CN214903580U

CN214903580U - A instantaneous sterilizer of high temperature for beverage production

Info

Publication number: CN214903580U
Application number: CN202120992928.8U
Authority: CN
Inventors: 孙丽燕; 荀超; 何静宇
Original assignee: Jinan Daofeng Food Co ltd
Current assignee: Jinan Daofeng Food Co ltd
Priority date: 2021-05-10
Filing date: 2021-05-10
Publication date: 2021-11-30
Anticipated expiration: 2031-05-10

Abstract

The application relates to the technical field of beverage production, and discloses a high-temperature instant sterilizer for beverage production, which comprises a preheating mechanism, an ultra-high temperature sterilization mechanism and a shunting mechanism communicated with a homogenizer, wherein the shunting mechanism is communicated between the preheating mechanism and the ultra-high temperature sterilization mechanism. This application has the effect that improves drink machining efficiency.

Description

A instantaneous sterilizer of high temperature for beverage production

Technical Field

The application relates to the field of beverage production, in particular to a high-temperature instantaneous sterilizer for beverage production.

Background

The ultrahigh-temperature instant sterilization is a sterilization process that the heating temperature is set to be 135-150 ℃, the heating time is 2-8s, and the heated product meets the commercial sterile requirement. The basic principles of the method comprise a microbial thermal death principle and a principle of how to keep the original flavor and quality of the food to the maximum extent. Because the sensitivity of the microorganisms to high temperature is far greater than that of most food components, the ultrahigh-temperature short-time sterilization can effectively kill the microorganisms in a short time and better maintain the original quality of the food.

At present, the chinese patent application with publication number CN102907495A discloses a processing technology of a compound beverage, which comprises the following steps: preparing jujube juice, pretreating nucleolus, processing fresh milk, preparing sugar solution, blending, preheating, homogenizing, degassing, sterilizing at ultrahigh temperature, filling and sealing.

In view of the above related technologies, the inventor believes that in the process of beverage production and processing, some beverages need to be preheated before entering a homogenizer for homogenization, and the materials also need to be preheated before ultra-high temperature sterilization, which has the defect of low efficiency in the process of beverage processing.

SUMMERY OF THE UTILITY MODEL

In order to alleviate the problem that machining efficiency is low in the beverage production process, the application provides a high temperature instant sterilizer for beverage production.

The application provides a high temperature instant sterilization machine for beverage production adopts following technical scheme:

the utility model provides a high temperature instantaneous sterilization machine for beverage production, includes preheating mechanism, ultra-high temperature sterilization mechanism and is used for the reposition of redundant personnel mechanism with the isotropic symmetry intercommunication, reposition of redundant personnel mechanism intercommunication is preheating between the mechanism and the ultra-high temperature sterilization mechanism.

Through adopting above-mentioned technical scheme, setting up reposition of redundant personnel mechanism between preheating mechanism and pasteurization mechanism, when the drink that produces need preheat before the homogeneity, utilize reposition of redundant personnel mechanism will preheat the feed inlet intercommunication of mechanism and isotropic symmetry, utilize the discharge gate intercommunication of reposition of redundant personnel mechanism with pasteurization mechanism and isotropic symmetry, the drink advances to preheat the mechanism and preheats before getting into the isotropic symmetry, directly gets into pasteurization mechanism after the homogeneity is accomplished and sterilizes, improves the machining efficiency of drink.

Optionally, the reposition of redundant personnel mechanism includes communicating pipe, flow divider, is used for the drain pipe with the isotropic symmetry feed end intercommunication, is used for feed liquor pipe and two ooff valves with the isotropic symmetry discharge end intercommunication, communicating pipe one end with preheat the mechanism intercommunication, the communicating pipe other end and pasteurization mechanism intercommunication, the flow divider sets up on communicating pipe, flow divider and communicating pipe intercommunication, drain pipe and communicating pipe intercommunication, the drain pipe is located the flow divider and preheats between the mechanism, feed liquor pipe and communicating pipe intercommunication, the feed liquor pipe is located between flow divider and the pasteurization mechanism, one of them ooff valve and feed liquor pipe intercommunication, another ooff valve and drain pipe intercommunication.

By adopting the technical scheme, the preheating mechanism is communicated with the ultra-high temperature sterilization mechanism by utilizing the communicating pipe, the communicating pipe is provided with the flow dividing valve, the communicating pipe is communicated with the feeding end of the homogenizer through the liquid outlet pipe, and the communicating pipe is communicated with the discharging end of the homogenizer through the liquid inlet pipe; when needs carry the homogeneity to the material that preheats in getting into the isotropic symmetry, close the flow divider, open two ooff valves, make the material that preheats carry and carry out the homogeneity in getting into the isotropic symmetry, get into after the homogeneity is accomplished and get into the super pasteurization mechanism through the discharging pipe and disinfect, the flow divider constructs and uses conveniently.

Optionally, the preheating mechanism includes a preheating box and a first feeding pipe, the first feeding pipe is located in the preheating box, the first feeding pipe is fixedly connected with the preheating box, one end of the first feeding pipe is communicated with the communicating pipe, the other end of the first feeding pipe is communicated with the outside of the preheating box, and a first liquid inlet and a first liquid outlet are formed in the preheating box.

Through adopting above-mentioned technical scheme, utilize first conveying pipe to carry the material, heating water gets into the preheating cabinet through first inlet, utilizes heating water to heat the material in the first conveying pipe, reaches the effect of preheating the material.

Optionally, the first feeding pipe is a serpentine coil.

Through adopting above-mentioned technical scheme, improve the path length that the material removed in the preheating cabinet to improve the heating effect of preheating the mechanism to the material.

Optionally, the ultra-high temperature sterilization mechanism is communicated with a cooling mechanism, the cooling mechanism comprises a cooling box and a second feeding pipe, the second feeding pipe is located in the cooling box, the second feeding pipe is fixedly connected with the cooling box, one end of the second feeding pipe is communicated with the ultra-high temperature sterilization mechanism, the other end of the second feeding pipe is communicated with the outside of the cooling box, and a second inlet and a second liquid outlet are formed in the cooling box.

Through adopting above-mentioned technical scheme, the super pasteurization mechanism intercommunication has cooling body, and in the material through super pasteurization got into the cooler bin through the second conveying pipe, the cooling water was in the cooler bin was got into through the second inlet, utilized the cooling water to cool down the material in the second conveying pipe.

Optionally, the second liquid outlet is communicated with the first liquid inlet.

Through adopting above-mentioned technical scheme, with second liquid outlet and first inlet intercommunication, utilize cooling water to cool off the back to the material, cooling water temperature risees, carries the cooling water that the temperature risees to get into the preheating cabinet and preheats the material, reduces the consumption of external energy, and is energy-concerving and environment-protective.

Optionally, a heating pipe is arranged in the preheating box, and the heating pipe is sleeved outside the first feeding pipe.

By adopting the technical scheme, the heating pipe is arranged in the preheating tank, so that the possibility of insufficient water temperature in the preheating tank is reduced.

Optionally, first liquid outlet intercommunication has the pond of keeping in, be provided with the water pump in the pond of keeping in, the import and the pond intercommunication of keeping in of water pump, the export and the second inlet intercommunication of water pump.

Through adopting above-mentioned technical scheme, carry the water that flows out in the preheating cabinet and get into the pond cooling of keeping in, utilize the water pump to reuse in going into the cooling tank with the water pump after the cooling to realize the cyclic utilization of water.

In summary, the present application includes at least one of the following beneficial technical effects:

1. by arranging the shunting mechanism between the preheating mechanism and the ultra-high temperature sterilization mechanism, when the produced beverage needs to be preheated before homogenization, the preheating mechanism is communicated with a feed inlet of the homogenizer by the shunting mechanism, the ultra-high temperature sterilization mechanism is communicated with a discharge outlet of the homogenizer by the shunting mechanism, the beverage enters the preheating mechanism for preheating before entering the homogenizer, and directly enters the ultra-high temperature sterilization mechanism for sterilization after homogenization is completed, so that the processing efficiency of the beverage is improved;

2. the second liquid outlet is communicated with the first liquid inlet, so that cooling water with increased temperature is conveyed into the preheating box to preheat the material, the consumption of external energy is reduced, and the device is energy-saving and environment-friendly;

3. water flowing out of the preheating box is conveyed to enter the temporary storage pool for cooling, and the water pump after being cooled is pumped into the cooling box for reuse, so that water recycling is realized.

Drawings

FIG. 1 is a schematic diagram of the overall structure of an embodiment of the present application;

fig. 2 is a schematic structural view of a cooling mechanism portion according to an embodiment of the present application.

Reference numerals: 100. a preheating mechanism; 110. a preheating box; 111. a first liquid inlet; 112. a first liquid outlet; 120. a first feed pipe; 200. an ultra-high temperature sterilization mechanism; 300. a flow dividing mechanism; 310. a communicating pipe; 320. a flow divider valve; 330. a liquid outlet pipe; 340. a liquid inlet pipe; 400. an on-off valve; 500. a cooling mechanism; 510. a cooling tank; 511. a second liquid inlet; 512. a second liquid outlet; 520. a second feed tube; 600. heating a tube; 700. a temporary storage pool; 800. and (4) a water pump.

Detailed Description

The present application is described in further detail below with reference to figures 1-2.

The embodiment of the application discloses a high-temperature instantaneous sterilizer for beverage production. Referring to fig. 1, a high temperature instant sterilizer for beverage production includes preheating mechanism 100 for preheating the material, preheating mechanism 100 is communicated with pasteurization mechanism 200 through reposition of redundant personnel mechanism 300, preheating mechanism 100 and pasteurization mechanism 200 are all communicated with the homogenizer through reposition of redundant personnel mechanism 300. The ultra-high temperature sterilization mechanism 200 is communicated with a cooling mechanism 500, and the material leaving the ultra-high temperature sterilization mechanism 200 is cooled by the cooling mechanism 500. The cooling mechanism 500 is communicated with the preheating mechanism 100, and cooling water after the cooling mechanism 500 works flows into the preheating mechanism 100 to preheat materials.

Referring to fig. 1 and 2, the preheating mechanism 100 includes a preheating compartment 110, and the preheating compartment 110 has a hollow rectangular parallelepiped box structure; a first liquid outlet 112 is formed in the position, close to the bottom, of the side wall of the preheating box 110, a first liquid inlet 111 is formed in the position, close to the top, of the side wall of the preheating box 110, and the first liquid inlet 111 and the first liquid outlet 112 are both communicated with a switch valve 400; a first feeding pipe 120 is fixedly connected in the preheating box 110, one end of the first feeding pipe 120 is communicated with the outside of the preheating box 110, and the other end of the first feeding pipe 120 is communicated with the flow dividing mechanism 300; the material enters the preheating box 110 through the first feeding pipe 120, heating water is input into the preheating box 110 through the first liquid inlet 111, and the material in the first feeding pipe 120 is heated by the heating water, so that the effect of preheating the material is achieved.

First conveying pipe 120 is serpentine coil, through setting up first conveying pipe 120 into serpentine coil, improves the path length that the material removed in preheating tank 110 to the improvement preheats the heating effect of mechanism 100 to the material. The heating pipe 600 is sleeved outside the first feeding pipe 120, and the heating pipe 600 is fixedly connected with the preheating box 110. By providing heating pipe 600 in preheating tank 110, the possibility of insufficient water temperature in preheating tank 110 is reduced.

Referring to fig. 1 and 2, the ultra-high temperature sterilization mechanism 200 is fixedly connected above the preheating chamber 110; the flow distribution mechanism 300 comprises a communication pipe 310, one end of the communication pipe 310 is communicated with the first feeding pipe 120, and the other end of the communication pipe 310 is communicated with the ultra-high temperature sterilization mechanism 200; the communicating pipe 310 is provided with a diverter valve 320, and the diverter valve 320 is communicated with the communicating pipe 310; the communicating pipe 310 is communicated with a liquid outlet pipe 330, the liquid outlet pipe 330 is positioned between the diverter valve 320 and the first feeding pipe 120, the communicating pipe 310 is communicated with a liquid inlet pipe 340, the liquid inlet pipe 340 is positioned between the diverter valve 320 and the ultra-high temperature sterilization mechanism 200, and the liquid outlet pipe 330 and the liquid inlet pipe 340 are both communicated with a switch valve 400.

The preheating mechanism 100 is communicated with the ultra-high temperature sterilization mechanism 200 through a communicating pipe 310, a diverter valve 320 is arranged on the communicating pipe 310, the communicating pipe 310 is communicated with the feed end of the homogenizer through a liquid outlet pipe 330, and the communicating pipe 310 is communicated with the discharge end of the homogenizer through a liquid inlet pipe 340; when need carry into the homogenizer preheating the material transport and carry out the homogeneity, close flow divider 320, open two ooff valves 400, make preheating the material carry and carry out the homogeneity in getting into the homogenizer, get into after the homogeneity is accomplished and get into super pasteurization mechanism 200 through the discharging pipe and disinfect, and flow divider 300 uses conveniently.

Referring to fig. 1 and 2, the cooling mechanism 500 includes a cooling box 510, the cooling box 510 is a hollow rectangular parallelepiped box structure, and the cooling box 510 is fixedly connected above the ultra-high temperature sterilization mechanism 200; a second liquid outlet 512 is formed in the position, close to the bottom, of the side wall of the cooling box 510, a second liquid inlet 511 is formed in the position, close to the top, of the side wall of the cooling box 510, and the second liquid inlet 511 and the second liquid outlet 512 are both communicated with a switch valve 400; a second feeding pipe 520 is fixedly connected in the cooling box 510, one end of the first feeding pipe 120 is communicated with the ultra-high temperature sterilization mechanism 200, and the other end of the second feeding pipe 520 is communicated with the outside of the cooling box 510; the material that passes through ultra-high temperature sterilization gets into the cooling box 510 through second conveying pipe 520 in, cooling water gets into the cooling box 510 through second inlet 511 in, utilizes cooling water to cool down the material in the second conveying pipe 520.

Second liquid outlet 512 and first inlet 111 intercommunication, through with second liquid outlet 512 and first inlet 111 intercommunication, utilize the cooling water to cool off the material after, the cooling water temperature risees, carries the cooling water that the temperature risees and gets into preheating cabinet 110 and preheat the material, reduces the consumption of external energy, and is energy-concerving and environment-protective.

Referring to fig. 2, the first liquid outlet 112 is communicated with the temporary storage tank 700, the heating water flowing out of the preheating tank 110 flows into the temporary storage tank 700 for cooling, the temporary storage tank 700 is fixedly connected with a water pump 800, an inlet of the water pump 800 is communicated with the temporary storage tank 700, an outlet of the water pump 800 is communicated with the second liquid inlet 511, and the water pump 800 after being cooled is reused in the cooling tank 510, so that water recycling is realized.

The implementation principle of the high-temperature instantaneous sterilizer for beverage production in the embodiment of the application is as follows: through setting up reposition of redundant personnel mechanism 300 between preheating mechanism 100 and pasteurization mechanism 200, when the drink that produces need preheat before the homogeneity, utilize reposition of redundant personnel mechanism 300 to preheat the feed inlet intercommunication of mechanism 100 and isotropic symmetry, utilize reposition of redundant personnel mechanism 300 to construct 200 pasteurization mechanism and the discharge gate intercommunication of isotropic symmetry, the drink advances to preheat mechanism 100 and preheats before getting into the isotropic symmetry, directly gets into pasteurization mechanism 200 after the homogeneity is accomplished and sterilizes, improve the machining efficiency of drink.

The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.

Claims

1. A high temperature instant sterilizer for beverage production which characterized in that: the device comprises a preheating mechanism (100), an ultra-high temperature sterilization mechanism (200) and a flow distribution mechanism (300) communicated with a homogenizer, wherein the flow distribution mechanism (300) is communicated between the preheating mechanism (100) and the ultra-high temperature sterilization mechanism (200).

2. A high-temperature instantaneous sterilizer for the production of drinks according to claim 1, characterized in that: the flow dividing mechanism (300) comprises a communicating pipe (310), a flow dividing valve (320), a liquid outlet pipe (330) communicated with the feeding end of the homogenizer, a liquid inlet pipe (340) communicated with the discharging end of the homogenizer and two switch valves (400), one end of the communicating pipe (310) is communicated with the preheating mechanism (100), the other end of the communicating pipe (310) is communicated with the ultra-high temperature sterilization mechanism (200), the flow dividing valve (320) is arranged on the communicating pipe (310), the flow dividing valve (320) is communicated with the communicating pipe (310), the liquid outlet pipe (330) is positioned between the flow dividing valve (320) and the preheating mechanism (100), the liquid inlet pipe (340) is communicated with the communicating pipe (310), the liquid inlet pipe (340) is positioned between the flow dividing valve (320) and the ultra-high temperature sterilization mechanism (200), one of the switch valves (400) is communicated with the liquid inlet pipe (340), the other switch valve (400) is communicated with the liquid outlet pipe (330).

3. A high-temperature instantaneous sterilizer for the production of drinks according to claim 2, characterized in that: the preheating mechanism (100) comprises a preheating box (110) and a first feeding pipe (120), the first feeding pipe (120) is located in the preheating box (110), the first feeding pipe (120) is fixedly connected with the preheating box (110), one end of the first feeding pipe (120) is communicated with a communicating pipe (310), the other end of the first feeding pipe (120) is communicated with the outside of the preheating box (110), and a first liquid inlet (111) and a first liquid outlet (112) are formed in the preheating box (110).

4. A high-temperature instantaneous sterilizer for the production of drinks according to claim 3, characterized in that: the first feeding pipe (120) is a serpentine coil.

5. A high-temperature instantaneous sterilizer for the production of drinks according to claim 4, characterized in that: the ultra-high temperature sterilization mechanism (200) is communicated with a cooling mechanism (500), the cooling mechanism (500) comprises a cooling box (510) and a second feeding pipe (520), the second feeding pipe (520) is located in the cooling box (510), the second feeding pipe (520) is fixedly connected with the cooling box (510), one end of the second feeding pipe (520) is communicated with the ultra-high temperature sterilization mechanism (200), the other end of the second feeding pipe (520) is communicated with the outside of the cooling box (510), and a second liquid inlet (511) and a second liquid outlet (512) are formed in the cooling box (510).

6. A high-temperature instantaneous sterilizer for the production of drinks according to claim 5, characterized in that: the second liquid outlet (512) is communicated with the first liquid inlet (111).

7. A high-temperature instantaneous sterilizer for the production of drinks according to claim 3, characterized in that: a heating pipe (600) is arranged in the preheating box (110), and the heating pipe (600) is sleeved on the outer side of the first feeding pipe (120).

8. A high-temperature instantaneous sterilization machine for beverage production according to claim 6, characterized in that: the first liquid outlet (112) is communicated with a temporary storage pool (700), a water pump (800) is arranged in the temporary storage pool (700), an inlet of the water pump (800) is communicated with the temporary storage pool (700), and an outlet of the water pump (800) is communicated with the second liquid inlet (511).