Energy-saving yellow wine high-temperature instantaneous sterilization and storage system

Abstract

The utility model discloses an energy-saving yellow wine high-temperature instantaneous sterilization and storage system. The energy-saving yellow wine high-temperature instantaneous sterilization and storage system comprises a balance cylinder, a material pump, an aging tank, a cleaning system and a timing high-temperature sterilization system, the balance cylinder is used for receiving sake raw materials and inputting the sake raw materials into the timing high-temperature sterilization system under the power of the material pump; the cleaning system is used for cleaning the balance cylinder, the aging tank and the pipeline; the timed high-temperature sterilization system is used for carrying out timed high-temperature sterilization on the sake raw material conveyed from the balance cylinder in a 120 DEG C stabilizing pipe after the sake raw material sequentially passes through the material heat exchange system and the material heating system; the sterilized sake raw material is cooled by the heat energy recovery system and the material heat exchange system in sequence and then is conveyed into the aging tank to be aged and aged. According to the device, normal-temperature conveying of sake raw materials is achieved, then preheating and heating are conducted, high-temperature timing sterilization is conducted, heat exchange cooling conveying is conducted, preheating and heating of hot water of a heating system are achieved, heat energy is greatly saved, and energy consumption is reduced.

Description

TECHNICAL FIELD

[0001] The utility model relates to yellow rice production technical field, concretely is a kind of energy-saving type yellow rice high temperature instantaneous sterilization storage system. BACKGROUND

[0002] When yellow rice is produced, the clear rice formed after the fermented wine is filtered and clarified needs to be heated at high temperature, then is transported to sterilization tank for high-temperature sterilization, and then is transported to aging tank for aging and maturation after cooling to improve flavor and quality. Since the energy cost of the clear rice after high-temperature heating is high in pipeline transportation, and the clear rice at high temperature is transported in the pipeline for a long time, which has a great influence on the quality of the matured yellow rice, therefore, the high-temperature sterilization storage technology needs to be improved to achieve the purpose of saving energy and ensuring the quality of yellow rice. SUMMARY

[0003] In view of the deficiencies in the prior art, the utility model provides an energy-saving type yellow rice high temperature instantaneous sterilization storage system to solve the problems in the above background.

[0004] To achieve the above purpose, the utility model realizes the following technical scheme: an energy-saving type yellow rice high temperature instantaneous sterilization storage system comprises a balance cylinder, a material pump, an aging tank, a cleaning system and a timing high-temperature sterilization system.

[0005] The balance cylinder is used to input the clear rice raw material into the timing high-temperature sterilization system under the power of the material pump.

[0006] The cleaning system is used to clean the balance cylinder, the aging tank and the pipeline.

[0007] The timing high-temperature sterilization system comprises a material heat exchange system, a material heating system, a heat energy recovery system and a stable pipe for timing high-temperature sterilization. The stable pipe is connected according to the sterilization time to realize timing, so as to achieve the best sterilization time for various yellow rice production of our enterprise, which can well complete sterilization and ensure the flavor and quality of yellow rice.

[0008] The clear rice raw material transported from the balance cylinder is sequentially subjected to the material heat exchange system and the material heating system, and then is subjected to timing high-temperature sterilization in the stable pipe at 120 degrees Celsius. The sterilized clear rice raw material is sequentially subjected to the heat energy recovery system and the material heat exchange system for cooling, and then is transported to the aging tank for aging and maturation.

[0009] Further, the material heat exchange system comprises a third plate heat exchanger and a fourth plate heat exchanger; a pipeline for conveying the raw sake material sequentially connects the balance cylinder, the fourth plate heat exchanger and the third plate heat exchanger, and the raw sake material after high-temperature sterilization is introduced into the aging tank through a return pipeline for conveying the raw sake material.

[0010] Further, the material heating system comprises a first plate heat exchanger, a second plate heat exchanger and a heating system; one end of the return pipeline for conveying the raw sake material is connected with the output pipeline of the third plate heat exchanger after heat exchange, and the other end sequentially connects the first plate heat exchanger and the second plate heat exchanger; the heating system heats the raw sake material between the first plate heat exchanger and the second plate heat exchanger to 120 degrees Celsius, and after high-temperature sterilization through the stabilizing pipeline arranged at the outlet of the second plate heat exchanger, the raw sake material is introduced into the return pipeline for conveying the raw sake material.

[0011] Further, the heating system comprises a hot water cylinder and a heater; the hot water cylinder conveys the water in the hot water pipeline sequentially connected to the third plate heat exchanger, the second plate heat exchanger and the first plate heat exchanger through a circulating hot water pump, and the water in the hot water pipeline is circulated and conveyed back to the hot water cylinder after heat exchange with the raw sake material between the first plate heat exchanger and the second plate heat exchanger; the connecting pipelines on the left and right sides of the second plate heat exchanger are provided with heaters; the heaters are provided with control valves connected to a heating steam pipeline; the hot water cylinder is provided with an on-off valve for water replenishment; the return circuit of the hot water pipeline is provided with a right-angle stop valve and a flow regulating butterfly valve.

[0012] Further, the heat energy recovery system sequentially connects the return pipeline for the raw sake introduced from the outlet of the stabilizing pipeline with the second plate heat exchanger and the third plate heat exchanger, so that the hot water pipeline of the heating system exchanges heat with the return pipeline for conveying the raw sake introduced from the outlet of the stabilizing pipeline, thereby heating the hot water pipeline; the return pipeline for conveying the raw sake introduced from the third plate heat exchanger is connected with the fourth plate heat exchanger, thereby preheating the pipeline for conveying the raw sake between the fourth plate heat exchanger and the third plate heat exchanger.

[0013] Further, the material heat exchange system is further connected with a material temperature adjusting standby system; one end of the material temperature adjusting standby system is connected with the fourth plate heat exchanger through a pipeline connected with a cooling water pipeline, and then the pipeline is introduced from the outlet of the fourth plate heat exchanger; the return pipeline for conveying the raw sake after heat exchange with the material heat exchange system is introduced into the aging tank; the pipeline connected with the cooling water pipeline is provided with a reversing valve.

[0014] Further, the return pipeline of the clear liquor raw material conveying pipe connected with the aging tank is sequentially provided with a pneumatic pressure maintaining valve, a sampling valve and a reversing valve in the return direction; whether the sterilized clear liquor raw material meets the yellow rice production index requirement is determined through the sampling valve; if the clear liquor raw material meets the yellow rice production index requirement, the clear liquor raw material is input into the aging tank through the reversing valve and the return pipeline of the clear liquor raw material conveying pipe; if the clear liquor raw material does not meet the yellow rice production index requirement, the clear liquor raw material is input into the balance cylinder through the reversing valve, a pneumatic stop valve, the reversing valve and the clear liquor raw material return pipeline, and the sterilization cycle is performed again.

[0015] Further, the cleaning system comprises pure water cleaning, acid and alkali cleaning and aging tank CIP cleaning; the pure water cleaning is to pump pure water into the balance cylinder for cleaning the balance cylinder and pipeline; the acid and alkali cleaning is to pump the concentrated acid or alkali cleaning solution in the acid and alkali cleaning solution tank into the cleaning ball arranged on the balance cylinder through a pneumatic diaphragm pump to clean the balance cylinder and pipeline; the pure water cleaning and the acid and alkali cleaning share one pipeline, and the type of cleaning solution is controlled through the reversing valve arranged on the pipeline; the aging tank CIP cleaning comprises a tank top assembly arranged on the top of the aging tank and a tank CIP water introduction pipeline; the tank CIP water is introduced into the aging tank through the pneumatic butterfly valve arranged on the tank CIP water introduction pipeline; the water after cleaning the aging tank is returned from the material outlet of the aging tank under the drive of the product discharge pump to form an aging tank CIP return loop; the pneumatic butterfly valve is arranged on the material outlet of the aging tank; the cleaning solution after the pure water cleaning and the acid and alkali cleaning is input into the aging tank through the return pipeline of the clear liquor raw material conveying pipe for cleaning, or the cleaning solution after the pure water cleaning and the acid and alkali cleaning is returned to the tank CIP return loop under the control of the pneumatic butterfly valve through the return pipeline of the clear liquor raw material conveying pipe; the pneumatic butterfly valve is arranged on the inlet of the return pipeline of the clear liquor raw material conveying pipe connected with the aging tank.

[0016] Further, the pipeline arranged on the balance cylinder is connected with the reversing valve to introduce the clear liquor raw material; the reversing valve is connected with the reversing valve through the pneumatic stop valve arranged on the pipeline to clean the pipeline; the pipeline of the balance cylinder for introducing the clear liquor raw material is further provided with the pneumatic stop valve and the reversing valve for introducing pure water.

[0017] Further, the material pump comprises a first material pump and a second material pump; the first material pump is arranged on the pipeline of the clear liquor raw material conveying pipe at the outlet of the balance cylinder; the second material pump is arranged on the return pipeline of the clear liquor raw material conveying pipe close to the first plate heat exchanger; the balance cylinder is provided with a liquid level meter; the pipeline of the clear liquor raw material conveying pipe on the feeding side of the first material pump is provided with an electric conductivity meter, and the pipeline of the clear liquor raw material conveying pipe on the discharging side is provided with an electromagnetic flowmeter. Advantages

[0018] The utility model provides a kind of energy-saving type yellow rice high temperature instantaneous sterilization storage system, and compared with prior art has the following beneficial effects: the normal temperature conveying of sake raw materials is realized, then preheating, heating to 120 degrees Celsius is carried out high-temperature sterilization, then heat exchange cooling conveying is carried out, the purpose of the timed sterilization of sake raw materials is achieved, the flavor and quality of yellow rice production are guaranteed, and by heat exchange system, both preheating of the entering sake raw materials to be sterilized and heating of the hot water of heating system can be carried out, and the sake raw materials after timed sterilization can also be cooled, greatly saving heat energy, and reducing energy consumption. BRIEF DESCRIPTION OF DRAWINGS

[0019] Figure 1 It is the overall principle structure schematic diagram of the utility model timed sterilization 5 seconds.

[0020] Figure 2 It is the overall principle structure schematic diagram of the utility model timed sterilization different time.

[0021] In the drawing: balance cylinder 1;Electric conductivity meter 2;First material pump 3;Electromagnetic flowmeter 4;Liquid level meter 5;Cleaning ball 6;Acid-base washing liquid tank 7;Pneumatic diaphragm pump 8;Aging tank 9;Product discharge pump 10;Stable pipe 11;Heater 12;Circulating hot water pump 13;Hot water cylinder 14;Second material pump 15;Material heat exchange system 16;Material temperature regulating standby system 19;First plate heat exchanger G;Second plate heat exchanger Z1;Third plate heat exchanger Z2;Fourth plate heat exchanger Z3;Fifth plate heat exchanger F;Reversing valve (V2, V3, V8, V9, V10, V11, V13);Pneumatic stop valve (V1, V4, V5, V6, V7);Pneumatic pressure maintaining valve V12;Control valve V14;Right-angle stop valve V15;Flow regulating butterfly valve V16;Pneumatic butterfly valve (V17, V18, V19, V20). DETAILED DESCRIPTION

[0022] The present disclosure will be further described below in conjunction with the drawings and embodiments. It can be understood that the specific embodiments described herein are only used to explain the related content, and not limited to the present disclosure. In addition, it needs to be explained that, for the convenience of description, only parts related to the present disclosure are shown in the drawings.

[0023] Embodiment 1: as shown in Figure 1 and Figure 2 An energy-saving type yellow rice high temperature instantaneous sterilization storage system includes balance cylinder 1, material pump, aging tank 9, cleaning system and timed high-temperature sterilization system;

[0024] The balance cylinder 1 is used to access sake raw materials, and under the power of material pump, the sake raw materials are input to the timed high-temperature sterilization system;

[0025] The cleaning system is used for cleaning the balance cylinder 1, the aging tank 9 and pipelines;

[0026] The timing high-temperature sterilization system comprises a material heat exchange system 16, a material temperature rising system 17, a heat energy recovery system 18 and a stable pipe 11 for timing high-temperature sterilization; the stable pipe 11 is cross-connected to realize timing according to sterilization time, the length of the stable pipe 11 determines the maintained time, different lengths of the stable pipe are combined to realize the purpose of maintaining different time; according to the accumulated experience, the sterilization time can be set to be 5 seconds, 10 seconds, 15 seconds and 20 seconds which are four types of relatively reasonable types to meet the best sterilization time of various yellow rice wine production of the enterprise, so that the sterilization can be well completed and the flavor and quality of the yellow rice wine can be ensured;

[0027] The timing high-temperature sterilization system realizes the normal-temperature tank entering of the yellow rice wine, high-temperature instantaneous sterilization, cold and hot wine heat energy exchange technology, reduces the energy consumption under the premise of ensuring the microbial index and improves the flavor and quality of the yellow rice wine.

[0028] As a preferred embodiment, the material heat exchange system 16 comprises a third plate heat exchanger Z2 and a fourth plate heat exchanger Z3; a pipeline for yellow rice wine material conveying is sequentially connected with the balance cylinder 1, the fourth plate heat exchanger Z3 and the third plate heat exchanger Z2; the yellow rice wine material after high-temperature timing sterilization is connected to the aging tank 9 through a return pipeline for yellow rice wine material conveying.

[0029] As a preferred embodiment, the material temperature rising system 17 comprises a first plate heat exchanger G, a second plate heat exchanger Z1 and a heating system; one end of the return pipeline for yellow rice wine material conveying is connected with an output pipe after heat exchange of the third plate heat exchanger Z2, and the other end is sequentially connected with the first plate heat exchanger G and the second plate heat exchanger Z1; the heating system heats the yellow rice wine material between the first plate heat exchanger G and the second plate heat exchanger Z1 to 120 degrees Celsius, and the yellow rice wine material is connected to the return pipeline for yellow rice wine material conveying after timing high-temperature sterilization through the stable pipe 11 arranged at the outlet of the second plate heat exchanger Z1.

[0030] As a preferred embodiment, the heating system comprises a hot water tank 14 and a heater 12; the hot water tank 14 transports water in the hot water pipe connected to the third plate heat exchanger Z2, the second plate heat exchanger Z1 and the first plate heat exchanger G in turn through the circulating hot water pump 13, and the water in the hot water pipe is transported back to the hot water tank 14 after heat exchange with the first plate heat exchanger G and the second plate heat exchanger Z1; the heater 12 is arranged on the left and right connecting pipes of the second plate heat exchanger Z1; the control valve V14 connected to the heating steam pipe is arranged on the heater 12; the on-off valve for water replenishment is arranged on the hot water tank 14; the straight angle stop valve V15 and the flow regulating butterfly valve V16 are arranged on the return circuit of the hot water pipe.

[0031] As a preferred embodiment, the heat energy recovery system 18 is connected to the second plate heat exchanger Z1 and the third plate heat exchanger Z2 in turn from the rice wine return pipe connected to the outlet of the stabilizing pipe 11, so that the hot water pipe of the heating system is heat exchanged with the return pipe of the rice wine raw material transported from the outlet of the stabilizing pipe 11, thereby achieving heating of the hot water pipe; the return pipe of the rice wine raw material transported from the third plate heat exchanger Z2 is connected to the fourth plate heat exchanger Z3, thereby achieving heat exchange preheating of the pipe for input of the rice wine raw material between the fourth plate heat exchanger Z3 and the third plate heat exchanger Z2.

[0032] As a preferred embodiment, the material heat exchange system 16 is further connected to the material temperature adjusting standby system 19; the material temperature adjusting standby system 19 is connected to the fourth plate heat exchanger Z3 through the pipe connected to the cooling water pipe at one end of the fifth plate heat exchanger F, and then led out from the outlet of the fourth plate heat exchanger Z3; the return pipe of the rice wine raw material transported after heat exchange with the material heat exchange system 16 is connected to the aging tank 9; the reversing valve V13 is arranged on the pipe connected to the cooling water pipe.

[0033] As a preferred embodiment, the return pipe of the rice wine raw material connected to the aging tank 9 is sequentially provided with the pneumatic pressure maintaining valve V12, the sampling valve and the reversing valve V8 in the return direction; the pneumatic pressure maintaining valve V12 is used to ensure the pressure of the material system, and the highest temperature and pressure that the material can reach are proportional, the pneumatic pressure maintaining valve V12 ensures the stability of the operation of the system, the sampling valve is used to determine whether the sterilized rice wine raw material meets the yellow rice production index requirements, if it meets the yellow rice production index requirements, it is input to the aging tank 9 through the reversing valve V8 and the return pipe of the rice wine raw material, if it does not meet the yellow rice production index requirements, it is input to the balance tank 1 through the reversing valve V8, the pneumatic stop valve V6, the reversing valve V2 and the rice wine raw material return pipe, and then the sterilization cycle is performed again.

[0034] As a preferred embodiment, the cleaning system includes pure water cleaning, acid-base cleaning and aging tank CIP cleaning; the pure water cleaning is to pump pure water into the balance cylinder 1 to clean the balance cylinder 1 and the pipeline; the acid-base cleaning is to pump the concentrated acid or alkali cleaning solution in the acid-base cleaning tank 7 into the cleaning ball 6 arranged on the balance cylinder 1 through the pneumatic diaphragm pump 8 to clean the balance cylinder 1 and the pipeline; the pure water cleaning and the acid-base cleaning share a pipeline, and the type of cleaning solution is controlled by connecting the reversing valve (V11, V10, V9) arranged on the pipeline; the aging tank CIP cleaning includes a tank top assembly arranged at the top of the aging tank 9 and a tank CIP water introduction pipe, the tank top assembly introduces tank CIP water through the pneumatic butterfly valve V20 arranged on the tank CIP water introduction pipe to clean the aging tank, and the water after cleaning the aging tank is returned to form an aging tank 9 tank CIP loop under the drive of the product discharge pump 10; the pneumatic butterfly valve V19 is arranged on the material outlet of the aging tank 9; the cleaning solution after the pure water cleaning and the acid-base cleaning is input into the aging tank 9 through the return pipeline of the clean beer raw material conveying for cleaning, or the cleaning solution after the pure water cleaning and the acid-base cleaning is returned to the tank CIP loop under the control of the pneumatic butterfly valve V18 through the return pipeline of the clean beer raw material conveying; the pneumatic butterfly valve V17 is arranged on the inlet of the return pipeline of the clean beer raw material conveying; effective cleaning is realized through the cleaning system, a clean environment is provided for clean beer conveying and sterilization, and product microbial contamination is avoided.

[0035] As a preferred embodiment, the pipeline arranged on the balance cylinder 1 is connected to the reversing valve V3 to introduce clean beer raw materials; the reversing valve V3 is connected to the reversing valve V8 through the pneumatic stop valve (V4, V5, V7) arranged on the pipeline to clean the pipeline; the pipeline arranged on the balance cylinder 1 to introduce clean beer raw materials is further provided with the pneumatic stop valve V1 and the reversing valve V2 to introduce pure water.

[0036] As a preferred embodiment, the material pump includes a first material pump 3 and a second material pump 15; the first material pump 3 is arranged on the pipeline of the clean beer raw material conveying at the outlet of the balance cylinder 1; the second material pump 15 is arranged on the return pipeline of the clean beer raw material conveying close to the first plate heat exchanger G; the balance cylinder 1 is provided with a liquid level meter 5; the pipeline of the clean beer raw material conveying at the feeding side of the first material pump 3 is provided with an electric conductivity meter 2, and the pipeline of the clean beer raw material conveying at the discharging side is provided with an electromagnetic flowmeter 4; the liquid level meter 5, the electric conductivity meter 2 and the electromagnetic flowmeter 4 feed data to the controller to control the stability of the liquid level and the flow rate, so that material shortage or tank overflow in the production process is avoided, and the production stability and the sterilization efficiency are ensured.

[0037] Embodiment 2: The method for using the energy-saving high-temperature instant sterilization storage system of yellow rice wine is as follows. Step 1: The concentrated acid or alkali cleaning solution in the acid and alkali cleaning solution tank 7 is pumped into the cleaning ball 6 arranged on the balance cylinder 1 by the pneumatic diaphragm pump 8 to clean the balance cylinder 1 and the pipeline. Step 2: The tank top assembly at the top of the aging tank 9 introduces the cleaning CIP water into the aging tank cleaning through the pneumatic butterfly valve V20 arranged on the cleaning CIP water introduction pipe. The water after cleaning the aging tank is returned from the material outlet of the aging tank 9 under the drive of the product discharge pump 10. Step 3: The pure water is pumped into the balance cylinder 1 to clean the balance cylinder 1 and the pipeline. The cleaning solution after cleaning returns to the cleaning CIP loop under the control of the pneumatic butterfly valve V18, and the cleaning process is completed. Step 4: The clear rice raw material is introduced into the balance cylinder 1. Under the power of the first material pump 3 and the second material pump 15, the clear rice raw material passes through the material heat exchange system 16 and the material temperature rising system 17 in turn. The heating system heats the clear rice raw material flowing through the hot water cylinder 14 and the heater 12 to make the temperature of the heated clear rice raw material reach 120 degrees, and the clear rice raw material is sterilized in the stabilizing pipe 11 for a certain time to reduce the energy consumption and the deterioration of the flavor and taste of the clear rice raw material caused by the overlong or too short time of staying at high temperature. The sterilized clear rice raw material passes through the heat energy recovery system 18. At this time, the temperature of the clear rice raw material is 120 degrees Celsius, which is high, so that the clear rice raw material exchanges heat with the hot water (at this time, the temperature of the hot water before heat exchange is about 105 degrees Celsius) in the pipeline of the heating system entering the second plate heat exchanger Z1 and the third plate heat exchanger Z2, thereby increasing the temperature of the hot water in the pipeline of the heating system and reducing the temperature of the sterilized clear rice raw material, so that the heat energy is recycled. The temperature of the clear rice raw material after passing through the heat energy recovery system 18 is reduced, which is about 110 degrees Celsius at this time. The clear rice raw material at this time exchanges heat with the clear rice raw material to be sterilized (at this time, the temperature of the clear rice raw material to be sterilized is about 20 degrees Celsius) in the material heat exchange system 16, so that the clear rice raw material to be sterilized can be heated to about 100 degrees Celsius, while the sterilized clear rice raw material is cooled to about 30 degrees Celsius, which meets the temperature requirement of the clear rice raw material entering the aging tank 9. If the sterilized clear rice raw material is still higher than 40 degrees Celsius after cooling, the material temperature adjusting standby system 19 is used for heat exchange and cooling to meet the temperature requirement of the clear rice raw material entering the aging tank 9. The sterilized clear rice raw material is sampled and analyzed through the sampling valve (not shown in the figure, which is a commonly used sampling component in the industry). If the sterilization index meets the requirement, the sterilized clear rice raw material is input into the aging tank 9 through the reversing valve V8 and the clear rice raw material conveying return pipeline to age and mature, and then the qualified yellow rice wine is output and filled through the product discharge pump 10. If the sterilization index does not meet the requirement, the sterilized clear rice raw material is input into the balance cylinder 1 through the reversing valve V8, the pneumatic stop valve V6, the reversing valve V2 and the clear rice raw material return pipeline to be sterilized again.Through the energy-saving type yellow rice high-temperature instantaneous sterilization storage system, the raw materials of yellow rice can be transported at normal temperature, then preheated and heated to 120 degrees Celsius for high-temperature sterilization, and then transported after heat exchange and temperature reduction, so that the raw materials of yellow rice achieve the purpose of sterilization, and the flavor and quality of yellow rice production are ensured. At the same time, through the heat exchange system, the raw materials of yellow rice to be sterilized can be preheated and the hot water of the heating system can be heated, and the raw materials of yellow rice after sterilization can also be cooled, which greatly saves heat energy and reduces energy consumption.

[0038] Those skilled in the art will understand that the above embodiments are only for clearly illustrating the present disclosure, and are not intended to limit the scope of the present disclosure. Based on the above disclosure, other changes or modifications can also be made by those skilled in the art, and these changes or modifications are still within the scope of the present disclosure.

Claims

1. An energy-saving high-temperature instant sterilization storage system for yellow rice wine, comprising a balance cylinder (1), a material pump, an aging tank (9), a cleaning system and a timing high-temperature sterilization system, characterized in that the balance cylinder (1) is used for accessing the raw materials of the rice wine and inputting the raw materials of the rice wine into the timing high-temperature sterilization system under the power of the material pump; the cleaning system is used for cleaning the balance cylinder (1), the aging tank (9) and the pipeline; the timing high-temperature sterilization system comprises a material heat exchange system (16), a material temperature rising system (17), a heat energy recovery system (18) and a stable pipe (11) for timing high-temperature sterilization; the stable pipe (11) is cross-connected to realize timing according to the sterilization time; the timing high-temperature sterilization system sequentially subjects the raw materials of the rice wine delivered from the balance cylinder (1) to the material heat exchange system (16) and the material temperature rising system (17), and then subjects the raw materials to timing high-temperature sterilization in the stable pipe (11) at 120 degrees Celsius, and sequentially subjects the sterilized raw materials of the rice wine to the heat energy recovery system (18) and the material heat exchange system (16) for cooling, and then delivers the sterilized raw materials of the rice wine into the aging tank (9). The material heat exchange system (16) comprises a third plate heat exchanger (Z2) and a fourth plate heat exchanger (Z3); the pipeline for delivering the raw materials of the rice wine sequentially connects the balance cylinder (1), the fourth plate heat exchanger (Z3) and the third plate heat exchanger (Z2); and the raw materials of the rice wine after high-temperature timing sterilization are accessed into the aging tank (9) through the return pipeline for delivering the raw materials of the rice wine. The material temperature rising system (17) comprises a first plate heat exchanger (G), a second plate heat exchanger (Z1) and a heating system; one end of the return pipeline for delivering the raw materials of the rice wine is connected with the output pipe of the third plate heat exchanger (Z2) after heat exchange, and the other end sequentially connects the first plate heat exchanger (G) and the second plate heat exchanger (Z1); the heating system heats the raw materials of the rice wine between the first plate heat exchanger (G) and the second plate heat exchanger (Z1) to 120 degrees Celsius, and then the raw materials are subjected to timing high-temperature sterilization through the stable pipe (11) arranged at the outlet of the second plate heat exchanger (Z1) side, and then the raw materials are accessed onto the return pipeline for delivering the raw materials of the rice wine. The heating system comprises a hot water cylinder (14) and a heater (12); the hot water cylinder (14) delivers the water in the hot water pipe sequentially connected to the third plate heat exchanger (Z2), the second plate heat exchanger (Z1) and the first plate heat exchanger (G) through a circulating hot water pump (13), and the water in the hot water pipe is delivered back to the hot water cylinder (14) after heat exchange with the raw materials of the rice wine between the first plate heat exchanger (G) and the second plate heat exchanger (Z1); the heater (12) is arranged on the connecting pipes on the left and right sides of the second plate heat exchanger (Z1) side; the control valve (V14) connected to the heating steam pipe is arranged on the heater (12); the on-off valve for water replenishment is arranged on the hot water cylinder (14); the straight angle stop valve (V15) and the flow regulating butterfly valve (V16) are arranged on the return circuit of the hot water pipe. ​ 2. The energy-saving type high-temperature instant sterilization and storage system for yellow rice wine according to claim 1, characterized in that, ​ 3. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 1, characterized in that, ​ 4. The energy-saving type high-temperature instant sterilization and storage system for yellow rice wine according to claim 3, characterized in that, ​ 5. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 4, characterized in that, The heat energy recovery system (18) is connected to the second plate heat exchanger (Z1) and the third plate heat exchanger (Z2) in sequence from the return pipe of the sake from the outlet of the stabilizing pipe (11), so that the hot water pipe of the heating system exchanges heat with the return pipe of the sake raw material delivery from the outlet of the stabilizing pipe (11), and the heating of the hot water pipe is realized; the return pipe of the sake raw material delivery from the third plate heat exchanger (Z2) is connected to the fourth plate heat exchanger (Z3), so that the pipe of the sake raw material input between the fourth plate heat exchanger (Z3) and the third plate heat exchanger (Z2) is preheated by heat exchange.

6. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 2, characterized in that, The material heat exchange system (16) is further connected with a material temperature adjusting standby system (19); one end of the fifth plate heat exchanger (F) of the material temperature adjusting standby system (19) is communicated with the fourth plate heat exchanger (Z3) through a pipe connected with a cooling water pipe, and then is led out from the outlet of the fourth plate heat exchanger (Z3); the return pipe of the sake raw material delivery after heat exchange with the material heat exchange system (16) is connected to the aging tank (9); a reversing valve (V13) is arranged on the pipe connected with the cooling water pipe.

7. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 2, characterized in that, The return pipe of the sake raw material delivery connected to the aging tank (9) is sequentially provided with a pneumatic pressure maintaining valve (V12), a sampling valve and a reversing valve (V8) in the return direction.

8. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 1, characterized in that, The cleaning system comprises pure water cleaning, acid and alkali cleaning and CIP cleaning of the aging tank; the pure water cleaning is to pump pure water into the balance cylinder (1) to clean the balance cylinder (1) and the pipeline; the acid and alkali cleaning is to pump the concentrated acid or alkali cleaning solution in the acid and alkali cleaning solution tank (7) into the cleaning ball (6) arranged on the balance cylinder (1) by the pneumatic diaphragm pump (8) to clean the balance cylinder (1) and the pipeline; the pure water cleaning and the acid and alkali cleaning share one pipeline, and the type of cleaning solution is controlled by the reversing valves (V11, V10, V9) arranged on the connected pipes; the CIP cleaning of the aging tank comprises a tank top assembly arranged on the top of the aging tank (9) and a tank CIP water introduction pipe, the tank CIP water is introduced into the aging tank by the pneumatic butterfly valve (V20) arranged on the tank CIP water introduction pipe to clean the aging tank, and the water after cleaning of the aging tank is returned from the material outlet of the aging tank (9) under the driving of the product discharge pump (10) to form a tank CIP loop of the aging tank (9); the pneumatic butterfly valve (V19) is arranged on the material outlet of the aging tank (9); the cleaning solution after the pure water cleaning and the acid and alkali cleaning is input into the aging tank (9) through the return pipe of the sake raw material delivery to clean, or the cleaning solution after the pure water cleaning and the acid and alkali cleaning is returned to the tank CIP loop under the control of the pneumatic butterfly valve (V18) through the return pipe of the sake raw material delivery; the pneumatic butterfly valve (V17) is arranged on the inlet of the aging tank (9) to which the return pipe of the sake raw material delivery is input.

9. The energy-saving type high-temperature instant sterilization and storage system for yellow rice wine according to claim 7, characterized in that, The pipeline on the balance cylinder (1) is connected with the reversing valve (V3) to introduce the sake raw materials; the reversing valve (V3) is connected with the reversing valve (V8) through the pipeline provided with the pneumatic stop valve (V4, V5, V7) to clean the pipeline; the pipeline on the balance cylinder (1) for introducing the sake raw materials is further provided with the pneumatic stop valve (V1) and the reversing valve (V2) for introducing the pure water.

10. The energy-saving type of high-temperature instant sterilization and storage system for yellow rice wine according to claim 3, characterized in that, The material pump comprises a first material pump (3) and a second material pump (15); the first material pump (3) is arranged on the pipeline for transporting the sake raw materials at the outlet of the balance cylinder (1); the second material pump (15) is arranged on the return pipeline for transporting the sake raw materials close to the first plate heat exchanger (G); the balance cylinder (1) is provided with a liquid level meter (5); the pipeline for transporting the sake raw materials on the feeding side of the first material pump (3) is provided with an electric conductivity meter (2), and the pipeline for transporting the sake raw materials on the discharging side is provided with an electromagnetic flowmeter (4).

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