WO2019223592A1 - 一种含颗粒液体饮料的配置杀菌设备及配置方法 - Google Patents

一种含颗粒液体饮料的配置杀菌设备及配置方法 Download PDF

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Publication number
WO2019223592A1
WO2019223592A1 PCT/CN2019/087158 CN2019087158W WO2019223592A1 WO 2019223592 A1 WO2019223592 A1 WO 2019223592A1 CN 2019087158 W CN2019087158 W CN 2019087158W WO 2019223592 A1 WO2019223592 A1 WO 2019223592A1
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Prior art keywords
container
heat exchange
liquid
switching valve
pure water
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PCT/CN2019/087158
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English (en)
French (fr)
Inventor
茅嘉惠
杨亚军
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江苏新美星包装机械股份有限公司
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Priority to JP2021515262A priority Critical patent/JP7089116B2/ja
Priority to EP19806578.1A priority patent/EP3811784B1/en
Publication of WO2019223592A1 publication Critical patent/WO2019223592A1/zh

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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/42—Preservation of non-alcoholic beverages
    • A23L2/46—Preservation of non-alcoholic beverages by heating
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385—Concentrates of non-alcoholic beverages
    • A23L2/39—Dry compositions
    • A23L2/395—Dry compositions in a particular shape or form
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/003—Control or safety devices for sterilisation or pasteurisation systems
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/16—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials
    • A23L3/18—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/16—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials
    • A23L3/18—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus
    • A23L3/22—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus with transport through tubes
    • A23L3/225—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus with transport through tubes in solid state
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/02—Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027—Cleaning the internal surfaces; Removal of blockages
    • B08B9/032—Cleaning the internal surfaces; Removal of blockages by the mechanical action of a moving fluid, e.g. by flushing
    • B08B9/0321—Cleaning the internal surfaces; Removal of blockages by the mechanical action of a moving fluid, e.g. by flushing using pressurised, pulsating or purging fluid
    • B08B9/0325—Control mechanisms therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/53—Mixing liquids with solids using driven stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/59—Mixing systems, i.e. flow charts or diagrams

Definitions

  • the invention relates to a sterilization device and a method for disposing a liquid beverage containing particles.
  • the purpose of the present invention is to provide a sterilizing device and a method for disposing a liquid beverage containing particles, which can reduce the cost of disposing the liquid beverage containing particles. It can effectively ensure the complete sterilization of the particles.
  • pure water is used.
  • the pure water in the container directly replaces the liquid beverage containing granules in the system.
  • the liquid beverage containing granules in the system is pushed into the storage container for temporary storage.
  • the pure water is used instead of the liquid beverage containing granules to circulate and sterilize to ensure the system's aseptic environment.
  • the problem of breakage caused by excessive repeated sterilization of liquid beverages containing particles is avoided.
  • a configuration sterilization device for a liquid beverage containing particles includes a storage container, a dosing mechanism in communication with the storage container, a pure water container, and a discharge pipeline communicating with the storage container and the pure water container, respectively,
  • the first switching valve is used to communicate the pure water container and the feeding end or to communicate the storage container and the feeding end;
  • the second switching valve is used to communicate the discharge end and the pure water container or to communicate the discharge end and the storage container;
  • the dosing mechanism includes a dosing container connected to the storage container, a liquid inlet pipeline connected to the dosing container, a flow meter provided on the liquid inlet pipeline, and a inlet connected to the dosing container.
  • a particle pipeline and a liquid level sensor provided in the batching container; the liquid level sensor is used to determine whether the particles entering the batching container raise the liquid level in the batching container to a set height.
  • the first switching valve has a first communication state and a second communication state, and when the first switching valve is switched to the first communication state, the pure water container communicates with the feed end, so The storage container is disconnected from the feeding end; when the first switching valve is switched to the second communication state, the pure water container is disconnected from the feeding end, and the storage container is disconnected from the feeding end The feed end is connected;
  • the second switching valve has a third communication state and a fourth communication state: when the second switching valve is switched to the third communication state, the discharge end is in communication with the pure water container, and the discharge When the second switching valve is switched to the fourth communication state, the discharge end is in communication with the storage container, and the discharge end is in communication with the pure water container disconnect.
  • the temperature increasing mechanism includes a preheating heat exchange tube and a preheating heat insulation tube which are sequentially connected;
  • the sterilization mechanism includes a sterilization heat exchange tube and a sterilization heat preservation tube which are connected in sequence;
  • the temperature reducing mechanism includes a temperature reduction heat exchanger which is connected in sequence Tube and outlet cooling heat exchange tube.
  • the device further includes a heat exchange mechanism, and the heat exchange mechanism includes a hot water container, a hot water outlet pipe and a steam heat exchange pipe connected to the hot water container, and the hot water outlet pipe is in this order.
  • the heat exchange mechanism includes a hot water container, a hot water outlet pipe and a steam heat exchange pipe connected to the hot water container, and the hot water outlet pipe is in this order.
  • the heat exchange mechanism further includes a first temperature sensor provided at an outlet end of the sterilization heat exchange tube, a first controller for controlling a flow rate of steam entering the steam heat exchange tube, and the first A temperature sensor is configured to send a first temperature signal to the first controller, and the first controller is configured to control a flow rate of the steam according to the first temperature signal.
  • the heat exchange mechanism further includes a second temperature sensor provided at an outlet end of the preheating and heat preservation pipe, and a second controller for controlling a flow of hot water entering the hot water container, wherein A second temperature sensor is configured to send a second temperature signal to the second controller, and the second controller is configured to control a flow rate of the hot water according to the second temperature signal.
  • the heat exchange mechanism further includes a cooling water pipeline that performs heat exchange with the outlet cooling heat exchange pipe.
  • a drain valve is provided between the second switching valve and the pure water container, and a recovery valve is connected to the drain valve.
  • a water top valve is provided between the first switching valve and the pure water container.
  • a method for disposing a liquid beverage containing particles In a batching container, a liquid level when a liquid medium reaches a set volume is defined as a set liquid level. A liquid is first introduced into the batching container. The volume ratio of liquid to particles in the liquid beverage and the set volume are calculated, and the amount of liquid passed into the ingredient container is measured by a flow meter, and then the particles are passed into the ingredient container until the The liquid level in the dosing container rises to the set liquid level.
  • the present invention provides a sterilizing device and a method for disposing a liquid beverage containing particles, which reduces the cost of disposing the liquid beverage containing particles; and can effectively guarantee the particles Thorough sterilization; when there is a problem with the back-end filling equipment, the pure water in the pure water container is used to directly replace the liquid beverage containing particles in the system, and the liquid beverage containing particles in the system is pushed into the storage container for temporary storage, using pure Water replaces the sterilization of liquid beverages containing particles to ensure the system's sterile environment while avoiding the problem of breakage caused by excessive repeated sterilization of liquid beverages with particles.
  • Figure 1 is a schematic diagram of the device of the present invention.
  • the above-mentioned sterilizing device for a liquid beverage containing particles includes a storage container 1 and a batching mechanism that is in communication with the storage container 1.
  • the batching mechanism includes a batching container 6 communicating with the storage container 1, a liquid inlet pipe 7 connected to the batching container 6, a flow meter 8 provided on the liquid inlet pipe 7, and a particle feeding tube connected to the batching container 6.
  • Road 9 A liquid level sensor 10 provided in the ingredient container 6; the liquid level sensor 10 is used to determine whether particles entering the ingredient container 6 have raised the liquid level in the ingredient container 6 to a set height.
  • the liquid level when the liquid medium reaches 100 L is defined in the ingredient container 6 as the set liquid level.
  • the volume ratio of the particles to the liquid is 3: 7.
  • 70 L of liquid is passed into the batching container 6, and the amount of the liquid in the batching container 6 is measured by the flow meter 8.
  • particles are poured into the batching container 6, until the liquid level in the batching container 6 rises to the set liquid. Bit.
  • the passage of particles is stopped.
  • the above-mentioned sterilizing equipment for a liquid beverage containing particles further includes a pure water container 2 and a discharge pipe 3 communicating with the storage container 1 and the pure water container 2, respectively.
  • the medium in the discharge pipe 3 flows into the heating mechanism and sterilizes in sequence. Mechanism, cooling mechanism, and finally flow into the filling equipment 29 or return to the storage container 1 or return to the pure water container 2.
  • the discharging pipe 3 includes a feeding end, a discharging end, a first switching valve 4 provided at the feeding end, and a second switching valve 5 provided at the discharging end.
  • the first switching valve 4 is used to communicate the pure water container 2 with the feeding end or is used to communicate the storage container 1 and the feeding end;
  • the second switching valve 5 is used to communicate the discharge end and the pure water container 2 or is used for Connect the discharge end to the storage container 1.
  • a drain valve 25 is provided between the second switching valve 5 and the pure water container 2, and a recovery valve 26 is connected to the drain valve 25; a water ceiling is provided between the first switching valve 4 and the pure water container 2. Valve 27.
  • the first switching valve 4 has a first communication state and a second communication state.
  • the pure water container 2 communicates with the feeding end, and the storage container 1 communicates with The feeding end is disconnected;
  • the first switching valve 4 is switched to the second communicating state, the pure water container 2 is disconnected from the feeding end, and the storage container 1 is communicating with the feeding end;
  • the second switching valve 5 has a third communicating state And the fourth communication state: when the second switching valve 5 is switched to the third communication state, the discharge end is connected to the pure water container 2 and the discharge end is disconnected from the storage container 1; the second switching valve 5 is switched to the fourth communication In the state, the discharge end is communicated with the storage container 1 and the discharge end is disconnected from the pure water container 2.
  • the A switching valve 4 maintains the second communication state, and the second switching valve 5 switches to the fourth communication state.
  • the water top valve 27 is opened first, and then the first switching is performed.
  • the valve 4 is switched to the first communication state, and the second switching valve 5 is maintained to the fourth communication state.
  • the granular liquid beverage in the system is pushed into the storage container 1 by pure water, and then the second switching valve 5 is switched to the third communication state.
  • Water into the water vessel 2, the water circulating in the system, the rear end of the residual material diluted discharged through the discharge valve 25 is performed, formulations may be recycled through the recovery valve 26.
  • the material top water and water top material discharge processes before and after production are very common, but during the material top process, it must be ensured that the material in the storage container 1 cannot be completely sucked by the rear-end conveying pump 28, otherwise it will Risks such as destruction of the UHT sterile environment caused by pump evacuation.
  • Generally experienced commissioning engineers will set a minimum protective liquid level for storage container 1. Once the protective liquid level is lowered, the top-liquid process will start, but the protective liquid level set in storage container 1 often becomes a product mix. Loss part.
  • the materials in the system can be jacked back to the storage container 1 through pure water, thereby avoiding the waste of materials.
  • the heating mechanism includes a preheating heat exchange tube 11 and a preheating insulation pipe 12 connected in sequence; the sterilization mechanism includes a sterilization heat exchange tube 13 and a sterilization insulation pipe 14 connected in sequence; the cooling mechanism includes a cooling heat exchange tube 15 and outlet cooling in order.
  • Heat exchange tube 16 The discharge pipe 3 passes through the preheating heat exchange pipe 11, the preheating heat preservation pipe 12, the sterilization heat exchange pipe 13, the sterilization heat preservation pipe 14, the cooling heat exchange pipe 15, and the outlet cooling heat exchange pipe 16 in this order.
  • the main problem of sterilizing liquid beverage products containing particles is that the core temperature of the particles cannot meet the corresponding sterilization requirements.
  • the present invention adopts a stepwise heating method, and sets different preheating heat exchange tubes 11 for preheating according to product characteristics, such as 110 °C, the product enters the preheating insulation tube 12 after reaching this temperature, and the inlet and outlet temperature of the preheating insulation tube 12 is detected after a specific time of insulation, such as 10s, 20s, 30s, and the insulation time is determined according to the heat transfer characteristics of the product.
  • the temperature deviation value is used to adjust the temperature of the system, and then the product enters the subsequent sterilization heat exchange tube 13 and sterilization heat insulation tube 14 for final temperature control sterilization. This can effectively ensure that the center temperature of the product particles reaches the sterilization requirements and make the sterilization more thorough.
  • the above-mentioned sterilization equipment for the liquid beverage containing particles further includes a heat exchange mechanism.
  • the heat exchange mechanism includes a hot water container 17, a hot water outlet pipe 18 communicating with the hot water container 17, a steam heat exchange pipe 19, and a hot water outlet pipe.
  • the path 18 passes through the cooling heat exchange tube 15, the steam heat exchange tube 19, and the sterilization heat exchange tube 13 in this order, and then passes through the preheating heat exchange tube 11 and enters the hot water container 17 in two ways.
  • the low-temperature hot water in the hot water outlet pipe 18 first exchanges heat with the products of the cooling heat exchange pipe 15 to heat up, and then exchanges heat with the steam in the steam heat exchange pipe 19 to heat up, and then exchanges heat with the sterilization heat exchange pipe 13
  • the product exchanges heat to cool down, and then divides into two paths. One way exchanges heat with the product in the preheating heat exchange tube 11 to cool down, and the other way directly enters the hot water container 17. With this structure, the thermal energy of the product in the cooling heat exchange tube 15 can be recovered.
  • the heat exchange mechanism further includes a first temperature sensor 20 provided at the outlet end of the sterilization heat exchange tube 13, a first controller 21 for controlling the flow rate of steam entering the steam heat exchange tube 19, and a first temperature sensor 20 is used to send a first temperature signal to the first controller 21, and the first controller 21 is used to control the flow of steam according to the first temperature signal.
  • the first controller 21 controls the steam flow to increase; when the real-time temperature fed back by the first temperature signal is greater than the set temperature, the first controller 21 controls the steam flow. The flow is reduced.
  • the heat exchange mechanism further includes a second temperature sensor 22 provided at the outlet end of the pre-heating insulation pipe 12, a second controller 23 for controlling the flow of hot water into the hot water tank 17, and the second temperature
  • the sensor 22 is configured to send a second temperature signal to the second controller 23, and the second controller 23 is configured to control a flow of hot water according to the second temperature signal.
  • the second controller 23 controls the flow of the hot water directly into the hot water tank 17 to decrease, so that the hot water that exchanges heat with the product in the preheating heat exchange tube 11
  • the second controller 23 controls the flow of hot water directly into the hot water tank 17 to increase, so that the product in the preheated heat exchange tube 11 is heated. The flow of hot water for heat exchange decreases.
  • the heat exchange mechanism also includes a cooling water pipe 24 that performs heat exchange with the outlet cooling heat exchange pipe 16. Through this setting, the product is finally cooled and sent to the filling equipment 29. At the same time, the heat in the product is further exchanged, so that Heat is recycled.

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  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Mechanical Engineering (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Devices For Dispensing Beverages (AREA)
  • Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)

Abstract

一种含颗粒液体饮料的配置杀菌设备及配置方法，包括储料容器、配料机构、纯水容器、出料管路，出料管路包括设于进料端处的第一切换阀和设于出料端处的第二切换阀；第一切换阀用于连通纯水容器与进料端或用于连通储料容器与进料端；第二切换阀用于连通出料端与纯水容器或用于连通出料端与储料容器；配料机构包括与储料容器连通的配料容器、进液体管路、设于进液体管路上的流量计、进颗粒管路、液位传感器；液位传感器用于判断进入配料容器中的颗粒是否将配料容器中的液面上升至设定高度。

Description

一种含颗粒液体饮料的配置杀菌设备及配置方法 技术领域
本发明涉及一种含颗粒液体饮料的配置杀菌设备及配置方法。
背景技术
目前国内以及东南亚市场含颗粒的饮品开始兴起，例如含有椰果颗粒的椰奶饮品、含有果肉粒的果汁饮品、含有谷物颗粒的谷物饮品，这些含有颗粒的液体类产品营养丰富，越来越受到消费者的青睐。
但是含颗粒液体饮料在配置过程中，需要用到昂贵的颗粒流量计，生产成本较高。同时，颗粒在杀菌过程中，由于颗粒的中心温度难以达标，无法保证颗粒的杀菌彻底。最后，当后端灌装设备出现问题时，由于UHT不能停机等候，一旦停机系统就要重新进行CIP/SIP工艺，大大提高生产成本和时间，为了保证设备中的无菌环境，含颗粒饮料需要在设备中循环杀菌，在杀菌过程中，由于颗粒易破损的特殊性，颗粒产品过度重复杀菌会引起颗粒产品的破损，大大降低饮品的口感。
发明内容
本发明的目的是提供一种含颗粒液体饮料的配置杀菌设备及配置方法，降低了含颗粒液体饮料的配置成本；能够有效的保证颗粒杀菌彻底；后端灌装设备出现问题时，用纯水容器中的纯水直接置换系统中的含颗粒液体饮料，同时将系统中的含颗粒液体饮料顶入储料容器中暂存，利用纯水代替含颗粒液体饮料循环杀菌，保证系统无菌环境的同时避免了含颗粒液体饮料由于过度重复杀菌引起的破损问题。
为达到上述目的，本发明采用的技术方案是：
一种含颗粒液体饮料的配置杀菌设备，包括储料容器、与所述储料容器连通的配料机构、纯水容器、分别与所述储料容器和所述纯水容器连通出料管路、连通在所述出料管路上的升温机构、杀菌机构、降温机构，所述出料管路中的介质依次流入所述升温机构、所述杀菌机构、所述降温机构，最后流入灌装设备或回流至所述储料容器或回流至所述纯水容器，所述出料管路包括设于进料端处的第一切换阀和设于出料端处的第二切换阀；
所述第一切换阀，用于连通所述纯水容器与所述进料端或用于连通所述储料容器与所述进料端；
所述第二切换阀，用于连通所述出料端与所述纯水容器或用于连通所述出料端与所述储料容器；
所述配料机构包括与所述储料容器连通的配料容器、连通在所述配料容器上的进液体管路、设于所述进液体管路上的流量计、连通在所述配料容器上的进颗粒管路、设于所述配料容器中的液位传感器；所述液位传感器，用于判断进入所述配料容器中的颗粒是否将所述配料容器中的液面上升至设定高度。
优选地，所述第一切换阀具有第一连通状态和第二连通状态，所述第一切换阀切换为所述第一连通状态时，所述纯水容器与所述进料端连通，所述储料容器与所述进料端断开；所述第一切换阀切换为所述第二连通状态时，所述纯水容器与所述进料端断开，所述储料容器与所述进料端连通；
所述第二切换阀具有第三连通状态和第四连通状态：所述第二切换阀切换为所述第三连通状态时，所述出料端与所述纯水容器连通，所述出料端与所述储料容器断开；所述第二切换阀切换为所述第四连通状态时，所述出料端与所述储料容器连通，所述出料端与所述纯水容器断开。
优选地，所述升温机构包括依次连通的预热换热管和预热保温管；所述杀菌机构包括依次连通的杀菌换热管和杀菌保温管；所述降温机构包括依次连通的降温换热管和出口冷却换热管。
更优选地，所述设备还包括换热机构，所述换热机构包括热水容器、与所述热水容器连通的出热水管路、蒸汽换热管，所述出热水管路依次经过所述降温换热管、所述蒸汽换热管、所述杀菌换热管，之后分两路分别经过所述预热换热管和进入所述热水容器中。
更进一步优选地，所述换热机构还包括设于所述杀菌换热管的出口端的第一温度传感器、用于控制进入所述蒸汽换热管的蒸汽流量的第一控制器，所述第一温度传感器，用于发送第一温度信号给所述第一控制器，所述第一控制器，用于根据所述第一温度信号控制所述蒸汽的流量。
更进一步优选地，所述换热机构还包括设于所述预热保温管的出口端的第二温度传感器、用于控制进入所述热水容器中的热水流量的第二控制器，所述第二温度传感器，用于发送第二温度信号给所述第二控制器，所述第二控制器，用于根据所述第二温度信号控制所述热水的流量。
更进一步优选地，所述换热机构还包括与所述出口冷却换热管进行换热的冷却水管路。
优选地，所述第二切换阀和所述纯水容器之间设有排放阀，所述排放阀上连通有回收阀。
优选地，所述第一切换阀和所述纯水容器之间设有水顶阀。
一种含颗粒液体饮料的配置方法，在配料容器中，定义液体介质达到设定体积时的液位为设定液位，首先向所述配料容器中通入液体，通入的液体体积根据颗粒液体饮料中液体与颗粒的体积配比以及所述设定体积计算得出，通过流量计计量通入所述配料容器中的液体的量，接着向所述配料容器中通入颗粒，直至所述配料容器中的液位上升至所述设定液位。
由于上述技术方案的运用，本发明与现有技术相比具有下列优点： 本发明一种含颗粒液体饮料的配置杀菌设备及配置方法，降低了含颗粒液体饮料的配置成本；能够有效的保证颗粒杀菌彻底；后端灌装设备出现问题时，用纯水容器中的纯水直接置换系统中的含颗粒液体饮料，同时将系统中的含颗粒液体饮料顶入储料容器中暂存，利用纯水代替含颗粒液体饮料循环杀菌，保证系统无菌环境的同时避免了含颗粒液体饮料由于过度重复杀菌引起的破损问题。
附图说明
附图1为本发明装置的结构示意图。
其中：1、储料容器；2、纯水容器；3、出料管路；4、第一切换阀；5、第二切换阀；6、配料容器；7、进液体管路；8、流量计；9、进颗粒管路；10、液位传感器；11、预热换热管；12、预热保温管；13、杀菌换热管；14、杀菌保温管；15、降温换热管；16、出口冷却换热管；17、热水容器；18、出热水管路；19、蒸汽换热管；20、第一温度传感器；21、第一控制器；22、第二温度传感器；23、第二控制器；24、冷却水管路；25、排放阀；26、回收阀；27、水顶阀；28、输送泵；29、灌装设备。
具体实施方式
下面结合附图来对本发明的技术方案作进一步的阐述。
参见图1所示，上述一种含颗粒液体饮料的配置杀菌设备，包括储料容器1、与储料容器1连通的配料机构。配料机构包括与储料容器1连通的配料容器6、连通在配料容器6上的进液体管路7、设于进液体管路7上的流量计8、连通在配料容器6上的进颗粒管路9、设于配料容器6中的液位传感器10；液位传感器10用于判断进入配料容器6中的颗粒是否将配料容器6中的液面上升至设定高度。
在本实施例中，在配料容器6中定义液体介质达到100L时的液位为设定液位，在需要配置的含颗粒液体饮料中，颗粒与液体的体积比为3:7。首先向配料容器6中通入70L液体，通过流量计8计量通 入配料容器6中的液体的量，接着向配料容器6中通入颗粒，直至配料容器6中的液位上升至设定液位。收到液位传感器10反馈的液位信号后，停止颗粒的通入。这种通过体积比例配合液位的配置方法，操作简单容易控制，能省去常规颗粒设备在线添加时，所用到的较为昂贵的颗粒流量计8，降低含颗粒液体饮料的配置成本；同时这种配置方法可以实现不同浓度颗粒产品的任意配置。
上述一种含颗粒液体饮料的配置杀菌设备还包括纯水容器2、分别与储料容器1和纯水容器2连通出料管路3，出料管路3中的介质依次流入升温机构、杀菌机构、降温机构，最后流入灌装设备29或回流至储料容器1或回流至纯水容器2。出料管路3包括进料端、出料端、设于进料端处的第一切换阀4、设于出料端处的第二切换阀5。第一切换阀4，用于连通纯水容器2与进料端或用于连通储料容器1与进料端；第二切换阀5，用于连通出料端与纯水容器2或用于连通出料端与储料容器1。
在本实施例中，第二切换阀5和纯水容器2之间设有排放阀25，排放阀25上连通有回收阀26；第一切换阀4和纯水容器2之间设有水顶阀27。
在本实施例中，第一切换阀4具有第一连通状态和第二连通状态，第一切换阀4切换为第一连通状态时，纯水容器2与进料端连通，储料容器1与进料端断开；第一切换阀4切换为第二连通状态时，纯水容器2与进料端断开，储料容器1与进料端连通；第二切换阀5具有第三连通状态和第四连通状态：第二切换阀5切换为第三连通状态时，出料端与纯水容器2连通，出料端与储料容器1断开；第二切换阀5切换为第四连通状态时，出料端与储料容器1连通，出料端与纯水容器2断开。
通过这个设置，系统未灌装时，纯水在系统中循环，使系统保持无菌状态，此时，水顶阀27打开，第一切换阀4切换为第一连通状态，第二切换阀5切换为第三连通状态；系统灌装时，纯水不进入系统中，含颗粒液体饮料进入系统中，此时，水顶阀27关闭，第一切 换阀4切换为第二连通状态，含颗粒液体饮料进入灌装设备29中；后端灌装设备29出现故障时，需要使系统中的含颗粒液体饮料回流至储料容器1中，含颗粒液体饮料在系统中循环杀菌，此时，第一切换阀4保持第二连通状态，第二切换阀5切换为第四连通状态；当系统中的含颗粒液体饮料的循环杀菌时间达到上限时，先打开水顶阀27，再将第一切换阀4切换为第一连通状态，第二切换阀5保持第四连通状态，通过纯水将系统中的含颗粒液体饮料顶入储料容器1中，接着第二切换阀5切换为第三连通状态，使纯水进入纯水容器2中，纯水在系统中循环，后端稀释残料通过排放阀25进行排放，也可以通过回收阀26进行回收再调配。
在UHT生产工艺中，生产前后的料顶水和水顶料排放工艺非常常见，但在顶料过程中，要保证储料容器1中的物料不能全部被后端的输送泵28吸走，否则会引起泵抽空导致UHT无菌环境破坏等风险出现。一般有经验的调试工程师会将储料容器1设置一个最低保护液位，一旦低于此保护液位才开始顶液工艺，但往往在储料容器1中设置的保护液位又成了产品混合损耗的一部分。通过上述结构的设置，在水顶料环节中，能够将系统中的物料通过纯水顶回储料容器1中，避免了物料的浪费。
升温机构包括依次连通的预热换热管11和预热保温管12；杀菌机构包括依次连通的杀菌换热管13和杀菌保温管14；降温机构包括依次连通的降温换热管15和出口冷却换热管16。出料管路3依次经过预热换热管11、预热保温管12、杀菌换热管13、杀菌保温管14、降温换热管15、出口冷却换热管16。含颗粒液体饮料产品灭菌的主要问题是颗粒中心温度不能达到相应的灭菌要求，本发明采用分梯段式升温方式，根据产品特性设置不同的预热换热管11进行预升温，例如110℃，产品达到此温度后进入预热保温管12，保温特定时间后检测预热保温管12的进出口温度，例如10s、20s、30s，保温时间等根据产品传热特性决定，校验进出口温度偏差值进行系统调温，然后产品再进入后续杀菌换热管13和杀菌保温管14进行最终控温杀菌， 这样能有效保证产品颗粒中心温度达到灭菌要求，使灭菌更为彻底。
上述一种含颗粒液体饮料的配置杀菌设备还包括换热机构，换热机构包括热水容器17、与热水容器17连通的出热水管路18、蒸汽换热管19，出热水管路18依次经过降温换热管15、蒸汽换热管19、杀菌换热管13，之后分两路分别经过预热换热管11和进入热水容器17中。通过这个设置，出热水管路18中的低温热水先与降温换热管15的产品交换热量升温，再与蒸汽换热管19中的蒸汽交换热量升温，接着与杀菌换热管13中的产品交换热量降温，之后分两路，一路与预热换热管11中的产品交换热量降温，另一路则直接进入热水容器17中。通过这个结构能够回收降温换热管15中的产品的热能。
在本实施例中，换热机构还包括设于杀菌换热管13的出口端的第一温度传感器20、用于控制进入蒸汽换热管19的蒸汽流量的第一控制器21，第一温度传感器20用于发送第一温度信号给第一控制器21，第一控制器21用于根据第一温度信号控制蒸汽的流量。当第一温度信号反馈的实时温度小于设定温度时，第一控制器21控制蒸汽的流量加大；当第一温度信号反馈的实时温度大于设定温度时，第一控制器21控制蒸汽的流量减小。
在本实施例中，换热机构还包括设于预热保温管12的出口端的第二温度传感器22、用于控制进入热水容器17中的热水流量的第二控制器23，第二温度传感器22用于发送第二温度信号给第二控制器23，第二控制器23用于根据第二温度信号控制热水的流量。当第二温度信号反馈的实时温度小于设定温度时，第二控制器23控制直接进入热水容器17中热水的流量减小，使得与预热换热管11中产品交换热量的热水的流量加大；当第二温度信号反馈的实时温度大于设定温度时，第二控制器23控制直接进入热水容器17中热水的流量加大，使得与预热换热管11中产品交换热量的热水的流量减小。
换热机构还包括与出口冷却换热管16进行换热的冷却水管路24，通过这个设置，对产品进行最终降温后送入灌装设备29中，同时还进一步交换了产品中的热量，使热量得到回收利用。
上述实施例只为说明本发明的技术构思及特点，其目的在于让熟悉此项技术的人士能够了解本发明的内容并加以实施，并不能以此限制本发明的保护范围，凡根据本发明精神实质所作的等效变化或修饰，都应涵盖在本发明的保护范围内。

Claims (10)

  1. 一种含颗粒液体饮料的配置杀菌设备，其特征在于：包括储料容器、与所述储料容器连通的配料机构、纯水容器、分别与所述储料容器和所述纯水容器连通出料管路、连通在所述出料管路上的升温机构、杀菌机构、降温机构，所述出料管路中的介质依次流入所述升温机构、所述杀菌机构、所述降温机构，最后流入灌装设备或回流至所述储料容器或回流至所述纯水容器，所述出料管路包括设于进料端处的第一切换阀和设于出料端处的第二切换阀；
    所述第一切换阀，用于连通所述纯水容器与所述进料端或用于连通所述储料容器与所述进料端；
    所述第二切换阀，用于连通所述出料端与所述纯水容器或用于连通所述出料端与所述储料容器；
    所述配料机构包括与所述储料容器连通的配料容器、连通在所述配料容器上的进液体管路、设于所述进液体管路上的流量计、连通在所述配料容器上的进颗粒管路、设于所述配料容器中的液位传感器；所述液位传感器，用于判断进入所述配料容器中的颗粒是否将所述配料容器中的液面上升至设定高度。
  2. 根据权利要求1所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述第一切换阀具有第一连通状态和第二连通状态，所述第一切换阀切换为所述第一连通状态时，所述纯水容器与所述进料端连通，所述储料容器与所述进料端断开；所述第一切换阀切换为所述第二连通状态时，所述纯水容器与所述进料端断开，所述储料容器与所述进料端连通；
    所述第二切换阀具有第三连通状态和第四连通状态：所述第二切换阀切换为所述第三连通状态时，所述出料端与所述纯水容器连通，所述出料端与所述储料容器断开；所述第二切换阀切换为所述第四连通状态时，所述出料端与所述储料容器连通，所述出料端与所述纯水容器断开。
  3. 根据权利要求1所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述升温机构包括依次连通的预热换热管和预热保温管；所述杀菌机构包括依次连通的杀菌换热管和杀菌保温管；所述降温机构包括依次连通的降温换热管和出口冷却换热管。
  4. 根据权利要求3所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述设备还包括换热机构，所述换热机构包括热水容器、与所述热水容器连通的出热水管路、蒸汽换热管，所述出热水管路依次经过所述降温换热管、所述蒸汽换热管、所述杀菌换热管，之后分两路分别经过所述预热换热管和进入所述热水容器中。
  5. 根据权利要求4所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述换热机构还包括设于所述杀菌换热管的出口端的第一温度传感器、用于控制进入所述蒸汽换热管的蒸汽流量的第一控制器，所述第一温度传感器，用于发送第一温度信号给所述第一控制器，所述第一控制器，用于根据所述第一温度信号控制所述蒸汽的流量。
  6. 根据权利要求4所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述换热机构还包括设于所述预热保温管的出口端的第二温度传感器、用于控制进入所述热水容器中的热水流量的第二控制器，所述第二温度传感器，用于发送第二温度信号给所述第二控制器，所述第二控制器，用于根据所述第二温度信号控制所述热水的流量。
  7. 根据权利要求4所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述换热机构还包括与所述出口冷却换热管进行换热的冷却水管路。
  8. 根据权利要求1所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述第二切换阀和所述纯水容器之间设有排放阀，所述排放阀上连通有回收阀。
  9. 根据权利要求1所述的一种含颗粒液体饮料的配置杀菌设备，其特征在于：所述第一切换阀和所述纯水容器之间设有水顶阀。
  10. 一种含颗粒液体饮料的配置方法，其特征在于：在配料容器中，定义液体介质达到设定体积时的液位为设定液位，首先向所述配 料容器中通入液体，通入的液体体积根据颗粒液体饮料中液体与颗粒的体积配比以及所述设定体积计算得出，通过流量计计量通入所述配料容器中的液体的量，接着向所述配料容器中通入颗粒，直至所述配料容器中的液位上升至所述设定液位。
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