified range. sexuality is guaranteed.

Next, the sterilizer (the first sterilizer 62 and/or the second sterilizer 64 (hereinafter also simply referred to as the first sterilizer 62, etc.)) is cleaned and/or sterilized (sterilizer cleaning and sterilization step, the symbol in FIG. 10A S20). At this time, first, the first sterilizer 62 and the like are cleaned (CIP processing). In the CIP process, after the alkaline cleaning liquid is poured into the flow path or before the alkaline cleaning liquid is flowed into the flow path, an acidic cleaning liquid obtained by adding an acidic agent such as nitric acid or phosphoric acid to water is flowed into the flow path. done by Alkaline cleaning solution is water mixed with caustic soda (sodium hydroxide), potassium hydroxide, sodium carbonate, sodium silicate, sodium phosphate, sodium hypochlorite, surfactant, chelating agent, etc. is. The alkaline cleaning process using an alkaline cleaning liquid and the acid cleaning process using an acidic cleaning liquid may be freely combined and carried out. As a result, residues and the like adhering to the interior of the flow path through which water passes are removed. Alternatively, the CIP treatment may be performed using only hot water or hot water without adding a cleaning agent. Contents do not adhere to the water sterilization line 50 . In addition, in the first sterilizer 62 and the like of the water sterilization line 50, ultraviolet rays are irradiated by the first ultraviolet lamp 67a and the like during production of the product bottles 101. As shown in FIG. As a result, the water sterilization line 50 is less likely to be contaminated with bacteria. Therefore, the CIP treatment of the water sterilization line 50 may be omitted.

Next, the first sterilizer 62 and the like are sterilized (SIP processing). In the SIP step, first, steam or hot water is supplied to the water sterilizer 60 (hot water supply step, symbol S201a in FIG. 10B1). In this case, steam or hot water is supplied to the circulation system 59A including the water sterilizer 60, for example. As a result, the first ultraviolet lamp 67a, the second ultraviolet lamp 67b, and the third ultraviolet lamp 67c (hereinafter simply referred to as the first ultraviolet lamp 67a, etc.) of the first sterilizer 62, etc. are heat sterilized with steam or hot water, respectively. be done. In addition, every corner in the pipe of the first sterilizer 62 and the pipe of the second sterilizer 64 is sterilized by heating with steam or hot water. When sterilizing the first sterilizer 62 and the second sterilizer 64, the foreign substance removing filter 61, the first sterile filter 63 and the second sterile filter 65 may be sterilized at the same time. In addition, by adjusting the temperature, concentration and/or time of the cleaning agent used in the CIP treatment, it is possible to inactivate bacteria (SIP treatment) at the same time without executing subsequent SIP treatment (CSIP treatment). . After the CIP process, SIP process, or CSIP process is completed, the cleaning agent is discharged from the circulation system 59A. After that, a rinsing process is performed to completely remove the cleaning agent. Pure water is supplied from the pure water tank 50a for rinsing. In the rinsing process, it is preferable to confirm that the irradiation amount or illuminance of ultraviolet rays is equal to or higher than a predetermined value by turning on the first ultraviolet lamp 67a or the like.

If the first sterilizer 62 or the like is weak against heat, the first sterilizer 62 or the like may be sterilized with a sterilizing agent (medicine) or a cleaning agent (medicine). At this time, first, a sterilant is supplied to the water sterilizer 60 (sterilant supply step, symbol S201b in FIG. 10B2). In this case, the disinfectant is supplied to the circulation system 59A including the water disinfector 60, for example. The sterilant or cleaning agent is supplied from the sterilant supply unit 96 (see FIGS. 2B and 2C) to the pre-stage sterilizer 62A, the first sterilizer 62, the second sterilizer 64, etc. provided in the water sterilization line 50. can be At this time, it is preferable that the sterilizing agent or cleaning agent does not pass through the foreign matter removing filter 61 and the first sterile filter 63 . That is, it is preferable to circulate the disinfectant or cleaning agent within the circulation system 95A. Specifically, for example, as shown by the thick lines in FIGS. 2B and 2C, the sterilant or cleaning agent passes through a third bypass line 95a provided between the pre-sterilizer 62A and the first sterilizer 62. preferably. Further, as indicated by the thick line in FIG. 2B, the sterilant or cleaning agent preferably passes through a fourth bypass line 95b provided between the first sterilizer 62 and the second sterilizer 64. Thereby, when the water sterilization line 50 is sterilized with a sterilizing agent or a cleaning agent, it is possible to prevent the sterilizing agent or the cleaning agent from passing through the foreign matter removing filter 61 and the first sterile filter 63 . A disinfectant or cleaning agent may be supplied from sampling points SP2-SP4.

The disinfectant may contain peracetic acid. Moreover, when the disinfectant contains peracetic acid, the concentration of the disinfectant may be 1000 ppm or more and 3000 ppm or less. When the concentration of the sterilant is 1000 ppm or more, the sterilization effect of the first sterilizer 62 and the like by the sterilant can be enhanced. Moreover, since the concentration of the sterilizing agent is 3000 ppm or less, the amount of peracetic acid used can be reduced, and the cost for sterilizing the water sterilizer 60 can be reduced.

Moreover, the temperature of the hot water, the disinfectant, or the cleaning agent supplied to the circulation system 59A may be 50°C or higher and 150°C or lower. By setting the temperature of the hot water, the disinfectant, or the cleaning agent to 50° C. or higher, the sterilizing effect and cleaning effect of the first sterilizer 62 and the like by the sterilizing agent can be enhanced. Moreover, since the temperature of the hot water, the sterilizing agent, or the cleaning agent is 150° C. or less, the first sterilizing device 62 and the like can be manufactured at low cost without using special heat-resistant materials.

Next, in the circulation system 95A including the sterilizer (the first sterilizer 62 and/or the second sterilizer 64), the hot water, the sterilant, or the cleaning agent is circulated (hot water circulation step, symbol S202a in FIG. 10B1, Sterilant circulation step, symbol S202b in FIG. 10B2). For example, hot water, a sterilant, or a cleaning agent is circulated in a circulation system 95A including the pre-stage sterilizer 62A, the first sterilizer 62, and the second sterilizer 64 provided in the water sterilization line 50. In this case, in the circulation system 95A including the pre-stage sterilizer 62A, the first sterilizer 62 and the second sterilizer 64, by circulating the sterilant or the like for at least 10 seconds or more and 60 minutes or less, the pre-stage sterilizer 62A and the first sterilizer 62 and second sterilizer 64 may be sterilized. When the circulation time is 10 seconds or longer, the sterilization effect of the first sterilizer 62 or the like by the sterilant or the like can be enhanced. Moreover, since the circulation time is 60 minutes or less, the sterilization time of the first sterilizer 62 and the like can be shortened. Therefore, downtime can be shortened. In addition, in the disinfectant circulation step, the hot water, the disinfectant, or the cleaning agent may be circulated not within the circulation system 95A but within the circulation system 59A.

Also, the hot water, the disinfectant, or the cleaning agent may be circulated with the first ultraviolet lamp 67a or the like turned on. If the first ultraviolet lamp 67a or the like does not have heat resistance, it is preferable to cool the first ultraviolet lamp 67a or the like to a temperature at which the first ultraviolet lamp 67a or the like can be turned on while circulating hot water, a disinfectant, or a cleaning agent. . At this time, heat exchange is preferably performed between the first ultraviolet lamp 67a or the like and the disinfectant or cleaning agent by a heat exchanger 97 provided in the circulation system 95A.

After that, the sterilant or the like is discharged from any of the sampling points SP2 to SP5 (hot water discharge step, symbol S203a in FIG. 10B1, sterilant discharge step, symbol S203b in FIG. 10B2), and then the circulation system 95A is cooled or Rinsing (cooling step, symbol S204a in FIG. 10B1, rinsing step, symbol S204b in FIG. 10B2). That is, when hot water is supplied to the circulation system 59A including the water sterilizer 60 (the above hot water supply step, symbol S201a in FIG. 10B1), the circulation system 59A is cooled (cooling step, symbol S204a in FIG. 10B1). On the other hand, when the sterilant or the like is supplied to the circulation system 59A including the water sterilizer 60 (the above-described sterilant supply step, symbol S201b in FIG. 10B2), the circulation system 95A is rinsed (rinsing step, symbol S204b in FIG. 10B2). When the sterilizing agent or the like is discharged, the sterilizing agent may be discharged in a short time while aseptic air is supplied to the piping in order to prevent contamination of the sterilized piping. The rinsing process may be performed without performing the disinfectant discharge process.

In the rinsing process, first, the pre-stage sterilizer 62A is sufficiently rinsed with rinsing water so that the sterilant does not adhere to the foreign matter removing filter 61. FIG. At this time, the rinsing water may be discharged from the first drain pipe 95c provided upstream of the foreign matter removing filter 61 . At this time, it is preferable to drain water from the first drain pipe 95c while maintaining positive pressure in the pipe supplying water to the foreign matter removing filter 61 . In this case, while water is being discharged from the first drain pipe 95c, it is advisable to confirm that the pressure inside the pipe is positive. After that, the rinsing water is passed through the foreign matter removing filter 61 .

Next, the sterilant remaining in the first sterilizer 62 is thoroughly rinsed with rinsing water. At this time, the rinse water may be discharged from the second drain pipe 95 d provided upstream of the first sterile filter 63 . At this time as well, it is preferable to drain water from the second drain pipe 95d while maintaining positive pressure in the pipe that supplies water to the first sterile filter 63 . In this case, while water is being discharged from the second drain pipe 95d, it is advisable to confirm that the pressure inside the pipe is positive. After that, the rinse water is passed through the first sterile filter 63 . After that, similar operations are performed in order toward the downstream side. Before discharging water from the first drain pipe 95c or the second drain pipe 95d, the first drain pipe 95c and the like may be sterilized in advance with steam or hot water.

Next, the sterile filters (the first sterile filter 63 and the second sterile filter 65 (hereinafter also simply referred to as the first sterile filter 63, etc.)) are sterilized (filter cleaning and sterilization step, symbol S21 in FIG. 10A). At this time, first, heated steam (fluid) or hot water (fluid) is supplied to the flow path of the first sterile filter 63 or the like (fluid supply step, symbol S211 in FIG. 10A). At this time, for example, steam for sterilization is supplied to the first sterile filter 63 and the like from the sterile air supply port 60a.

Next, the temperature of the heated steam or hot water supplied to the flow path of the first aseptic filter 63 or the like is measured, and the F value is calculated based on the measured temperature (F value calculation step, symbol in FIG. 10A S212).

After that, when the F value becomes equal to or greater than the target value, sterilization of the first sterile filter 63 and the like is terminated. In this way, the first sterile filter 63 and the like are sterilized. By heat sterilizing the first sterile filter 63 and the like using the F value in this way, the first sterile filter 63 and the like can be sterilized without applying excessive heat to the first sterile filter 63 and the like. . Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Moreover, since the first sterile filter 63 and the like can be sterilized without applying excessive heat to the first sterile filter 63 and the like, damage to the membrane of the first sterile filter 63 and the like can be suppressed. Therefore, the life of the first sterile filter 63 and the like can be lengthened, and the first sterile filter 63 and the like can be used for a long period of time without being replaced. For example, the first sterile filter 63 and the like may be sterilized at 121° C. or higher for 20 minutes (timer method) without calculating the F value.

When sterilizing the first sterile filter 63 and the like, the area to be sterilized by steam may be defined by opening and closing valves (not shown) provided at the sampling points SP1 to SP6. For example, the steam that sterilizes the first sterile filter 63 may be supplied to the region between sampling points SP3 and SP4 to sterilize that region. Also, the steam that sterilizes the second sterile filter 65 may be supplied to the area between the sampling points SP5 and SP6 to sterilize the area. Note that the foreign matter removing filter 61 may be sterilized together with the first sterile filter 63 and the second sterile filter 65 .

In this manner, SIP processing is performed on the first sterile filter 63 and the second sterile filter 65 . After that, the first sterile filter 63 and the second sterile filter 65 are cooled (S213 in FIG. 10A).

Next, at least one of the sterile filters (the first sterile filter 63 and the second sterile filter 65) of the water sterilizer 60 is subjected to an integrity test (second integrity test) (S22 in FIG. 10A). ). That is, at least one of the first sterile filter 63 and the second sterile filter 65 of the water sterilizer 60 is subjected to an integrity test before production (reference S22 in FIG. 10A). In the integrity test, first, water is supplied to the housing (not shown) in the first sterile filter 63 or the like (wetting step (not shown)). The wetting step is performed with the first ultraviolet lamp 67a and the like turned on. As a result, the water irradiated with ultraviolet rays passes through the first sterile filter. Next, after closing the valve (not shown) near the first sterile filter 63 and the like to drain the water in the first sterile filter 63 and the like, sterile air is supplied to the first sterile filter 63 and the like. At this time, aseptic air is injected into the first aseptic filter 63 and the like filled with water from, for example, aseptic air supply port 60a. Then, the sterile air supplied to the first sterile filter 63 and the like is gradually pressurized, and the bubble point value of the first sterile filter 63 and the like is measured. After that, it is confirmed whether or not the first sterile filter 63 and the like are complete (whether or not sterile air leaks at a predetermined pressure) based on the bubble point values measured a plurality of times (for example, three times).

Here, for example, water cannot be supplied to the first sterile filter 63 while the integrity test is being performed on the first sterile filter 63 . On the other hand, when water continues to stay in the main body 66 (see FIGS. 3 to 6B) of the first sterilizer 62, etc., the temperature of the water in the main body 66 rises due to the heat of the first ultraviolet lamp 67a. do. In particular, when the first ultraviolet lamp 67a or the like is a medium-pressure mercury lamp, the operating temperature of the medium-pressure mercury lamp is high (approximately 600° C. or higher and 900° C. or lower). can rise. For this reason, for example, while the integrity test is being performed on the first sterile filter 63, for example, as indicated by the thick line in FIG. It is preferable to circulate inside. As a result, overheating of the first ultraviolet lamp 67a and the like can be suppressed, and damage to the first ultraviolet lamp 67a and the like can be suppressed.

After that, the content filling (production) by the content filling system 10 is restarted. It should be noted that water sterilized by the first sterilizer 62 is preferably used for the integrity test. Also, aseptic air should be used for the integrity test.

As shown in FIG. 10C, the order of the sterilizer cleaning/sterilizing step (S20 in FIG. 10A) and the filter cleaning/sterilizing step (S21 in FIG. 10A) may be reversed. Further, as shown in FIG. 10D, during the SIP of the foreign matter removal filter 61, the first sterile filter 63, and the second sterile filter 65 (for example, during the cooling of the first sterile filter 63, etc.), the first sterilizer 62 and the second The cleaning and sterilizing steps of the 2 sterilizers 64 may be performed in parallel. In this case, pipes or valves positioned upstream or downstream such as the first sterile filter 63 come into contact with the sterilant. Therefore, the cooling time can be shortened. Specifically, the sterilant is supplied to the first sterilizer 62 and the second sterilizer 64 from the time when the foreign matter removal filter 61, the first sterile filter 63, and the second sterile filter 65 are each cooled to less than 110°C. May be. As a result, the sterilizer cleaning and sterilizing process can be terminated while the foreign matter removing filter 61, the first sterile filter 63, and the second sterile filter 65 are being cooled.

In addition, in the first sterilizer 62 and the like, ultraviolet rays are irradiated by the first ultraviolet lamp 67a and the like during production of the product bottles 101 . As a result, the first sterilizer 62 and the like are less likely to be contaminated with bacteria. Therefore, when sterilizing the water sterilizer 60, the first sterilizer 62 and the like do not have to be sterilized.

As another embodiment, as shown in FIG. 10E, the step of sterilizing the sterile filters (the first sterile filter 63 and the second sterile filter 65) of the water sterilizer 60 is performed by the sterilizer (the first sterilizer 62 and second sterilizer 64) or while the step of sterilizing the sterilizers (first sterilizer 62 and second sterilizer 64) is being performed. That is, the first sterile filter 63 and the second sterile filter 65 of the water sterilizer 60 and the first sterilizer 62 and the second sterilizer 64 may be cleaned and sterilized at the same time.

In this case, first, filling (production) ends, as shown in FIG. 10E. After that, at least one of the first sterile filter 63 and the second sterile filter 65 is subjected to a post-production integrity test (first integrity test) (reference S30 in FIG. 10E).

Next, cleaning (CIP) processing of the first sterile filter 63, the second sterile filter 65, the first sterilizer 62, and the second sterilizer 64 is performed (S31 in FIG. 10E). At this time, the cleaning agent and the sterilizing agent are supplied from before (upstream side) the foreign matter removing filter 61, and the circulation line 59 is used to circulate the cleaning agent and the sterilizing agent in the circulation system 59A for a predetermined time.

After the CIP treatment, sterilization (SIP) treatment of the first sterile filter 63, the second sterile filter 65, the first sterilizer 62, and the second sterilizer 64 may be performed (S32 in FIG. 10E). Alternatively, instead of CIP processing and SIP processing, cleaning and sterilization of the first sterile filter 63, the second sterile filter 65, the first sterilizer 62, and the second sterilizer 64 may be performed simultaneously (CSIP processing) (Fig. 10E reference S33).

Cleaning agents and disinfectants used for CIP treatment, SIP treatment, or CSIP treatment include acidic agents such as peracetic acid, acetic acid, hydrogen peroxide, pernitric acid, nitric acid, and phosphoric acid, and alkaline agents such as sodium hydroxide and potassium hydroxide. Chemical agents, chlorine-based agents such as sodium hypochlorite and chlorine dioxide, alcohols such as ethyl alcohol and isopropyl alcohol, ozone water, acidic water, and surfactants may be used alone, and two or more of these may be used. may be used in combination. A heater (not shown) may be used to raise the temperature of the detergent and disinfectant. The CIP treatment, SIP treatment, or CSIP treatment is performed under predetermined conditions (temperature, concentration, time) based on the values of the thermometer T and densitometer 59c installed in the water sterilizer 60 and circulation line 59. Also good.

The cleaning agent and disinfectant are discharged from the circulation system 59A by supplying pure water from the pure water tank 50c to the circulation system 59A and conveying the pure water from the pump P1, thereby replacing the disinfectant with pure water. It's okay to be broken. Further, water may be supplied to the circulation system 59A from another device (not shown), and the sterilant may be discharged. The discharge of the sterilant may be performed while monitoring the value of the densitometer 59c provided on the downstream side of the circulation line 59. FIG. In this case, for example, it is preferable to rinse the circulation system 59A with rinsing water until the value of the densitometer 59c becomes the same as the value of the densitometer (not shown) provided in the pure water production apparatus 50a. Also, in the rinsing process, the rinsing time may be controlled by a timer. Also, the rinsing process may be set to be completed when a predetermined time has elapsed. During the CIP process, the SIP process, or the CSIP process, the first ultraviolet lamp 67a and the like may or may not be lit. Also, the first ultraviolet lamp 67a and the like may be turned on only during the rinsing process. After the CIP treatment and SIP treatment or CSIP treatment is completed, at least one of the first sterile filter 63 and the second sterile filter 65 is subjected to a pre-production integrity test (second integrity test) ( Reference S34 in FIG. 10E). That is, one or both of the first sterile filter 63 and the second sterile filter 65 are subjected to integrity testing prior to production.

Next, when the result of the integrity test before the start of production is passed (when no leak is found), the production preparation process is started (S35 in FIG. 10E). In the production preparation process, while circulating pure water in the circulation system 59A, it is confirmed that the illuminance of ultraviolet rays emitted from the first ultraviolet lamps 67a and the like is equal to or higher than a predetermined value. In this case, in each sterilizer (first sterilizer 62 or second sterilizer 64), the total irradiation dose of the first ultraviolet lamp 67a may be, for example, 10 mJ/cm ² or more, and may be 100 mJ/cm It is preferably ² or more.

Then start production.

In addition, the contents do not adhere to the water sterilizer 60 . In addition, in the first sterilizer 62 and the like, ultraviolet rays are irradiated by the first ultraviolet lamp 67a and the like during production of the product bottles 101 . As a result, the first sterilizer 62 and the like are less likely to be contaminated with bacteria. Therefore, when sterilizing the water sterilizer 60, the first sterilizer 62 and the like do not have to be sterilized.

As described above, according to the present embodiment, the content filling system 10 includes the water sterilization line 50 for non-heat sterilization of water, the stock solution sterilization line 70 for heat sterilizing the product stock solution, the water sterilization line 50 and the stock solution sterilization. A filling device 20 is connected to the line 70 and fills the bottle 100 with water and the product concentrate. Compared to diluting the undiluted product solution with sterile water made using a sterilizer that heats and sterilizes water, this reduces the amount of carbon dioxide emitted when making the contents. can. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Moreover, according to the present embodiment, the content filling system 10 further includes a control section 90 that controls the water sterilization line 50 . Then, the control unit 90 discharges water to the outside of the water sterilization line 50 when the irradiation amount or illuminance of ultraviolet rays is equal to or less than a predetermined value. As a result, the sterility of the second water tank 52 and the like can be maintained.

Further, according to this embodiment, the filling device 20 has the water filling device 21 connected to the water sterilization line 50 and the concentrate filling device 22 connected to the concentrate sterilization line 70 . Further, the water filling device 21 fills the bottle 100 with sterilized water, and the concentrate filling device 22 fills the bottle 100 with the sterilized product concentrate. As a result, it is possible to narrow the area where stains due to the contents adhere. Therefore, the area to be cleaned and sterilized can be narrowed. As a result, the amount of steam used can be reduced. Also, cleaning time and sterilization time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Further, according to the present embodiment, the water filling device 21 fills the empty bottle 100 with water. Further, the filling speed at which the water filling device 21 fills the bottle 100 with water is faster than the filling speed at which the concentrate filling device 22 fills the bottle 100 with the product concentrate. As a result, the number of water filling nozzles of the water filling device 21 can be reduced without causing dirt to adhere to the periphery of the bottle 100 . Therefore, the size of the water filling device 21 can be reduced without causing dirt to adhere to the periphery of the bottle 100 .

Further, according to the present embodiment, the water sterilization line 50 includes the first water tank 51 that stores water, the water sterilizer 60 that non-heat sterilizes the water stored in the first water tank 51, and the water sterilizer. and a second water tank 52 for storing water sterilized by the machine 60 . In addition, the undiluted solution sterilization line 70 includes a first undiluted solution tank 71 that stores the undiluted product, a undiluted product sterilizer 80 that thermally sterilizes the undiluted product stored in the first undiluted solution tank 71, and a sterilized by the undiluted product sterilizer 80. and a second undiluted solution tank 72 for storing the product undiluted solution. Thereby, the flow of water and the product stock solution can be made smooth.

Further, according to the present embodiment, the first bypass line 55 that connects the water sterilization line 50 and the cap sterilizer 18 to each other is provided downstream of the second water tank 52 . As a result, the water sterilized by the water sterilizer 60 can be used for washing the cap 88 . Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be further reduced.

Further, according to the present embodiment, the addition unit 75 for adding solids to the product concentrate is connected to the downstream side of the second concentrate tank 72 . As a result, the content filling system 10 can fill the bottle 100 with the solid content.

Further, according to the present embodiment, the content filling system 10 includes a preform sterilization device 34a that sterilizes the preform 100a, a blow molding section (container molding device) 32 that molds the bottle 100 from the preform 100a, A sterilization device (container sterilization device) 11 for sterilizing the bottle 100 is further provided. Then, the blow molding section (container molding apparatus) 32 molds the bottle 100 without adjusting the temperature of the bottle 100 with the hot water of the mold temperature controller. As a result, bacteria adhering to the bottle 100 can be reduced, and the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Moreover, since hot water need not be supplied to the mold of the blow molding section 32, the blow molding section 32 can be simplified.

(Modification of contents filling system)
Next, a modification of the contents filling system will be described.

（ただし、Ｔは任意の殺菌温度（℃）、１０＾｛（Ｔ－Ｔｒ）／Ｚ｝は任意の殺菌温度Ｔでの致死率、Ｔｒは基準温度（℃）、ＺはＺ値（℃）を表す。）
において、基準温度Ｔｒが１２１．１℃、Ｚ値が１０℃の場合に算出されるＦ値である。 (First modification)
Although the water sterilization line 50 (the water sterilizer 60) sterilizes water without heating in the above-described embodiment, the present invention is not limited to this. For example, the water sterilization line 50 (water sterilizer 60) may sterilize water by heating the water to a predetermined temperature. The number of bacteria in the pure water produced by the pure water production device 50a is generally less than that in the product stock solution if the pure water production device 50a is properly managed. Therefore, if the pH of the contents after filling or after the cap 88 is attached to the bottle 100 is less than 4.5, the water sterilization line 50 (the first sterilizer 62 and the second sterilizer 64) has an F ₀ value of You may sterilize water so that is 0.00029 or more and less than 3.1. Further, when the pH of the contents is 4.5 or higher, the water sterilization line 50 (the first sterilizer 62 and the second sterilizer 64) dispenses water so that the _F0 value is 3.1 or more and 100 or less. You can sterilize it. When filling contents with different pH while switching, the water sterilization line 50 (first sterilizer 62 and second sterilizer 64) is unified in order to reduce the number of times of washing and/or sterilization of the water sterilization line 50. The water may be sterilized so that the _F0 value is 3.1 or more and 100 or less. where the F ₀ value is the formula given above:

(However, T is an arbitrary sterilization temperature (° C.), 10^{(T−Tr)/Z} is the lethality rate at an arbitrary sterilization temperature T, Tr is the reference temperature (° C.), Z is the Z value (° C.) represents.)
is the F value calculated when the reference temperature Tr is 121.1°C and the Z value is 10°C.

According to this modification, compared to the case of using a sterilizer that sterilizes water by heating it to a high temperature at the same time as the product stock solution with the same sterilization strength as the product stock solution (usually, the _F0 value is about 30 or more and 80 or less). Therefore, the amount of carbon dioxide emitted when sterilizing water can be reduced. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Also, when the water sterilization line 50 (the first sterilizer 62 and the second sterilizer 64) changes the sterilization conditions based on the pH of the contents, the amount of carbon dioxide emitted when sterilizing water can be further reduced, and the amount of carbon dioxide emitted by the content filling system 10 can be further reduced.

(Second modification)
In the above-described embodiment, the water filling device 21 fills the bottle 100 with sterilized water, and the undiluted solution filling device 22 fills the water-filled bottle 100 with a sterilized product. Although the example of filling the undiluted solution has been described, the present invention is not limited to this. For example, the undiluted solution filling device 22 may fill the bottles 100 with sterilized product undiluted solution, and the water filling device 21 may fill the bottles 100 filled with the product undiluted solution with sterilized water. good.

In this case, as shown in FIG. 11, the undiluted solution filling device 22 may be arranged upstream of the water filling device 21 in the transport direction of the bottle 100 . Also, the undiluted solution filling device 22 may be housed inside the first sterile chamber 70f, and the water filling device 21 may be housed inside the second sterile chamber 70h.

(Third modification)
Further, in the above-described embodiment, an example in which the undiluted product solution is diluted with water has been described, but the present invention is not limited to this. For example, only one of the water filling device 21 and the concentrate filling device 22 may be used to fill the bottle 100 with water or the product concentrate. Specifically, the bottle 100 may be filled only with water by using only the water filling device 21 . That is, mineral water may be produced by using only the water filling device 21 in the content filling system 10 . Alternatively, the bottle 100 may be filled with only the product concentrate by using only the concentrate filling device 22 . That is, in the content filling system 10, a so-called conch product (concentrated product) may be manufactured by using only the concentrate filling device 22. It should be noted that when the bottles 100 are filled only with product concentrates that do not require sterilization, the bottles 100 may be fed to the transport wheels 12 housed inside the intermediate area chamber 70g.

According to this modification, only one of the water filling device 21 and the concentrate filling device 22 is used to fill the bottle 100 with water or the product concentrate. As a result, mineral water and so-called conch products can be produced in the content filling system 10 . Therefore, the types of product bottles 101 produced by the content filling system 10 can be increased.

(Fourth modification)
Further, in the above-described embodiment, an example in which the filling device 20 has the water filling device 21 connected to the water sterilization line 50 and the concentrate filling device 22 connected to the concentrate sterilization line 70 has been described. . In this case, the filling device 20 may have a plurality of undiluted solution filling devices 22 . Further, for example, as shown in FIG. 12A , the content filling system 10 may include a plurality of (for example, two) undiluted solution sterilization lines 70 . The filling device 20 may have a plurality of (for example, two) stock solution filling devices 22 connected to each of the stock solution sterilization lines 70 .

In this case, the filling device 20 may have a first liquid concentrate filling device 22a for filling the product liquid concentrate without flavor and a second liquid concentrate filling device 22b for filling the product liquid concentrate containing flavor. In other words, of the two concentrate filling devices 22, one of the concentrate filling devices 22 may be, for example, a filling device (first concentrate filling device 22a) that fills a product concentrate containing no flavor such as tea-based beverages. good. The other concentrate filling device 22 may be a filling device (second concentrate filling device 22b) that fills product concentrates containing flavors such as fruit beverages, milk drinks, and sports drinks. The second concentrate filling device 22b may be a filling device that fills solids.

As described above, since the filling device 20 has the first concentrate filling device 22a and the second concentrate filling device 22b, when the bottle 100 is filled with a flavorless content such as a tea-based beverage, It is possible to prevent the scent of the previous contents from adhering to the contents. Further, when one of the concentrate filling devices 22 is a filling device (first concentrate filling device 22a) that fills the product concentrate containing no flavor, the flow path of the product concentrate in the first concentrate filling device 22a, etc. No flavor sticks. For example, the flavor does not adhere to seal elements such as packings provided at connection points of each pipe and each device. Therefore, when switching the type of contents, the area to be cleaned (CIP) can be narrowed. As a result, cleaning time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

In the illustrated example, the first concentrate filling device 22a, the second concentrate filling device 22b and the capping device 16 are housed inside the second aseptic chamber 70h. Also, as shown in FIG. 12B, a chamber wall 710 is provided inside the second aseptic chamber 70h. The chamber wall 710 includes a first space (space) 701 in which the first concentrate filling device 22a is accommodated, a second space 702 in which the second concentrate filling device 22b is accommodated, and a second space in which the cap attaching device 16 is accommodated. 3 space 703 is separated. In other words, the first liquid filling device 22a is accommodated in the first space 701 defined by the chamber wall 710. As shown in FIG. The second liquid filling device 22b is housed in a second space 702 defined by the chamber wall 710, and the capping device 16 is housed in a third space 703 defined by the chamber wall 710.

The chamber wall 710 prevents the sterilant or the like in each space from flowing into unintended spaces, and plays a role in stabilizing the pressure in each space. The chamber wall 710 is formed with gaps G1 to G6 (see FIG. 12C described later) through which the bottle 100 can pass. The gaps G1 to G6 are formed to have a minimum size of, for example, about one bottle 100 so that the pressure in each space does not change. Further, the chamber wall 710 may be provided with shutters sh1 to sh6 (see FIG. 12C described later) for opening and closing the gaps G1 to G6. The shutters sh1 to sh6 may be configured to automatically open and close in response to signals from the control section 90, for example.

In addition, since the chamber wall 710 is provided inside the second aseptic chamber 70h in this way, for example, the second space 702 can be cleaned (COP) and sterilized ( SOP) as well as cleaning (CIP) and sterilization (SIP) of the second concentrate filling device 22b. As a result, the downtime can be greatly reduced, and the productivity of the product bottle 101 can be improved. Here, for example, when cleaning (CIP) and sterilizing (SIP) the second concentrate filling device 22b during operation of the first concentrate filling device 22a, even if the shutter sh1 provided on the chamber wall 710 is closed, good. As a result, even if the sterilant or the like is prevented from entering the space (sterile space) housing the first liquid filling device 22a from the space (non-sterile space) housing the second liquid filling device 22b, good.

Of the conveying wheels 12 accommodated in the second aseptic chamber 70h, the first conveying wheel (first wheel) 12a that delivers the bottle 100 to the first concentrate filling device 22a and the bottle 100 from the first concentrate filling device 22a. are arranged outside the first space 701, respectively. Among the transport wheels 12 accommodated in the second aseptic chamber 70h, the third transport wheel 12c that delivers the bottle 100 to the second liquid filling device 22b and the fourth transport wheel that receives the bottle 100 from the second liquid filling device 22b The wheels 12d are arranged outside the second space 702 respectively.

Here, as shown in FIG. 12C, the first transport wheel 12a includes a gripper (first gripper) 121 that transports the bottle 100. As shown in FIG. This gripper 121 is provided so as to be openable and closable.

Similarly, the second to fourth transport wheels 12 b to 12 d each include grippers 122 , 123 , 124 for transporting the bottles 100 . Grippers 122, 123, and 124 are provided so as to be openable and closable.

The first concentrate filling device 22 a also includes a wheel 221 (second wheel), and the wheel 221 (second wheel) is arranged inside the first space 701 . This wheel 221 includes a gripper (second gripper) 222 for carrying the bottle 100 . This gripper 222 is provided so as to be openable and closable.

Similarly, the second concentrate filling device 22b includes a wheel 223, and the wheel 223 is arranged inside the second space 702. As shown in FIG. This wheel 223 contains a gripper 224 that carries the bottle 100 . This gripper 224 is provided so as to be openable and closable.

Next, the case of cleaning and sterilizing the second space 702 (and/or the second concentrate filling device 22b) during operation of the first concentrate filling device 22a accommodated in the first space 701 will be described with reference to FIG. 12C. That is, while filling the product concentrate into the bottle 100 by the first concentrate filling device 22a, the second space 702 and/or the second concentrate filling device 22b (hereinafter also simply referred to as the second space 702, etc.) are cleaned and sterilized. explain.

First, after the filling of the product concentrate in the second concentrate filling device 22b is completed, for example, the operation button of the controller 90 is operated. Thereby, for example, among the gaps G1 to G6 formed in the chamber wall 710, the gaps G1 and G4 are closed by the shutters sh1 and sh4, respectively.

Next, the bottle 100 is conveyed from the first conveying wheel 12a to the first concentrate filling device 22a. At this time, the gripper 123 of the third transport wheel 12c takes the open position so as not to interfere with the gripper 121 of the first transport wheel 12a. In this embodiment, the gripper 123 assumes the open position by rotating the pair of claws of the gripper 123 horizontally by 90 degrees from the closed position. The rotation angle of each claw may be 60 degrees or more and 130 degrees or less.

In this open position the gripper 123 does not interfere with the shutter sh1 closing the gap G1. As a result, when cleaning and sterilizing the second space 702 and the like, the bottle 100 can be transported to the first liquid concentrate filling device 22a while maintaining the inside of the first space 701 in a sterile state.

When the bottle 100 is filled with the product concentrate by the first concentrate filling device 22a, the gripper (second gripper) 222 of the wheel 221 of the first concentrate filling device 22a is replaced by the gripper (first gripper) of the first conveying wheel 12a. Receive bottle 100 from 121 . That is, the bottle 100 is transferred from the first conveying wheel (first wheel) 12a arranged outside the first space 701 to the wheel 221 (second wheel) arranged inside the first space 701. .

Next, the bottle 100 is filled with the product concentrate in the first concentrate filling device 22a. At this time, the bottle 100 conveyed by the gripper 222 is filled with the product concentrate.

Subsequently, the bottle 100 filled with contents is conveyed to the capping device 16 by the second conveying wheel 12b. At this time, the gripper 124 of the fourth transport wheel 12d takes the open position so as not to interfere with the gripper 122 of the second transport wheel 12b. In this embodiment, the gripper 124 assumes the open position by rotating the pair of pawls of the gripper 124 horizontally by 90 degrees from the closed position. The rotation angle of each claw may be 60 degrees or more and 130 degrees or less.

In this open position the gripper 124 does not interfere with the shutter sh4 closing the gap G4. As a result, when cleaning and sterilizing the second space 702 and the like, the bottle 100 can be transported to the capping device 16 while maintaining the inside of the first space 701 and the third space 703 in a sterile state.

Thus, the product bottle 101 filled with the product concentrate by the first concentrate filling device 22a is obtained. During this time, the second space 702 and the like are cleaned and sterilized.

In this way, when cleaning the second space 702 during operation of the first concentrate filling device 22a accommodated in the first space 701, the pressure in the first space 701 is preferably 10 Pa or more and 40 Pa or less. , the pressure in the second space 702 is preferably -10 Pa or more and 10 Pa or less, and the pressure in the third space 703 is preferably 5 Pa or more and 30 Pa or less. As a result, the air in the second space 702 and the air in the third space 703 can be effectively prevented from entering the first space 701, and the aseptic state in the first space 701 can be maintained even better.

When the second space 702 is sterilized during the operation of the first concentrate filling device 22a housed in the first space 701, the pressure in the second space 702 increases to 22a may be higher than the pressure in the second space 702 when cleaning the second space 702. When sterilizing the second space 702, the pressure in the first space 701 is preferably 10 Pa or more and 40 Pa or less, the pressure in the second space 702 is preferably 0 Pa or more and 20 Pa or less, and the third space The pressure inside 703 is preferably 5 Pa or more and 30 Pa or less. As a result, the air in the second space 702 and the air in the third space 703 can be effectively prevented from entering the first space 701, and the aseptic state in the first space 701 can be favorably maintained.

Next, the case where the bottle 100 is not filled with the product concentrate by the first concentrate filling device 22a will be described. Here, during the operation of the second concentrate filling device 22b housed in the second space 702, the first space 701 and/or the first concentrate filling device 22a (hereinafter also simply referred to as the first space 701 and the like) are washed and cleaned. The case of sterilization will be explained with reference to FIG. 12D. That is, a case will be described in which the first space 701 and the like are cleaned and sterilized while the bottle 100 is being filled with the product concentrate by the second concentrate filling device 22b.

First, after the filling of the product concentrate in the first concentrate filling device 22a is completed, for example, the operation button of the controller 90 is operated. Thereby, for example, among the gaps G1 to G6 formed in the chamber wall 710, the gaps G5 and G6 are closed by the shutters sh5 and sh6, respectively.

Next, the bottle 100 is conveyed from the first conveying wheel 12a to the second concentrate filling device 22b. At this time, the gripper (second gripper) 222 of the wheel 221 (second wheel) of the first liquid filling device 22a takes an open position so as not to interfere with the gripper (first gripper) 121 of the first conveying wheel 12a. . In this embodiment, the gripper 222 assumes the open position by rotating the pair of pawls of the gripper 222 horizontally by 90 degrees from the closed position. The rotation angle of each claw may be 60 degrees or more and 130 degrees or less.

In this open position, gripper 222 does not interfere with shutter sh6 closing gap G6. As a result, when cleaning and sterilizing the first space 701 and the like, the inside of the second space 702 can be kept sterile while the bottle 100 can be transported to the second concentrate filling device 22b.

When filling the product concentrate into the bottle 100 by the second concentrate filling device 22b, the gripper 123 of the third conveying wheel 12c receives the bottle 100 from the gripper 121 of the first conveying wheel 12a.

Also, when the bottle 100 is filled with the product concentrate by the second concentrate filling device 22b, the gripper 224 of the wheel 223 of the second concentrate filling device 22b receives the bottle 100 from the gripper 123 of the third conveying wheel 12c. That is, the bottle 100 is transferred from the third conveying wheel 12 c arranged outside the second space 702 to the wheel 223 arranged inside the second space 702 .

Next, the bottle 100 is filled with the product concentrate in the second concentrate filling device 22b. At this time, the bottle 100 conveyed by the gripper 224 is filled with the product concentrate.

Subsequently, the bottle 100 filled with contents is conveyed to the second conveying wheel 12b by the fourth conveying wheel 12d.

The bottle 100 is then transported to the capping device 16 by the second transport wheel 12b. At this time, the gripper 222 of the wheel 221 of the first liquid filling device 22a takes the open position so as not to interfere with the gripper 122 of the second conveying wheel 12b. Also, in this open position, the gripper 222 does not interfere with the shutter sh5 closing the gap G5. Thus, when cleaning and sterilizing the first space 701 and the like, the bottle 100 can be transported to the capping device 16 while maintaining the inside of the second space 702 and the third space 703 in a sterile state.

Thus, the product bottle 101 filled with the product concentrate by the second concentrate filling device 22b is obtained. During this time, the first space 701 and the like are cleaned and sterilized.

When cleaning the first space 701 while the second concentrate filling device 22b accommodated in the second space 702 is in operation, the pressure in the first space 701 is preferably −10 Pa or more and 10 Pa or less. The pressure in the space 702 is preferably 10 Pa or more and 40 Pa or less, and the pressure in the third space 703 is preferably 5 Pa or more and 30 Pa or less. As a result, the air in the first space 701 and the air in the third space 703 can be effectively prevented from entering the second space 702, and the aseptic state in the second space 702 can be maintained even better.

When the first space 701 is sterilized during the operation of the second concentrate filling device 22b accommodated in the second space 702, the pressure in the first space 701 increases to the second concentrate filling device accommodated in the second space 702. 22b may be higher than the pressure in the first space 701 when cleaning the first space 701. When sterilizing the first space 701, the pressure in the first space 701 is preferably 0 Pa or more and 20 Pa or less, the pressure in the second space 702 is preferably 10 Pa or more and 40 Pa or less, and the third space The pressure inside 703 is preferably 5 Pa or more and 30 Pa or less. As a result, the air in the first space 701 and the air in the third space 703 can be effectively prevented from entering the second space 702, and the aseptic state in the second space 702 can be favorably maintained.

To summarize the above, the pressure in each space may be as shown in Tables 3 and 4 below.

According to this modification, the filling device 20 has a plurality of concentrate filling devices 22 . As a result, for example, the second concentrate filling device 22b can be cleaned (CIP) and sterilized (SIP) while the first concentrate filling device 22a is in operation. As a result, the downtime can be greatly reduced, and the productivity of the product bottle 101 can be improved.

Moreover, according to this modification, the content filling system 10 includes a plurality of undiluted solution sterilization lines 70 . A plurality of undiluted solution filling devices 22 are connected to the respective undiluted solution sterilization lines 70, respectively. As a result, the types of product bottles 101 produced by the content filling system 10 can be increased.

Further, according to this modification, the filling device 20 has a first liquid concentrate filling device 22a that fills the product liquid concentrate that does not contain flavor, and a second liquid concentrate filling device 22b that fills the product liquid concentrate that contains flavor. there is As a result, when the bottle 100 is filled with a flavor-free content, it is possible to prevent the scent of the previous content from adhering. In addition, since the first liquid concentrate filling device 22a is filled with the product liquid concentrate that does not contain flavor, the flavor does not adhere to the flow path of the product liquid concentrate in the first liquid concentrate filling device 22a. Therefore, when switching the type of contents, the area to be cleaned (CIP) can be narrowed. As a result, cleaning time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Further, at this time, since the first concentrate filling device 22a and the second concentrate filling device 22b are connected to mutually different concentrate sterilization lines 70, for example, the concentrate to which the first concentrate filling device 22a is connected In the sterilization line 70, washing for removing flavor (so-called deodorizing CIP) may not be performed. Here, deodorizing CIP requires more time and energy than normal CIP. Therefore, when the deodorizing CIP is not performed, the downtime can be shortened and energy can be saved as compared with the case where the deodorizing CIP is performed.

Further, according to this modification, when the bottle 100 is filled with the product concentrate by the first concentrate filling device 22a, the gripper (second gripper) 222 of the wheel 221 of the first concentrate filling device 22a moves the first conveying wheel 12a. receives the bottle 100 from the gripper (first gripper) 121 of . When the bottle 100 is not filled with the product concentrate by the first concentrate filling device 22a, the gripper (second gripper) 222 of the wheel 221 (second wheel) of the first concentrate filling device 22a is replaced by the gripper of the first conveying wheel 12a. The open position is taken so as not to interfere with the (first gripper) 121 . As a result, the bottle 100 can be transported to the first concentrate filling device 22a when cleaning and sterilizing the second space 702 and the like.

Furthermore, according to this modified example, when the bottle 100 is not filled with the product concentrate by the first concentrate filling device 22a, the gaps G5 and G6 are closed by the shutters sh5 and sh6. Then, the gripper (second gripper) 222 of the wheel 221 of the first liquid filling device 22a takes an open position so as not to interfere with the shutters sh5 and sh6 closing the gaps G5 and G6. As a result, when cleaning and sterilizing the second space 702 and the like, the inside of the second space 702 and the third space 703 can be kept sterile while the bottle 100 can be transported to the first concentrate filling device 22a.

Although the gripper 222 and the like take the open position by rotating the pair of claws of the gripper 222 and the like in the horizontal direction from the closed position, the present invention is not limited to this. Grippers 222, etc. may be in the open position by any configuration. For example, a gripper 222 or the like may assume an open position by bending a pair of pawls upward or downward. Also, the gripper 222 and the like may be provided so as to be openable and closable by configuring a pair of claws to be extendable.

(Another example of the fourth modification)
Next, another example of the fourth modification will be described.

<First example>
In a first example shown in FIG. 12E, the filling system further comprises a fifth sterile chamber 70j, a sixth sterile chamber 70k and a seventh sterile chamber 70m. The fifth aseptic chamber 70j is provided upstream of the first aseptic chamber 70f. The sixth aseptic chamber 70k is provided downstream of the second aseptic chamber 70h. The seventh aseptic chamber 70m is provided downstream of the sixth aseptic chamber 70k. That is, in the illustrated example, the fifth aseptic chamber 70j, the first aseptic chamber 70f, the second aseptic chamber 70h, the sixth aseptic chamber 70k, the seventh aseptic chamber 70m and the exit chamber 70i are connected to the bottle 100 (FIG. 12A etc.). ) are arranged in this order from the upstream side to the downstream side along the conveying direction. Also, the fifth aseptic chamber 70j, the first aseptic chamber 70f, the second aseptic chamber 70h, the sixth aseptic chamber 70k, and the seventh aseptic chamber 70m are arranged side by side on the outer periphery of the circular carrier 110 that rotates and conveys the bottle 100. are placed.

Among them, the conveying wheel 12 for conveying the air-rinsed bottle 100 may be housed inside the fifth aseptic chamber 70j. Inside the sixth aseptic chamber 70k, the second concentrate filling device 22b is accommodated. Also, the capping device 16 is housed inside the seventh aseptic chamber 70m. That is, in the example shown in FIG. 12E, the second concentrate filling device 22b and the capping device 16 are in a sterile chamber (sixth sterile chamber 70k or housed inside the seventh sterile chamber 70m).

In FIG. 12E, bottles 100 previously sterilized upstream are transported to the first aseptic chamber 70f via transport wheel 12 and circular transport 110 located in the fifth aseptic chamber 70j. The bottle 100 is then transported to the water filling device 21 via the transport wheel 12 arranged inside the first aseptic chamber 70f.

Next, in the water filling device 21 , the water sterilized by the water sterilization line 50 is filled into the empty bottle 100 . The water filling device 21 fills the inside of the bottles 100 with water while the plurality of bottles 100 are rotationally conveyed.

The bottle 100 in the first aseptic chamber 70f is then transferred via the carrier wheel 12 located in the first aseptic chamber 70f, the circular carrier 110, and the carrier wheel 12 located in the second aseptic chamber 70h to It is transported to the first liquid filling device 22a.

Next, in the first liquid concentrate filling device 22a, the product liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled into the bottle 100 filled with water by the water filling device 21 in advance. In the first liquid concentrate filling device 22a, the product concentrate is filled into the bottles 100 while the bottles 100 are rotatingly conveyed.

After that, the bottle 100 in the second aseptic chamber 70h passes through the carrier wheel 12 located in the second aseptic chamber 70h, the circular carrier 110, and the carrier wheel 12 located in the sixth aseptic chamber 70k, It is conveyed to the second liquid filling device 22b.

Next, in the second liquid concentrate filling device 22b, another liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled into the bottle 100 previously filled with water and the liquid concentrate. In this second liquid concentrate filling device 22b, the insides of the bottles 100 are filled with other product liquid concentrates while the bottles 100 are rotatingly conveyed.

After that, the bottle 100 in the sixth aseptic chamber 70k is transferred through the carrier wheel 12, the circular carrier 110 located in the sixth aseptic chamber 70k, and the carrier wheel 12 located in the seventh aseptic chamber 70m, It is conveyed to the cap attaching device 16 .

Next, in the capping device 16, the bottle 100 filled with water and product concentrate is closed with a cap 88 (see FIG. 12A, etc.). In this manner, the bottle 100 is sealed such that outside air and/or microorganisms cannot enter the bottle 100 . In this capping device 16, the caps 88 are attached to the mouths of the bottles 100 while the plurality of bottles 100 filled with water and product concentrate are rotated and conveyed. Thus, the product bottle 101 (see FIG. 12A etc.) is obtained.

<Second example>
Next, a second example will be described with reference to FIG. 12F. In a second example shown in FIG. 12F, the filling system further comprises a sixth sterile chamber 70k, a seventh sterile chamber 70m and an eighth sterile chamber 70n. A sixth aseptic chamber 70k is provided downstream of the first aseptic chamber 70f. The seventh aseptic chamber 70m is provided downstream of the second aseptic chamber 70h and the sixth aseptic chamber 70k. The eighth aseptic chamber 70n is provided between the second aseptic chamber 70h and the sixth aseptic chamber 70k. Here, in FIG. 12F, the second aseptic chamber 70h and the sixth aseptic chamber 70k are arranged in parallel downstream of the first aseptic chamber 70f along the transport direction of the bottle 100 (see FIG. 12A etc.). there is That is, in the illustrated example, the first aseptic chamber 70f, the second aseptic chamber 70h or the sixth aseptic chamber 70k, the seventh aseptic chamber 70m and the exit chamber 70i are arranged in the conveying direction of the bottle 100 (see FIG. 12A etc.). , are arranged in this order from the upstream side to the downstream side.

Among them, the sixth aseptic chamber 70k accommodates the second undiluted solution filling device 22b. Also, the capping device 16 is housed inside the seventh aseptic chamber 70m. Further, the conveying wheel 12 for conveying the bottle 100 filled with water by the water filling device 21 may be housed inside the eighth aseptic chamber 70n.

In FIG. 12F, bottles 100 that have been previously sterilized upstream are conveyed to water filling device 21 via conveying wheels 12 located in first aseptic chamber 70f.

Next, in the water filling device 21 , the water sterilized by the water sterilization line 50 is filled into the empty bottle 100 . The water filling device 21 fills the inside of the bottles 100 with water while the plurality of bottles 100 are rotationally conveyed.

The bottles 100 in the first aseptic chamber 70f are then transferred, for example, to the transport wheel 12 located in the first aseptic chamber 70f, the transport wheel 12 located in the eighth aseptic chamber 70n, and the second aseptic chamber 70h. is conveyed to the first liquid filling device 22a via the conveying wheel 12 arranged in the .

Next, in the first liquid concentrate filling device 22a, the product liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled into the bottle 100 filled with water by the water filling device 21 in advance. In the first liquid concentrate filling device 22a, the product concentrate is filled into the bottles 100 while the bottles 100 are rotatingly conveyed.

The bottle 100 in the second aseptic chamber 70h is then placed in the carrier wheel 12 located in the second aseptic chamber 70h, the carrier wheel 12 located in the eighth aseptic chamber 70n, and the seventh aseptic chamber 70m. It is conveyed to the cap attaching device 16 via the conveying wheel 12 .

Next, in the capping device 16, the bottle 100 filled with water and product concentrate is closed with a cap 88 (see FIG. 12A, etc.). Thus, the product bottle 101 (see FIG. 12A etc.) is obtained.

Here, the bottle 100 in the first aseptic chamber 70f may be transported to the second concentrate filling device 22b without being transported to the first concentrate filling device 22a. For example, the bottle 100 in the first sterile chamber 70f is placed in the carrier wheel 12 located in the first sterile chamber 70f, the carrier wheel 12 located in the eighth sterile chamber 70n, and the sixth sterile chamber 70k. It may be conveyed to the second liquid filling device 22b via the conveying wheel 12. In this case, the bottle 100 in the first aseptic chamber 70f is not transported to the first concentrate filling device 22a arranged in the second aseptic chamber 70h.

When the bottle 100 is conveyed to the second liquid concentrate filling device 22b, another product liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled in the bottle 100 previously filled with water in the second liquid concentrate filling device 22b. . In this second liquid concentrate filling device 22b, the insides of the bottles 100 are filled with other product liquid concentrates while the bottles 100 are rotatingly conveyed.

The bottle 100 in the sixth aseptic chamber 70k is then transferred to the capping device 16 via the transport wheel 12 located in the sixth aseptic chamber 70k and the transport wheel 12 located in the seventh aseptic chamber 70m. be transported.

Thus, in the second example shown in FIG. 12F, when the product concentrate is filled into the bottle 100 by the second concentrate filling device 22b, the bottle 100 is filled with the first aseptic chamber 70f, the eighth aseptic chamber 70n, and the second aseptic chamber 70n. 6 aseptic chamber 70k and then through the seventh aseptic chamber 70m in sequence.

In the example shown in FIG. 12F, when producing mineral water in the content filling system 10, the bottle 100 filled with water by the water filling device 21 in the first aseptic chamber 70f is placed in the seventh aseptic chamber 70m. may be transported directly to the capping device 16 located in the . In other words, the bottle 100 filled with water is not transferred to the first liquid filling device 22a or the second liquid filling device 22b, but capped only through the transfer wheel 12 arranged in the eighth aseptic chamber 70n. It may be transported directly to the device 16 . In this case, the product bottle 101 is obtained by attaching the cap 88 to the mouth of the bottle 100 filled only with water. In this case, as described with reference to FIGS. 12C and 12D, it is preferable that the grippers of the transport wheels 12 adjacent to the first liquid filling device 22a or the second liquid filling device 22b take the open position. . Thereby, interference between grippers can be suppressed.

<Third example>
Next, a third example will be described with reference to FIG. 12G. In the third example shown in FIG. 12G, unlike the second example shown in FIG. 6 aseptic chamber 70k, eighth aseptic chamber 70n, and seventh aseptic chamber 70m, in that order. Other configurations of the content filling system 10 according to the third example are the same as those of the second example shown in FIG. 12F, so detailed description thereof is omitted here.

<Fourth example>
Next, a fourth example will be described with reference to FIG. 12H. In a fourth example shown in FIG. 12H, the filling system further comprises a sixth sterile chamber 70k, a seventh sterile chamber 70m and a ninth sterile chamber 70p. The sixth sterile chamber 70k is provided downstream of the first sterile chamber 70f and the second sterile chamber 70h. The seventh aseptic chamber 70m is provided downstream of the sixth aseptic chamber 70k. The ninth aseptic chamber 70p is provided between the first aseptic chamber 70f, the second aseptic chamber 70h, the sixth aseptic chamber 70k, and the seventh aseptic chamber 70m.

Further, a second concentrate filling device 22b is housed inside the sixth aseptic chamber 70k. Also, the capping device 16 is housed inside the seventh aseptic chamber 70m. Further, the carrier wheel 12 may be housed inside the ninth sterile chamber 70p.

In FIG. 12H, a bottle 100 previously sterilized upstream is passed through the water filling device via the transport wheel 12 located in the ninth aseptic chamber 70p and the transport wheel 12 located in the first aseptic chamber 70f. Transported to 21.

Next, in the water filling device 21 , the water sterilized by the water sterilization line 50 is filled into the empty bottle 100 . The water filling device 21 fills the inside of the bottles 100 with water while the plurality of bottles 100 are rotationally conveyed.

The bottles 100 in the first aseptic chamber 70f are then placed in the transport wheel 12 located in the first aseptic chamber 70f, the transport wheel 12 located in the ninth aseptic chamber 70p, and the second aseptic chamber 70h. It is conveyed to the first liquid filling device 22a via the conveying wheel 12.

Next, in the first liquid concentrate filling device 22a, the product liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled into the bottle 100 filled with water by the water filling device 21 in advance. In the first liquid concentrate filling device 22a, the product concentrate is filled into the bottles 100 while the bottles 100 are rotatingly conveyed.

The bottle 100 in the second aseptic chamber 70h is then placed in the carrier wheel 12 located in the second aseptic chamber 70h, the carrier wheel 12 located in the ninth aseptic chamber 70p, and the sixth aseptic chamber 70k. It is conveyed to the second liquid filling device 22b via the conveying wheel 12.

Next, in the second concentrate filling device 22b, another product concentrate sterilized by the concentrate sterilization line 70 is filled into the bottle 100 filled with water in advance. In this second liquid concentrate filling device 22b, the insides of the bottles 100 are filled with other product liquid concentrates while the bottles 100 are rotatingly conveyed.

The bottle 100 in the sixth aseptic chamber 70k is then placed in the transfer wheel 12 positioned in the sixth aseptic chamber 70k, the transfer wheel 12 positioned in the ninth aseptic chamber 70p, and the seventh aseptic chamber 70m. It is conveyed to the cap attaching device 16 via the conveying wheel 12 .

Thus, in the fourth example shown in FIG. 12H, when the product concentrate is filled into the bottle 100 by the first concentrate filling device 22a and the second concentrate filling device 22b, the bottle 100 includes the first aseptic chamber 70f, A ninth sterile chamber 70p, a second sterile chamber 70h, a ninth sterile chamber 70p, a sixth sterile chamber 70k, a ninth sterile chamber 70p, and a seventh sterile chamber 70m are passed in that order.

<Fifth example>
Next, a fifth example will be described with reference to FIG. 12I. In a fifth example shown in FIG. 12I, the filling system further comprises a sixth aseptic chamber 70k, a seventh aseptic chamber 70m and a tenth aseptic chamber 70q. The sixth sterile chamber 70k is provided downstream of the first sterile chamber 70f and the second sterile chamber 70h. The seventh aseptic chamber 70m is provided downstream of the sixth aseptic chamber 70k. A tenth aseptic chamber 70q is provided between the second aseptic chamber 70h and the sixth aseptic chamber 70k.

Further, a second concentrate filling device 22b is housed inside the sixth aseptic chamber 70k. Also, the capping device 16 is housed inside the seventh aseptic chamber 70m. Further, the carrier wheel 12 may be housed inside the ninth sterile chamber 70p.

In the fifth example shown in FIG. 12I, the first liquid concentrate filling device 22a and the second liquid concentrate filling device 22b are filling devices used when the amount of product liquid concentrate to be filled is small. In this case, the first concentrate filling device 22a and the second concentrate filling device 22b respectively include a metering type filling nozzle 22e and a filling nozzle 22f fixed on the mouth of the bottle 100 for use. The first concentrate filling device 22a and the second concentrate filling device 22b may each include a plurality of filling nozzles 22e and a plurality of filling nozzles 22f.

Then, when the bottle 100 reaches the filling nozzles 22e and 22f, the bottle 100 is detected by near-infrared rays. As a result, each bottle 100 is intermittently filled with the product concentrate from the filling nozzles 22e and 22f only while the mouth of the bottle 100 is passing below the filling nozzles 22e and 22f. The filling nozzles 22e and 22f may not be of the type that intermittently fills the product concentrate, but may be of the type that continuously fills the product concentrate.

In FIG. 12I, bottles 100 that have been previously sterilized upstream are transported to water filling device 21 via transport wheels 12 located in first aseptic chamber 70f.

Next, in the water filling device 21 , the water sterilized by the water sterilization line 50 is filled into the empty bottle 100 . The water filling device 21 fills the inside of the bottles 100 with water while the plurality of bottles 100 are rotationally conveyed.

The bottle 100 in the first aseptic chamber 70f is then conveyed to the first liquid concentrate filling device 22a via the conveying wheel 12 arranged in the first aseptic chamber 70f.

Next, in the first liquid concentrate filling device 22a, the product liquid concentrate sterilized by the liquid concentrate sterilization line 70 is filled into the bottle 100 filled with water by the water filling device 21 in advance. In this first concentrate filling device 22a, the bottle 100 is intermittently filled with the product concentrate.

After that, the bottle 100 in the second aseptic chamber 70h is transported to the second concentrate filling device 22b via the transport wheel 12 arranged in the tenth aseptic chamber 70q.

Next, in the second concentrate filling device 22b, another product concentrate sterilized by the concentrate sterilization line 70 is filled into the bottle 100 filled with water in advance. In this second liquid concentrate filling device 22b, the bottle 100 is intermittently filled with another product liquid concentrate.

The bottle 100 in the sixth aseptic chamber 70k is then transported to the capping device 16 via the transport wheel 12 located in the seventh aseptic chamber 70m.

(Fifth modification)
Further, in the above-described embodiment, an example in which the filling device 20 has the water filling device 21 connected to the water sterilization line 50 and the concentrate filling device 22 connected to the concentrate sterilization line 70 has been described. However, it is not limited to this. For example, the content filling system 10 may comprise a single filling device 20, as shown in FIG.

In this case, the content filling system 10 includes a preform sterilization chamber 70a, a molding section chamber 70b, an atmosphere isolation chamber 70c, a sterilant spray chamber 70d, an air rinse chamber 70e, a first aseptic chamber 70f, an outlet It may have a chamber 70i. That is, the content filling system 10 may not have the intermediate area chamber 70g and the second aseptic chamber 70h. The filling device 20 and the capping device 16 may also be housed inside the first aseptic chamber 70f.

In this modification, a mixing tank 57 for mixing water and the product concentrate may be interposed between the water sterilization line 50 and the concentrate sterilization line 70 and the filling device 20 . This allows the contents to be formulated by diluting the product stock solution with water prior to filling. In this case, the mixing tank 57 may be a so-called filling machine tank, and may be installed vertically above the filling device 20 in order to improve the filling accuracy of the filling device 20 . Furthermore, the mixing tank 57 may serve as a so-called cushion tank that ensures smooth flow of the contents even when the amount of the contents used on the downstream side of the mixing tank 57 changes.

Such a mixing tank 57 may be provided with a densitometer for measuring the concentration of the prepared contents. In addition, in order to ensure the concentration of the content prepared in the mixing tank 57, at least one tank such as a filling machine tank may be provided downstream of the mixing tank 57 in which the densitometer is installed. . The volume of the mixing tank 57 may be 0.1 m ³ or more and 30 m ³ or less, and may be 0.3 m ³ as an example. Incidentally, in this modified example, the addition unit 75 described above may be connected to the downstream side of the mixing tank 57 .

In this modification, when cleaning (COP) and sterilizing (SOP) the inside of the first aseptic chamber 70f, for example, of the water sterilization line 50, from the connection point CP3 that connects the water sterilization line 50 and the undiluted solution sterilization line 70 The downstream side of the connection point CP3 may be cleaned (CIP) and sterilized (SIP) while the upstream side is maintained in a sterile state. Similarly, when cleaning (CIP) and sterilizing (SIP) the filling device 20 housed inside the first aseptic chamber 70f, for example, while maintaining the upstream side of the connection point CP3 in a sterile state, the connection The downstream side of point CP3 may be cleaned (CIP) and sterilized (SIP). Also in this case, the area to be cleaned and sterilized can be narrowed. Therefore, the amount of steam used can be reduced. Moreover, since the area to be cleaned and sterilized can be narrowed, the cleaning time and sterilization time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Also, in this modification, compared to the case of diluting the product stock solution with sterile water produced using a sterilizer that heats and sterilizes water, the carbon dioxide emitted when producing the contents emissions can be reduced. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

As shown in FIG. 14, the mixing tank 57 for mixing water and the product concentrate may not be interposed between the water sterilization line 50 and the concentrate sterilization line 70 and the filling device 20 . In this case, the filling device 20 may include a plurality of filling nozzles 20a (see FIG. 15) for filling with water and product concentrate, each filling nozzle 20a having a water sterilization line 50 and a concentrate sterilization line 70, respectively. It may be connected. Then, water and the undiluted product solution may be filled with one filling nozzle 20a.

Specifically, as shown in FIG. 15, the filling nozzle 20a may include a nozzle body portion 20b. The water sterilization line 50 and the undiluted solution sterilization line 70 may be connected to the nozzle main body 20b. The water sterilization line 50 and the concentrate sterilization line 70 may each be provided with a flow meter F and a valve V2 for measuring the flow rate of water or product concentrate. Alternatively, the filling amount of water or undiluted product may be measured by detecting the actual weight of the filled water or undiluted product with a load cell. In this case, the order in which the bottle 100 is filled with water and the product concentrate may be appropriately changed in consideration of foaming in the bottle 100 or ease of mixing of the water and the product concentrate. For example, the undiluted product solution may be filled after the undiluted product solution is filled, or the water may be filled after the undiluted product solution is filled. When water is filled after filling the product undiluted solution, it is possible to reduce the risk of contamination due to the contents adhering to the tip of the filling nozzle 20a. Alternatively, the undiluted product solution may be filled after the water is filled, and then the water may be further filled. Alternatively, water and product concentrate may be filled simultaneously.

In the example shown in FIG. 14, when cleaning (COP) and sterilizing (SOP) the inside of the first aseptic chamber 70f, for example, in the water sterilization line 50, up to the third water tank 54 is maintained in a sterile state, The downstream side of the third water tank 54 may be cleaned (CIP) and sterilized (SIP). Similarly, when cleaning (CIP) and sterilizing (SIP) the filling device 20 housed inside the first aseptic chamber 70f, for example, the water sterilization line 50 up to the third water tank 54 is kept aseptic. In this state, the downstream side of the third water tank 54 may be cleaned (CIP) and sterilized (SIP). Also in this case, the area to be cleaned and sterilized can be narrowed. Therefore, the amount of steam used can be reduced. Moreover, since the area to be cleaned and sterilized can be narrowed, the cleaning time and sterilization time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

Also in this modification, compared to the case of diluting the product undiluted solution with sterilized water produced using a sterilizer that heats and sterilizes water, emissions of carbon dioxide emitted when producing the contents can be reduced. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

(Sixth modification)
Further, in the embodiment described above, an example in which the third water tank 54 is provided downstream of the second water tank 52 has been described. In this case, as shown in FIG. 16A, a carbonation device 58 for adding carbonation to water may be connected to the upstream side of the third water tank 54 .

Here, the water filling device 21 includes a plurality of water filling nozzles 21a (see FIG. 16B) for filling water. In this modification, the water filling nozzle 21a of the water filling device 21 fills with carbonated water. As shown in FIG. 16B, each water filling nozzle 21a is connected to a water sterilization line 50 and a counter gas line 58a. Specifically, the water filling nozzle 21a includes a nozzle body portion 21b. A water sterilization line 50 and a counter gas line 58a are connected to the nozzle main body 21b. One end of the water sterilization line 50 is connected to a third water tank 54 filled with aseptic carbonated water, and the other end communicates with the inside of the bottle 100 . The aseptic carbonated water supplied from the third water tank 54 passes through the water sterilization line 50 and is injected into the bottle 100 .

The counter gas line 58a is a line that supplies aseptic carbon dioxide gas filled in the third water tank 54 toward the water filling nozzle 21a. One end of the counter gas line 58 a is connected to the third water tank 54 and the other end communicates with the inside of the bottle 100 . Then, the counter pressure gas consisting of aseptic carbon dioxide supplied from the third water tank 54 passes through the counter gas line 58a and fills the inside of the bottle 100. As shown in FIG.

A snift line 58b for discharging the gas inside the bottle 100 is connected to each water filling nozzle 21a. One end of the snift line 58b is connected to the counter gas line 58a. Via this snift line 58b, the gas inside the bottle 100 is discharged from the other end of the snift line 58b into the first aseptic chamber 70f.

Furthermore, a packing P (sealing member) is provided at the tip of each water filling nozzle 21a to suppress leakage of gas inside the bottle 100 by being in close contact with the bottle 100. As shown in FIG. When filling the bottle 100 with the carbonated beverage, the water filling device 21 fills the bottle 100 with the carbonated beverage while keeping the packing P in close contact with the mouth of the bottle 100 (adherence filling). As a result, it is possible to prevent the aseptic carbon dioxide gas for counter pressure from leaking from the inside of the bottle 100 . Therefore, the internal pressure of the bottle 100 can be made higher than the atmospheric pressure so that the internal pressure of the bottle 100 is the same as the internal pressure of the third water tank 54 . Although not shown, the water sterilization line 50 and the like may be provided with a flow meter, a valve, and the like for measuring the flow rate of water and the like.

According to this modification, a carbonation device 58 for adding carbonation to water is connected to the upstream side of the third water tank 54 . As a result, the bottle 100 can be filled with the carbonated beverage in the contents filling system 10 . In addition, since the carbonation device 58 is connected to the water sterilization line 50 in this way, when carbonated water is filled as the content, the flavor of the previous content is suppressed from adhering to the carbonated water. can. Only when the bottle 100 is filled with a carbonated beverage, the water from the second water tank 52 is supplied to the carbonation device 58, and after cooling, aseptically carbonic acid gas is added with an aseptic carbonator, and then carbonic acid is added. The water thus obtained may be supplied to the third water tank 54 . Moreover, when producing carbonated water as the content, the undiluted solution filling device 22 may or may not be used.

Even when the water filling device 21 includes the water filling nozzle 21a capable of filling carbonated water, the water filling device 21 may fill water to which carbon dioxide is not added. In this case, mineral water may be produced by using only the water filling device 21 in the contents filling system 10 . In this case also, the water filling device 21 may fill the water while the packing P is in close contact with the mouth of the bottle 100 . This makes it possible to minimize the spillage of water from inside the bottle 100 . In this case, the water filling device 21 may fill water under pressure. As a result, water can be filled in a short time. Here, if the pressure resistance of the bottle 100 is low, the water filling device 21 preferably pressurizes and fills the bottle 100 with water through the snift line 58b in a state in which the gas inside the bottle 100 can be discharged. For example, the water filling device 21 preferably fills water under pressure with the snift line 58b opened after the packing P is brought into close contact with the mouth of the bottle 100 . As a result, deformation and/or breakage of the bottle 100 due to pressure can be suppressed even when water is filled under pressure. Therefore, water can be filled in a short time, and deformation and/or breakage of the bottle 100 can be suppressed.

When the undiluted solution filling device 22 is used together with the water filling device 21, the liquid level of the water filled by the water filling device 21 is lowered compared to when only the water filling device 21 is used. Therefore, there is little risk of the filled water blowing out. Therefore, the water filling speed may be 100 mL/sec or more, preferably 200 mL/sec or more. This makes it possible to further reduce the number of water filling nozzles 21a. In this case, the bottle 100 can be filled with water while the internal pressure of the third water tank 54 is higher than the internal pressure of the third liquid tank 74 . During close contact filling, the internal pressure of the third liquid tank 74 may be 0.02 MPa or more and 0.1 MPa or less, and the internal pressure of the third water tank 54 may be 0.03 MPa or more and 0.9 MPa.

In addition, the water filling device 21 fills the bottle 100 with water in a state in which a gap is formed between the water filling nozzle 21a (packing P) and the bottle 100 without the packing P adhering to the mouth of the bottle 100. It may be filled (orally filled). Even in this case, the bottle 100 can be filled with water while the internal pressure of the third water tank 54 is higher than the internal pressure of the third concentrate tank 74 . Specifically, at the time of top filling, the internal pressure of the third liquid tank 74 may be 0.02 MPa or more and 0.1 MPa or less, and the internal pressure of the third water tank 54 may be 0.03 MPa or more and 0.07 MPa or less. It can be.

Furthermore, when the concentrate filling device 22 is used together with the water filling device 21, the water filling device 21 may fill the empty bottle 100 with water as described above. In this case, foaming in the bottle 100 can be suppressed, so there is little risk of part of the filled liquid splashing outside from the mouth of the bottle 100 . Here, the concentrate filling device 22 includes a plurality of concentrate filling nozzles 22c (see FIG. 16C) for filling the product concentrate. As shown in FIG. 16C, a concentrate sterilization line 70 is connected to each concentrate filling nozzle 22c. Specifically, the undiluted solution filling nozzle 22c includes a nozzle body portion 22d. A concentrate sterilization line 70 is connected to the nozzle main body 22d. Although not shown, the undiluted solution sterilization line 70 may be provided with a flow meter, a valve, and the like for measuring the flow rate of the undiluted product solution.

As described above, when the water filling device 21 fills the empty bottle 100 with water, foaming in the bottle 100 can be suppressed, so that part of the filled liquid flows out from the mouth of the bottle 100 to the outside. Less risk of scattering. Therefore, the diameter of the water filling nozzle 21 a of the water filling device 21 may be larger than the diameter of the liquid filling nozzle 22 c of the liquid filling device 22 . Thereby, the filling time for filling with water can be shortened. For example, the diameter of the water filling nozzle 21 a of the water filling device 21 may be 1.2 times or more and 1.5 times or less the diameter of the liquid filling nozzle 22 c of the liquid filling device 22 . Since the diameter of the water filling nozzle 21a is 1.2 times or more the diameter of the undiluted solution filling nozzle 22c, the filling time for filling water can be further shortened. Further, since the diameter of the water filling nozzle 21a is 1.5 times or less the diameter of the undiluted solution filling nozzle 22c, the risk of part of the filled liquid scattering outside from the mouth of the bottle 100 can be further reduced. In order to reduce the number of water filling nozzles 21a of the water filling device 21 and make the water filling device 21 compact, the filling method (close filling, mouth filling), filling pressure, or the diameter of the water filling nozzle 21a, etc. You may change it suitably.

(Seventh modification)
Moreover, in the embodiment described above, an example in which the water sterilization line 50 has the first water tank 51, the water sterilizer 60, and the second water tank 52 has been described. In this case, the water sterilization line 50 may have a plurality of (for example, two) water sterilizers 60, as shown in FIG. Thus, when one water sterilizer 60 is being cleaned (CIP) or sterilized (SIP), the other water sterilizer 60 can be used to sterilize water. Therefore, the product bottles 101 can be manufactured continuously. Further, for example, when one water sterilizer 60 is cleaned (CIP) or sterilized (SIP) and the other water sterilizer 60 is used to clean the inside of the second aseptic chamber 70h or the like, the second aseptic It is possible to prevent a shortage of water supplied to the chamber 70h and the like. Also, for example, while the first sterile filter 63 or the like of one water sterilizer 60 is sterilized (SIP) or integrity tested, the other water sterilizer 60 is used to wash the inside of the second sterile chamber 70h or the like. In this case, the shortage of water supplied to the second aseptic chamber 70h and the like can be suppressed.

(Eighth modification)
Further, in the above-described embodiment, the water sterilizer 60 includes the foreign matter removal filter 61, the first sterilizer 62, the first sterile filter 63, the second sterilizer 64, and the second sterile filter 65. Although an example has been described, it is not limited to this. For example, if the pure water produced by the pure water production device 50a is highly sanitary and no mold is detected in the first water tank 51, the water sterilizer 60 does not have the foreign matter removal filter 61. good. If the number of bacteria in the first water tank 51 is large, the water sterilizer 60 may further include a third sterilizer (not shown) provided upstream of the foreign matter removal filter 61 . In this case, the configuration of the third sterilizer may be substantially the same as that of the first sterilizer 62 shown in FIGS. 3 to 6B. That is, the third sterilizer may be a sterilizer that sterilizes water with ultraviolet rays.

(Ninth modification)
Further, in the above-described embodiment, the UHT 80 includes the first stage heating section 81, the second stage heating section 82, the holding tube 83, the first stage cooling section 84, the second stage cooling section 85, and the third stage heating section 85. An example having the stage cooling section 86 has been described. In this case, as shown in FIG. 18A, the UHT 80 includes a plurality of (eg, two) second-stage heating units 82, a plurality of (eg, two) holding tubes 83, and a plurality of (eg, two) first-stage heating units. A cooling unit 84 may also be provided. As a result, even if charring or the like adheres to one of the second stage heating section 82, the holding tube 83, or the first stage cooling section 84, etc., the other holding tube 83 or the like is used to sterilize the product stock solution. can. That is, when one holding tube 83 or the like is cleaned (CIP), sterilized (SIP), or cleaned and sterilized (CSIP), the other holding tube 83 or the like can be used to sterilize the product concentrate. Therefore, the product bottles 101 can be manufactured continuously.

(Tenth Modification)
Also, in the above-described embodiment, the product undiluted solution sterilizer 80 has been described as a UHT, but it is not limited to this. For example, the product concentrate sterilizer 80 may be an ohmic (Joule type) heat sterilizer that directly energizes the product concentrate to generate heat by itself. Further, the product concentrate sterilizer 80 may be a sterilizer that sterilizes the product concentrate using microwaves (915 MHz, 2450 MHz). In this case, microwaves may be applied from the outside of the piping through which the product stock solution or solid matter passes. Thereby, the temperature of the product concentrate or solid can be increased, and the product concentrate or solid can be sterilized. Even in these cases, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

(11th modification)
Further, in the above-described embodiment, an example in which the filling device 20 (the water filling device 21 and the concentrate filling device 22) is a so-called rotary filler has been described, but the present invention is not limited to this. For example, the filling device 20 may be a so-called linear aseptic filling machine that fills containers (such as cups or paper containers) transported by a conveyor with water or the like. In this case, for example, sterile water may be first filled and then the product stock solution may be filled. Further, the concentrate filling device 22 for filling the product concentrate containing the flavor or the solid matter may be provided downstream of the concentrate filling device 22 for filling the product concentrate. The order of filling sterile water and undiluted product is not limited to this. For example, the undiluted product solution may be filled first, and then sterile water may be filled. Also, as described with reference to FIG. 15, one filling nozzle 20a may be used to fill sterile water and product undiluted solution.

Here, when the filling device 20 is a so-called linear aseptic filling machine, as shown in FIG. A container molding section 150 may be provided. This container forming section 150 may be arranged in the eleventh aseptic chamber 70r. A conveyor 125 for transporting the container 140 may be provided in the eleventh aseptic chamber 70r. Further, the content filling system 10 may include a sterilant spray nozzle 11A, an air rinse nozzle 160, a habitual folding portion 170, a heating portion 180, and a sealing portion 190. Among them, the sterilant spray nozzle 11A is a nozzle for spraying the sterilant on the inner and outer surfaces of the container 140 . The air rinse nozzle 160 is a nozzle for blowing sterile air onto the inner surface of the container 140 . The habitual folding portion 170 is a portion for folding the container 140 . The heating part 180 is a part that heats the container 140 . The seal portion 190 is a portion that seals the container 140 . The sterilant spray nozzle 11A, the air rinse nozzle 160, the water filling device 21, the stock solution filling device 22, the distorted folding section 170, the heating section 180, and the sealing section 190 are arranged from the upstream side to the downstream side along the conveying direction of the container 140. , may be arranged in this order from the upstream side to the downstream side. In such a content filling system 10, one container 140 may be simultaneously filled with water and a product concentrate from the water filling nozzle 21a and the concentrate filling nozzle 22c. The order in which the bottle 100 is filled with water and the product concentrate may be appropriately changed in consideration of foaming in the bottle 100, ease of mixing of water and the product concentrate, or production capacity. Also, as described with reference to FIG. 15, one filling nozzle 20a may be used to fill sterile water and product undiluted solution.

Also, the content filling system 10 may be a so-called roll-fed aseptic filling system instead of an aseptic filling system that forms the container 140 from the packaging material 130 (sleeve). A roll supply type aseptic filling system is, for example, a filling system that forms a container (paper container or pouch) from a packaging material supplied in roll form and fills the formed container with contents. In this case, as shown in FIG. 18C, the packaging material 200 supplied in roll form is first sterilized by being immersed in a sterilizing solution (eg, hydrogen peroxide) in a sterilizing bath 201 . Both sides of the packaging material may be sterilized by blowing gas or mist of the sterilizing agent on both sides of the packaging material and then drying and removing the sterilizing agent with hot air. Alternatively, both sides of the packaging material may be sterilized by irradiating both sides of the packaging material with electron beams. Next, in the forming section 202, a container (paper container or pouch) 203 is formed by subjecting the packaging material to predetermined processing. In the illustrated example, the paper container 203 is formed by subjecting the packaging material to processing such as heat sealing in the forming unit 202 . At this time, the water and the product concentrate may be simultaneously filled from the water filling nozzle 21a and the concentrate filling nozzle 22c. Although not shown, as described with reference to FIG. 15, one filling nozzle 20a may be used to fill the sterile water and the undiluted product solution. After that, the paper container 203 is cut into a predetermined shape in the molding section 202 to obtain a product containing the contents.

(Twelfth modification)
Further, in the above-described embodiment, the case where the sterilization device that performs hydrogen peroxide sterilization is used as the preform sterilization device and the container sterilization device has been described, but the present invention is not limited to this. For example, a sterilizer that performs hydrogen peroxide sterilization may be either a preform sterilizer or a container sterilizer. In addition, the preform sterilization device and the container sterilization device perform a peracetic acid sterilization method in which the inner and outer surfaces of the bottle are sterilized with a peracetic acid solution (or gas, mist, or a mixture thereof), and then the inner and outer surfaces are rinsed with sterile water. It may be a sterilizer. Alternatively, the preform sterilization device and the container sterilization device use peracetic acid, acetic acid, pernitric acid, nitric acid, sodium hypochlorite, chlorine, caustic soda, etc. alone as a sterilizing agent in addition to hydrogen peroxide and ethanol. It may be a device, or a sterilization device using a combination of two or more of these sterilization agents. Also, the sterilizer may be used not only for sterilizing bottles, but also for sterilizing cups, pouches, paper containers or composites thereof. Further, the preform sterilization device may sterilize the preforms by spraying chemicals, rinsing chemicals, steam, sterile water, sterile air, electron beams, X-rays, or ultraviolet light. Similarly, the container sterilization device may sterilize the container by chemical spray, chemical rinse, steam, sterile water, sterile air, electron beam, X-ray or ultraviolet light.

(13th modification)
Further, in the above-described embodiment, the case where the content filling system 10 includes the bottle molding section 30 has been described, but the present invention is not limited to this. For example, the content filling system may be configured to sequentially receive molded empty bottles 100 from the outside by air transportation or the like, and transport the received bottles 100 toward the sterilization device 11 . Also in this case, the effects described above can be obtained.

(14th modification)
Furthermore, in the above-described embodiment, the content filling system 10 has been described as a system that fills the bottle 100 with content, but the present invention is not limited to this. The content filling system 10 according to the present embodiment can also be applied to a filling system for filling containers such as cups with so-called chilled beverages such as milk beverages. Even in this case, compared to the case of diluting the product stock solution with sterile water prepared using a sterilizer that heats and sterilizes water, the amount of carbon dioxide emitted when preparing the contents can be reduced. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced. Moreover, when the content is a milk drink or the like, the number of bacteria in the product concentrate may increase. In this way, even when the number of bacteria in the product concentrate is increased, the product concentrate is heat sterilized. Therefore, even if the content is a milk drink or the like, the sterility of the content can be sufficiently ensured. Moreover, in the content filling system 10 according to the present embodiment, any liquid that requires sterilization (for example, seasonings, alcoholic beverages, milk beverages, etc.) may be filled into the container.

(Modified Example of Sterilization Method for Content Filling System)
Next, a modified example of the sterilization method for the content filling system will be described.

(First modification)
In the above-described embodiment, the chamber sterilization method includes a COP process (reference S12 in FIG. 9), a CIP process (reference S13 in FIG. 9), a SIP process (reference S14 in FIG. 9), and an SOP process (reference S14 in FIG. 9). 9, reference S15) and S15) have been described, but the present invention is not limited to this. For example, as shown in FIG. 19, in the chamber sterilization method, after the rinsing step (S310 in FIG. 19), the COP step (S320 in FIG. 19) and the CIP step (S330 in FIG. 19) are performed at the same time. It can be done. Also, after the COP process and the CIP process, the SIP process (symbol S340 in FIG. 19) and the SOP process (symbol S350 in FIG. 19) may be performed at the same time. As a result, the downtime can be greatly reduced, and the productivity of the product bottle 101 can be improved.

Further, as shown in FIG. 20, in the chamber sterilization method, after the rinsing step (reference S41 in FIG. 20), a CSOP step (reference S42 in FIG. 20) in which the COP step and the SOP step are performed simultaneously, and a CIP step. A CSIP step (reference S43 in FIG. 20) that is performed simultaneously with the SIP step may be performed at the same time. In this case, for example, during the CSOP process, the cleaning agent having a temperature of 70° C. or higher is preferably sprayed into the intermediate area chamber 70g and the second aseptic chamber 70h for at least 1 minute or longer, and preferably for 5 minutes or longer. more preferably. This purifies and sterilizes the inner wall surface of the intermediate area chamber 70g, etc., and the surface of equipment such as the filling device 20, etc. FIG. Further, for example, during the CSIP process, the flow path of the product undiluted solution in the undiluted solution filling device 22 is rinsed with sterile water, and a cleaning agent having a temperature of 70° C. or higher is supplied to the circulation path (not shown) including the flow path. do. In the circulation path, the cleaning agent is preferably circulated for at least 5 minutes or longer, more preferably 10 minutes or longer. As a result, the flow path of the product concentrate in the concentrate filling device 22 is sterilized. Even in this case, the downtime can be greatly reduced, and the productivity of the product bottle 101 can be improved.

Also in this modification, the number of times of cleaning and sterilizing the inside of the first aseptic chamber 70f can be reduced, and the area to be cleaned and sterilized in the content filling system 10 can be narrowed. In addition, the number of times of cleaning and sterilizing the filling device 20 accommodated inside the first aseptic chamber 70f can be reduced, and the area to be cleaned and sterilized in the content filling system 10 can be narrowed. Therefore, the amount of steam used can be reduced. Moreover, since the area to be cleaned and sterilized can be narrowed, the cleaning time and sterilization time can be shortened. Therefore, the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

When the CSIP process, in which the CIP process and the SIP process are simultaneously performed, is performed, it is necessary to rinse the cleaning agent used after the CSIP process while maintaining the inside of the undiluted solution filling device 22 and the like in an aseptic state. At this time, by using the water sterilized in the water sterilization line 50 for rinsing, the amount of carbon dioxide discharged by the content filling system 10 can be reduced. Further, since the water sterilized by the water sterilization line 50 can be stored in the second water tank 52, the cleaning agent can be rinsed immediately after the CSIP process. Therefore, downtime can be shortened. The flow path from the second water tank 52 to the aseptic area where the CSIP process and the CSOP process are performed is preferably cleaned (CIP) and sterilized (SIP) before rinsing the cleaning agent after the CSIP process. . In this case, for example, a cleaning agent or a disinfectant may be supplied to the second bypass line 56 from a connection point CP1 (see FIGS. 1 and 2A, etc.) that connects the second bypass line 56 to the water disinfection line 50, The channels may be sterilized, such as by steam or hot water.

(Second modification)
In the above-described embodiment, when sterilizing the first sterilizer 62 and the like of the water sterilizer 60, an example of sterilizing the first sterilizer 62 and the like with steam, hot water, or a sterilant was described. It is not limited to this. For example, if the first sterilizer 62 or the like is weak against heat and/or has low chemical resistance, the first sterilizer 62 or the like may be sterilized with sterilized water. In this case, the sterilized water may be water that has been sterilized with ultraviolet light inside the first sterilizer 62 or the like. Then, the control unit 90 circulates the sterilized water in the circulation system 59A (see FIG. 2A etc.) including the water sterilizer 60, thereby gradually reducing the number of bacteria in the circulating water. The sterilizer 62 or the like may be sterilized. At this time, the controller 90 may circulate the sterilized water in the circulation system 59A at least three times or more, preferably ten times or more.

In this modified example, first, the first sterile filter 63 and the second sterile filter 65 are sterilized (SIP) (SIP step, symbol S231 in FIG. 21). In this case, the foreign matter removing filter 61 is also preferably sterilized (SIP) with steam in advance.

Next, water is supplied to the circulation system 59A including the water sterilizer 60 (water supply step, symbol S232 in FIG. 21). At this time, pure water is first conveyed by the pump P1. At this time, pure water adjusted to a predetermined temperature (for example, 25° C.) by a heat exchanger (not shown) is supplied to the first sterile filter 63 and the like. This wets the membranes of the first sterile filter 63 and the like. After that, the pump P1 is stopped.

Next, at least one of the first sterile filter 63 and the second sterile filter 65 is subjected to an integrity test (integrity test step, symbol S233 in FIG. 21). During the integrity test, valves (not shown) near the first sterile filter 63 and the like are closed to supply sterile air to the first sterile filter 63 and the like. Then, the sterile air supplied to the first sterile filter 63 and the like is gradually pressurized, and the bubble point value of the first sterile filter 63 and the like is measured. After that, it is confirmed whether or not the first sterile filter 63 and the like are complete (whether or not sterile air leaks at a predetermined pressure) based on the bubble point values measured a plurality of times (for example, three times). If the integrity test confirms that the first sterile filter 63 and the like are not perfect, the first sterile filter 63 and the like are replaced.

Next, the water is sterilized inside the first sterilizer 62 or the like (water sterilization step, symbol S234 in FIG. 21). At this time, pure water is first conveyed by the pump P1. After the inside of the first sterilizer 62 and the like is filled with water, the water is irradiated with ultraviolet rays by the first ultraviolet lamp 67a and the like. In this case, the irradiation time (sterilization time) for irradiating ultraviolet rays is preferably 10 seconds or more and 30 minutes or less. At this time, the illuminance of the ultraviolet rays emitted from the first ultraviolet lamp 67a or the like may be checked. When the illuminance of the ultraviolet rays emitted from the first ultraviolet lamp 67a or the like is abnormal, the first ultraviolet lamp 67a or the like may be replaced.

Here, the medium-pressure mercury lamp has an operating temperature of approximately 600° C. or higher and 900° C. or lower. Therefore, when the first ultraviolet lamp 67a or the like is a medium-pressure mercury lamp, it is preferable to irradiate the water with ultraviolet rays while conveying the water by the pump P1. Thereby, overheating of the first ultraviolet lamp 67a and the like can be suppressed. At this time, the water irradiated with ultraviolet rays may be stored in the second water tank 52, for example. Alternatively, water irradiated with ultraviolet rays may be circulated within the circulation system 59A. When the UV-irradiated water is circulated in the circulation system 59A, the sterility level of the water can be enhanced.

On the other hand, low-pressure mercury lamps have an operating temperature of approximately 40° to 100°. Therefore, if the first ultraviolet lamp 67a or the like is a low-pressure mercury lamp, water may be irradiated with ultraviolet rays while the pump P1 is stopped.

Next, the sterilized water is circulated in the circulation system 59A including the water sterilizer 60 (water circulation step, symbol S235 in FIG. 21). At this time, the water irradiated with ultraviolet rays passes through the second sterile filter 65 . The pure water that has passed through the second sterile filter 65 is supplied to the first water tank 51 through the circulation line 59 . Thus, the sterilized pure water circulates in the circulation system 59A.

After that, in the circulation system 59A, the sterilized water may be circulated at least once, preferably three times or more. By circulating the pure water three times or more in the circulation system 59A in this manner, the sterilization effect of the first sterilizer 62 and the like by water can be enhanced. At this time, the cumulative irradiation dose of ultraviolet rays to the circulating sterilized water is preferably at least 100 mJ/cm ² or more and 3000 mJ/cm ² or less, and more preferably 1000 mJ/cm ² or more and 3000 mJ/cm ² or less. . By setting the cumulative irradiation amount of ultraviolet rays to circulating water to be 100 mJ/cm ² or more, the sterilization effect of water by ultraviolet rays can be enhanced. Further, by setting the cumulative irradiation amount of ultraviolet rays to 3000 mJ/cm ² or less, the amount of electricity consumption can be reduced, and the amount of carbon dioxide emitted by the content filling system 10 can be reduced.

In this manner, the first sterilizer 62 and the like are sterilized.

Also, the first sterilizer 62 and the like may be sterilized with, for example, a cleaning agent. In this case, the first sterilizer 62 and the like may be sterilized by supplying the cleaning agent only to the first sterilizer 62 and the second sterilizer 64 . The cleaning agent may be, for example, a cleaning agent containing peracetic acid, hydrogen peroxide, an alkaline chemical, an acidic chemical, sodium hypochlorite, or the like. Thereafter, the first sterilizer 62 and the like may be rinsed with aseptic water by supplying aseptic water to the circulation system 59A from the second water tank 52 in which aseptic water is stored in advance.

According to this modification, the controller 90 sterilizes the first sterilizer 62 by circulating sterilized water in the circulation system 59A including the water sterilizer 60 . In this way, by sterilizing the first sterilizer 62 without using steam, hot water, or a heated sterilant, the amount of carbon dioxide emitted by the content filling system 10 can be reduced, and water The cost for sterilizing the sterilizer 60 can be reduced.

Further, according to this modification, water is sterilized by ultraviolet rays inside the first sterilizer 62 . As a result, the amount of carbon dioxide emitted by the content filling system can be reduced compared to the case where water is sterilized by heating it.

It is also possible to appropriately combine a plurality of constituent elements disclosed in the above embodiments and modifications as necessary. Alternatively, some components may be deleted from all the components shown in the above embodiments and modifications.

10 content filling system 11 sterilization device 18 cap sterilization device 20 filling device 20a filling nozzle 21 water filling device 21a water filling nozzle 22 undiluted solution filling device 22a first undiluted solution filling device 22b second undiluted solution filling device 22c undiluted solution filling nozzle 32 blow molding part 34a preform sterilizer 50 water sterilization line 51 first water tank 52 second water tank 55 first bypass line 57 mixing tank 58b snift line 60 water sterilizer 70 concentrate sterilization line 71 first concentrate tank 72 second concentrate tank 75 addition Unit 80 Product Undiluted Solution Sterilizer 88 Cap 90 Control Part 100 Bottle 100a Preform P Packing

Claims (20)

a circulation system including a water sterilizer that sterilizes water without heating;
a water tank provided downstream of the water sterilizer and outside the circulation system;
A control unit that controls the water sterilizer,
The water sterilizer is
a first sterilizer that sterilizes the water;
a first sterile filter provided downstream of the first sterilizer;
and a second sterile filter provided downstream of the first sterile filter,
The first sterilizer sterilizes the water with ultraviolet light,
The contents filling system, wherein the controller circulates the sterilized water in a circulation system when the water tank becomes full while the product bottles are being produced in the contents filling system. The contents filling system according to claim 1 , wherein the water sterilizer sterilizes water having an electric conductivity of 0.1 µS/cm or more and 20 µS/cm or less. 2. The content filling system according to claim 1 , wherein the water sterilizer has an integrated UV irradiation dose to the water of 10 mJ/cm ^<2> or more and 10000 mJ/cm ^{<2> or} less. The water sterilizer continues to sterilize the water without stopping the sterilization of the water while producing product bottles by filling the containers with the contents in the contents filling system. 2. The content filling system according to 1 . The contents filling system according to claim 1 , wherein the second sterile filter has an opening of 0.1 µm or more and 0.45 µm or less. The contents filling system according to claim 1 , wherein the first sterile filter has an opening of 0.1 µm or more and 0.45 µm or less. 2. The content filling system according to claim 1 , wherein said first sterilizer has an ultraviolet irradiation section including a medium-pressure mercury lamp. The water sterilizer further includes a second sterilizer provided between the first sterile filter and the second sterile filter, and a first sterilizer configured by the first sterilizer and the first sterile filter The content filling according to claim 1 , wherein the sterilization set and the second sterilization set configured by the second sterilizer and the second aseptic filter are arranged in series along the water conveying direction. system. At least one of between the first sterilizer and the first sterile filter and between the first sterile filter and the second sterile filter has a sampling point for aseptically sampling water. 2. The content filling system of claim 1 , provided. 2. The contents filling system according to claim 1 , wherein the processing capacity of said water sterilizer is 105% or more of the maximum processing capacity required during production of product bottles. In a sterilization method for sterilizing a content filling system equipped with a water sterilizer that sterilizes water without heat,
supplying hot water to the water sterilizer;
circulating the hot water in a circulation system including the water sterilizer;
and a cooling step of the circulatory system,
The water sterilizer is
a first sterilizer that sterilizes the water;
a first sterile filter provided downstream of the first sterilizer;
A second sterile filter provided downstream of the first sterile filter,
The first sterilizer sterilizes the water with ultraviolet light,
The sterilization method, wherein in the step of circulating the hot water, the circulation of the hot water is performed with the ultraviolet lamp of the first sterilizer turned on. The sterilization method according to claim 11 , wherein the water sterilizer sterilizes water having an electric conductivity of 0.1 µS/cm or more and 20 µS/cm or less. 12. The sterilization method according to claim 11 , wherein the water sterilizer has a cumulative irradiation dose of ultraviolet rays to the water of 10 mJ/cm ^<2> or more and 10000 mJ/cm ^{<2> or} less. The water sterilizer continues to sterilize the water without stopping the sterilization of the water while producing product bottles by filling the containers with the contents in the contents filling system. 12. The sterilization method according to 11 . The sterilization method according to claim 11 , wherein the second sterile filter has an opening of 0.1 µm or more and 0.45 µm or less. The sterilization method according to claim 11 , wherein the first sterile filter has an opening of 0.1 µm or more and 0.45 µm or less. 12. The sterilization method according to claim 11 , wherein said first sterilizer has an ultraviolet irradiation unit including a medium pressure mercury lamp. The water sterilizer further includes a second sterilizer provided between the first sterile filter and the second sterile filter, and a first sterilizer configured by the first sterilizer and the first sterile filter The sterilization method according to claim 11 , wherein the sterilization set and the second sterilization set composed of the second sterilizer and the second sterile filter are arranged in series along the water conveying direction. At least one of between the first sterilizer and the first sterile filter and between the first sterile filter and the second sterile filter has a sampling point for aseptically sampling water. 12. A sterilization method according to claim 11 , wherein a sterilization method is provided. The sterilization method according to claim 11 , wherein the processing capacity of the water sterilizer is 105% or more of the maximum processing capacity required during production of product bottles.

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