CN212713447U - Edible vinegar automated production system - Google Patents

Abstract

The utility model relates to an automatic production system of edible vinegar, the outlet of the discharge elephant trunk and a vinegar back flow of a plurality of fermentation tanks are connected with the inlet of a vinegar unstrained spirits delivery pump together, the outlet of the vinegar unstrained spirits delivery pump is connected with each vinegar unstrained spirits sieve through a vinegar unstrained spirits delivery pipe, the liquid phase outlet of each vinegar unstrained spirits sieve is connected with the inlet of a vinegar circulating pump respectively, the outlet of each vinegar circulating pump is connected with the inlet of a vinegar tank respectively, the outlet of the vinegar tank is connected with a vinegar preparing working section and a vinegar back flow through a vinegar pump; the solid phase outlet of each vinegar mash sieve is respectively connected with the inlet of a vinegar pouring tank, and the filtrate outlet of each vinegar pouring tank is connected with the inlet of a vinegar circulating pump. The outlet of each vinegar circulating pump is also respectively connected with the inlet of the second vinegar tank, the outlet of the second vinegar tank is connected with the medium inlet of the heat exchanger through the second vinegar pump, and the medium outlet of the heat exchanger is connected with the top inlet of each vinegar pouring tank. The system can reduce labor intensity, improve output rate, and has good product quality and high production efficiency.

Description

Edible vinegar automated production system

Technical Field

The utility model relates to a production system of edible vinegar, in particular to edible vinegar automated production system belongs to edible vinegar production technical field.

Background

The traditional edible vinegar production mode is simple, still adopts a workshop-type production mode, uses open-type operation, has poor production environment sanitary conditions, reduces the product quality and increases the production cost of an edible vinegar factory; and the automatic production can not be realized, and the labor intensity is high. Overall, the workshop-type production has the following disadvantages:

the method has the advantages that the used equipment is simple and crude, the process is discontinuous, and automatic operation cannot be adopted;

the intermediate materials are generally conveyed by a rickshaw and a movable belt conveyor, so that the transportation sanitary condition is poor, the materials are thrown on the ground of a workshop, the workshop is serious in running, leakage and leakage, and the environmental sanitary condition is poor;

the intermediate materials are subjected to open type operation in the transportation and fermentation process, flies are easy to breed, and fly killing and fly prevention devices are added in workshops and doors and windows, but the breeding of flies cannot be avoided, so that the quality of products is influenced;

since the fermentation process of the intermediate materials is carried out in open equipment, a workshop has a great vinegar smell, and the physical health of operators is damaged;

the raw materials, the intermediate materials, the vinegar residue and the like are transported manually or semi-manually, and are conveyed by a rickshaw, a crane grab bucket or a movable belt conveyor, so that the labor intensity of operators is high;

sixthly, manually measuring fermentation parameters such as fermentation temperature and the like, wherein the detection error is large, the phenomenon of inaccurate measurement or untimely measurement exists, the fermentation environment cannot be automatically controlled, and manual detection is relied on;

the fermentation is carried out by using the traditional fermentation bed, the number of layers of fermentation equipment cannot be increased, the occupied area of a fermentation workshop is large, and the unit area output rate of a factory is low.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to overcome the problem that exists among the prior art, provide an edible vinegar automated production system, can realize automatic continuous production, operative employee's low in labor strength, site environment sanitary condition is good, and product quality is good, and production efficiency is high.

In order to solve the technical problem, the utility model discloses an automatic production system of edible vinegar, including a plurality of fermentation tanks, the export of the ejection of compact elephant trunk of each fermentation tank and vinegar back flow is continuous with the entry of portable vinegar unstrained spirits delivery pump jointly, and the export of portable vinegar unstrained spirits delivery pump links to each other with the entry of vinegar unstrained spirits conveyer pipe, the export of vinegar unstrained spirits conveyer pipe links to each other with the entry of vinegar unstrained spirits sieve, and the liquid phase outlet of vinegar unstrained spirits sieve links to each other with the entry of corresponding vinegar circulating pump respectively, and the export of vinegar circulating pump links to each other with the entry of vinegar jar respectively, the export of vinegar jar reaches vinegar back flow through vinegar pump and vinegar allotment workshop section together one; the solid phase outlet of each vinegar mash sieve is respectively connected with the inlet of a vinegar pouring tank, and the filtrate outlet of each vinegar pouring tank is connected with the inlet of a corresponding vinegar circulating pump.

Compared with the prior art, the utility model discloses following beneficial effect has been obtained: the fermenters can be discharged in multiple layers, rows and columns to increase yield. The mixed auxiliary materials and the fermented glutinous rice are fermented in fermentation tanks, after fermentation of a certain fermentation tank is finished, the vinegar mash is discharged into an inlet of a movable vinegar mash conveying pump from a discharge chute, a vinegar flows out from a vinegar return pipe and also enters the inlet of the movable vinegar mash conveying pump, and the solid and the liquid are mixed and then are convenient to convey; the outlet of the movable vinegar culture conveying pump is connected with a vinegar culture conveying pipe through a hose quick connector, vinegar culture and vinegar flow into each vinegar culture sieve along the vinegar culture conveying pipe under the conveying of the movable vinegar culture conveying pump, solid-liquid separation is realized, vinegar flows out from the liquid phase outlet of the vinegar culture sieve, the vinegar is sent into a vinegar tank for temporary storage through a vinegar circulating pump, after the vinegar is pumped out by a vinegar pump, the vinegar can be sent into a next procedure, namely a vinegar blending section, and a vinegar return pipe can be returned to continue to be mixed with the vinegar culture for conveying. The vinegar mash separated by the vinegar mash sieve enters a vinegar pouring tank, and a piece of vinegar poured out is pumped out by a vinegar circulating pump; and continuously soaking the vinegar mash by using the second vinegar, continuously discharging the first vinegar obtained after soaking from a filtrate outlet of the vinegar pouring tank, and conveying the first vinegar into the first vinegar tank for temporary storage by using a vinegar circulating pump. The system adopts the butt joint of the movable vinegar culture delivery pump and the discharge chutes of the fermentation tanks, and the vinegar culture adopts the pumping, so that the throwing of manual transportation is avoided, the environmental sanitation condition is greatly improved, the fly breeding caused by material exposure is avoided, the product quality and the production efficiency are improved, and the labor intensity of operators is reduced.

As the improvement of the utility model, the solid phase outlet of each vinegar pouring tank and the outlet of the circulating water pipe are connected with the inlet of the corresponding vinegar lees pump, the outlet of each vinegar lees pump is connected with the inlet of the vinegar lees sieve, the liquid phase outlet of the vinegar lees sieve is connected with the inlet of the circulating water tank, and the outlet of the circulating water tank is connected with the circulating water pipe through the circulating water pump. The first conveying mode of the vinegar residue is that circulating water from a circulating water pipe and the vinegar residue discharged from a vinegar pouring tank enter an inlet of a vinegar residue pump together, the circulating water and the vinegar residue are mixed and then are convenient to pump, the vinegar residue pump conveys the vinegar residue into a vinegar residue sieve along with water flow for solid-liquid separation, the separated circulating water enters a circulating water tank for temporary storage, and the circulating water is conveyed back to the circulating water pipe by the circulating water pump for continuous circulation, so that the automatic conveying of the vinegar residue is realized.

As a further improvement of the utility model, the solid phase outlet of the vinegar residue sieve is connected with the inlet of the squeezing machine, and the liquid phase outlet of the squeezing machine is connected with the inlet of the circulating water tank. The vinegar residue separated by the vinegar residue sieve enters a squeezing machine for further dehydration, the dehydrated circulating water enters a circulating water tank from a liquid phase outlet of the squeezing machine for collection, and the dehydrated vinegar residue is convenient for long-distance transportation.

As a further improvement of the utility model, the solid phase outlet of each vinegar pouring tank is connected with the material inlet of the air seal machine, the air outlet of the Roots blower is connected with the air inlet of the air seal machine, and the outlet of the air seal machine is connected with the vinegar lees air supply pipe. The second conveying mode of the vinegar residue is that the vinegar residue discharged from the vinegar pouring tank enters a material inlet of the air seal machine, and is conveyed outwards by compressed air discharged by a Roots blower.

As the further improvement of the utility model, each the export of vinegar circulating pump still links to each other with the entry of two vinegar jars respectively, the export of two vinegar jars links to each other through the medium entry of two vinegar pumps with the heat exchanger, the medium export of heat exchanger with soak vinegar pipe and link to each other, soak the export of vinegar pipe respectively with each the top entry of drenching the vinegar jar links to each other. The vinegar in the vinegar tank is pumped out by a vinegar pump, heated by a heat exchanger, enters the vinegar pouring tank from the vinegar soaking pipe to soak the vinegar grains for the first time, and is sent into the vinegar tank for temporary storage by a vinegar circulating pump, so that the yield of vinegar in the first time can be improved.

As a further improvement of the utility model, the clean water pipe is connected with the inlet of the clean water tank, and the outlet of the clean water tank is connected with the medium inlet of the heat exchanger through the clean water pump; the outlet of each vinegar circulating pump is also respectively connected with the inlet of a three-way vinegar tank, and the outlet of the three-way vinegar tank is connected with the medium inlet of the heat exchanger through a three-way vinegar pump. And the vinegar in the three vinegar tanks is pumped out by a vinegar pump, heated by a heat exchanger, enters the vinegar pouring tank from the vinegar soaking pipe to carry out secondary soaking on the vinegar grains, secondary soaking is carried out to obtain secondary vinegar, and the secondary vinegar is conveyed into the secondary vinegar tank by a vinegar circulating pump to be temporarily stored. Clear water in the clear water tank is pumped into the heat exchanger by a clear water pump to be heated, and then enters the vinegar pouring tank from the vinegar dipping pipe to carry out the third soaking on the vinegar grains, three vinegar are obtained after the third soaking, and the vinegar is pumped into the three vinegar tanks by a vinegar circulating pump to be temporarily stored. So that the vinegar can be extracted in grades and in sequence, and the product yield is improved.

As a further improvement of the utility model, the bottoms of the vinegar pouring tanks are respectively connected with a steam pipe through steam valves. The unsteamed vinegar is used for producing aromatic vinegar; after vinegar liquid in each vinegar pouring tank is drained, steam is adopted for fumigation, and the fumigated vinegar mash can be used for producing mature vinegar.

As a further improvement of the utility model, the wine mash feed pipe links to each other with the entry of wine mash jar, the export of wine mash jar is passed through the wine mash pump and is linked to each other with the wine mash conveyer pipe, and the wine mash conveyer pipe links to each other with the feed inlet of each fermentation cylinder jointly with mixing the auxiliary material wind and sending the pipe, and the inlet and the clear water pipe of each fermentation cylinder reach the wine mash conveyer pipe links to each other, and the steam inlet of each fermentation cylinder links to each other with the steam pipe. The mixed auxiliary materials are conveyed into the feeding hole of the fermentation tank through the mixed auxiliary material conveying pipe, simultaneously, the wine mash in the wine mash tank is conveyed out through the wine mash conveying pipe by the wine mash pump, and after being mixed with the mixed auxiliary materials, the mixed auxiliary materials and the wine mash enter the feeding hole of the fermentation tank together, so that dust generated by feeding can be reduced. After the mixed auxiliary materials are fed, the wine mash is continuously input, and the mixed auxiliary materials are immersed into the fermentation. After the fermentation is finished and the material is discharged, clear water can be input to clean the fermentation tank, and then steam is introduced to sterilize.

Drawings

The invention will be described in further detail with reference to the drawings and the detailed description, which are provided for reference and illustration purposes only and are not intended to limit the invention.

FIG. 1 is a flow chart of a fermentation section in an automatic production system of edible vinegar.

FIG. 2 is a flow chart of a first embodiment of the vinegar pouring section of the present invention.

FIG. 3 is a flow chart of the second embodiment of the vinegar pouring section of the present invention.

In the figure: 1. a mash tank; 2. a fermentation tank; 2a, discharging chute; 3. sieving the vinegar grains; 4. a vinegar pouring tank; 5. a vinegar tank; 6. a second vinegar tank; 7. three vinegar pots; 8. a heat exchanger; 9. a clean water tank; 10. sieving vinegar residue; 11. a circulating water tank; 12. a squeezing machine; 13. a Roots blower; 14. a wind seal machine; 15. a vinegar blending section; G1. a mash feed pipe; G2. a mash delivery pipe; G3. conveying the mixed auxiliary material into a pipe; G4. a clear water pipe; G5. a steam pipe; G6. a conveying pipe for vinegar grains; G7. a vinegar return pipe; G8. a vinegar soaking pipe; G9. a circulating water pipe; G10. conveying the vinegar residue into a pipe by wind; B1. a mash pump; B2. a movable vinegar grain delivery pump; B3. a vinegar circulating pump; B4. a vinegar pump; B5. a second vinegar pump; B6. a vinegar pump; B7. a clean water pump; B8. a vinegar residue pump; B9. and (4) a water circulating pump.

Detailed Description

As shown in fig. 1 and 2, the utility model discloses an edible vinegar automated production system includes a plurality of fermentation tanks 2, fermentation tank 2 can the multilayer multirow multiseriate discharge, wine mash feed pipe G1 links to each other with wine mash jar 1's entry, wine mash jar 1's export is passed through wine mash pump B1 and is linked to each other with wine mash conveyer pipe G2, wine mash conveyer pipe G2 links to each other with the feed inlet of mixing supplementary material wind conveying pipe G3 with each fermentation tank 2 jointly, each fermentation tank 2's inlet links to each other with clear water pipe G4 and wine mash conveyer pipe G2, each fermentation tank 2's steam inlet links to each other with steam pipe G5. The outlet of the discharge chute 2a of each fermentation tank 2 and the outlet of a vinegar return pipe G7 are connected with the inlet of a movable vinegar mash conveying pump B2, and the outlet of the movable vinegar mash conveying pump B2 is connected with the inlet of a vinegar mash conveying pipe G6.

The mixed auxiliary materials are conveyed into the feed port of the fermentation tank 2 through the mixed auxiliary material conveying pipe G3, simultaneously, the wine mash in the wine mash tank 1 is conveyed out through the wine mash conveying pipe G2 by the wine mash pump B1, and after being mixed with the mixed auxiliary materials, the mixed auxiliary materials enter the feed port of the fermentation tank 2 together, so that the dust generated by feeding can be reduced. After the mixed auxiliary materials are fed, the wine mash is continuously input, and the mixed auxiliary materials are immersed into the fermentation. After fermentation of a certain fermentation tank 2 is finished, vinegar grains are discharged into an inlet of a movable vinegar grain conveying pump B2 from a discharge chute 2a, a vinegar flow-out pipe G7 flows out of a vinegar return pipe and also enters an inlet of a movable vinegar grain conveying pump B2, and solid and liquid are mixed and then are convenient to convey; the outlet of the movable vinegar mash conveying pump B2 is connected with a vinegar mash conveying pipe G6 through a hose quick connector. After the fermentation is finished and the material is discharged, clear water can be input to clean the fermentation tank 2, and then steam is introduced to sterilize.

As shown in fig. 2, the outlet of the vinegar culture delivery pipe G6 is connected with the inlet of each vinegar culture sieve 3, the liquid phase outlet of each vinegar culture sieve 3 is respectively connected with the inlet of the corresponding vinegar circulating pump B3, the outlet of each vinegar circulating pump B3 is respectively connected with the inlet of a vinegar tank 5, and the outlet of the vinegar tank 5 is connected with a vinegar blending section 15 and a vinegar return pipe G7 through a vinegar pump B4; the solid phase outlet of each vinegar mash sieve 3 is respectively connected with the inlet of a vinegar pouring tank 4, and the filtrate outlet of each vinegar pouring tank 4 is connected with the inlet of a corresponding vinegar circulating pump B3.

The solid phase outlet of each vinegar pouring tank 4 and the outlet of the circulating water pipe G9 are connected with the inlet of the corresponding vinegar residue pump B8, the outlet of each vinegar residue pump B8 is connected with the inlet of the vinegar residue sieve 10, the liquid phase outlet of the vinegar residue sieve 10 is connected with the inlet of the circulating water tank 11, and the outlet of the circulating water tank 11 is connected with the circulating water pipe G9 through the circulating water pump B9. The solid phase outlet of the vinegar residue sieve 10 is connected with the inlet of the wringing machine 12, and the liquid phase outlet of the wringing machine 12 is connected with the inlet of the circulating water tank 11.

The vinegar mash and a vinegar flow into each vinegar mash sieve 3 along a vinegar mash conveying pipe G6 under the conveying of a movable vinegar mash conveying pump B2, solid-liquid separation is realized, a vinegar flow flows out from a liquid phase outlet of the vinegar mash sieve 3 and is conveyed into a vinegar tank 5 by a vinegar circulating pump B3 for temporary storage, a vinegar pump B4 can convey a vinegar into a next procedure, namely a vinegar blending procedure 15, and the vinegar flow can return to a vinegar return pipe G7 to continue to be mixed with the vinegar mash for conveying. The vinegar mash separated by the vinegar mash sieve 3 enters a vinegar pouring tank 4, and a piece of vinegar poured out is pumped out by a vinegar circulating pump B3; the vinegar mash is continuously soaked by the second vinegar, and the primary vinegar obtained after soaking is continuously discharged from a filtrate outlet of the vinegar pouring tank 4 and is still sent into the primary vinegar tank 5 by a vinegar circulating pump B3 for temporary storage. The system adopts the movable vinegar culture delivery pump B2 to be butted with the discharge chutes 2a of the fermentation tanks 2, and the vinegar culture is pumped, so that the throwing of manual transportation is avoided, the environmental sanitation condition is greatly improved, the fly breeding caused by material exposure is avoided, the product quality and the production efficiency are improved, and the labor intensity of operators is reduced.

The first conveying mode of the vinegar residue is that the circulating water from the circulating water pipe G9 and the vinegar residue discharged from the vinegar pouring tank 4 enter the inlet of the vinegar residue pump B8 together, the mixture is convenient for pumping, the vinegar residue pump B8 conveys the vinegar residue into the vinegar residue sieve 10 along with the water flow for solid-liquid separation, the separated circulating water enters the circulating water tank 11 for temporary storage, and the circulating water is conveyed back to the circulating water pipe G9 by the circulating water pump B9 for continuous circulation, so that the automatic conveying of the vinegar residue is realized. The vinegar residue separated by the vinegar residue sieve 10 enters a squeezing machine 12 for further dehydration, the dehydrated circulating water enters a circulating water tank 11 from a liquid phase outlet of the squeezing machine 12 for collection, and the dehydrated vinegar residue is convenient for long-distance transportation.

The outlet of each vinegar circulating pump B3 is also connected with the inlet of the second vinegar tank 6, the outlet of the second vinegar tank 6 is connected with the medium inlet of the heat exchanger 8 through a second vinegar pump B5, the medium outlet of the heat exchanger 8 is connected with a vinegar soaking pipe G8, and the outlet of the vinegar soaking pipe G8 is connected with the top inlet of each vinegar pouring tank 4.

The clean water pipe G4 is connected with the inlet of the clean water tank 9, and the outlet of the clean water tank 9 is connected with the medium inlet of the heat exchanger 8 through a clean water pump B7; the outlet of each vinegar circulating pump B3 is also respectively connected with the inlet of the three vinegar tanks 7, and the outlet of the three vinegar tanks 7 is connected with the medium inlet of the heat exchanger 8 through the three vinegar pumps B6.

The second vinegar stored in the second vinegar tank 6 is sent out by a second vinegar pump B5, heated by a heat exchanger 8, enters the vinegar pouring tank 4 from a vinegar dipping pipe G8 to carry out primary soaking on the vinegar grains, a vinegar is obtained after primary soaking, and is sent into the vinegar tank 5 by a vinegar circulating pump B3 to be temporarily stored.

The three vinegar stored in the three vinegar tanks 7 are sent out by a three vinegar pump B6, heated by a heat exchanger 8, enter the vinegar pouring tank 4 from a vinegar dipping pipe G8 to carry out secondary soaking on the vinegar mash, obtain secondary vinegar after secondary soaking, and are sent into a secondary vinegar tank 6 by a vinegar circulating pump B3 to be temporarily stored. Clear water in the clear water tank 9 is sent into the heat exchanger 8 by a clear water pump B7 to be heated, then enters the vinegar pouring tank 4 from the vinegar dipping pipe G8 to carry out the third soaking on the vinegar grains, three vinegar are obtained after the third soaking, and the vinegar is sent into the three vinegar tanks 7 by a vinegar circulating pump B3 to be temporarily stored. So that the vinegar can be extracted in grades and in sequence, and the product yield is improved.

The bottom of each vinegar pouring tank 4 is respectively connected with a steam pipe G5 through a steam valve. The unsteamed vinegar is used for producing aromatic vinegar; after the vinegar liquid in each vinegar pouring tank 4 is drained, steam is adopted for fumigation, and the fumigated vinegar mash can be used for producing mature vinegar.

As shown in fig. 3, the second transportation mode of the vinegar residue is that the solid phase outlet of each vinegar pouring tank 4 is connected with the material inlet of the air seal machine 14, the air outlet of the roots blower 13 is connected with the air inlet of the air seal machine 14, and the outlet of the air seal machine 14 is connected with the vinegar residue air conveying pipe G10. The vinegar residue discharged from the vinegar pouring tank 4 enters a material inlet of an air seal machine 14, and is sent to a vinegar residue air conveying pipe G10 to be conveyed outwards by compressed air discharged by a Roots blower 13.

The above description is only a preferred embodiment of the present invention, and not intended to limit the scope of the present invention. In addition to the above embodiments, the present invention can also have other embodiments, and all technical solutions formed by equivalent replacement or equivalent transformation fall within the protection scope of the present invention. The undescribed technical features of the present invention can be realized by or using the prior art, and are not described herein again.

Claims (8)

1. The utility model provides an edible vinegar automated production system, includes a plurality of fermentation tanks, its characterized in that: the discharge chute of each fermentation tank and the outlet of a vinegar return pipe are connected with the inlet of a movable vinegar culture conveying pump, the outlet of the movable vinegar culture conveying pump is connected with the inlet of a vinegar culture conveying pipe, the outlet of the vinegar culture conveying pipe is connected with the inlet of each vinegar culture sieve, the liquid phase outlet of each vinegar culture sieve is connected with the inlet of a corresponding vinegar circulating pump, the outlet of each vinegar circulating pump is connected with the inlet of a vinegar tank, and the outlet of the vinegar tank is connected with a vinegar blending section and the vinegar return pipe through a vinegar pump; the solid phase outlet of each vinegar mash sieve is respectively connected with the inlet of a vinegar pouring tank, and the filtrate outlet of each vinegar pouring tank is connected with the inlet of a corresponding vinegar circulating pump.

2. The automated vinegar production system according to claim 1, wherein: the solid phase outlet of each vinegar pouring tank and the outlet of the circulating water pipe are connected with the inlet of the corresponding vinegar residue pump together, the outlet of each vinegar residue pump is connected with the inlet of the vinegar residue sieve respectively, the liquid phase outlet of the vinegar residue sieve is connected with the inlet of the circulating water tank, and the outlet of the circulating water tank is connected with the circulating water pipe through the circulating water pump.

3. The automated vinegar production system according to claim 2, wherein: and a solid phase outlet of the vinegar residue sieve is connected with an inlet of a squeezing machine, and a liquid phase outlet of the squeezing machine is connected with an inlet of the circulating water tank.

4. The automated vinegar production system according to claim 1, wherein: the solid phase outlet of each vinegar pouring tank is connected with the material inlet of the air seal machine, the air outlet of the Roots blower is connected with the air inlet of the air seal machine, and the outlet of the air seal machine is connected with the vinegar residue air supply pipe.

5. The automated vinegar production system according to claim 1, wherein: the outlet of each vinegar circulating pump is also respectively connected with the inlet of a secondary vinegar tank, the outlet of the secondary vinegar tank is connected with the medium inlet of a heat exchanger through a secondary vinegar pump, the medium outlet of the heat exchanger is connected with a vinegar soaking pipe, and the outlet of the vinegar soaking pipe is respectively connected with the top inlet of each vinegar pouring tank.

6. The automated vinegar production system according to claim 5, wherein: the clean water pipe is connected with the inlet of the clean water tank, and the outlet of the clean water tank is connected with the medium inlet of the heat exchanger through a clean water pump; the outlet of each vinegar circulating pump is also respectively connected with the inlet of a three-way vinegar tank, and the outlet of the three-way vinegar tank is connected with the medium inlet of the heat exchanger through a three-way vinegar pump.

7. The automated vinegar production system according to claim 1, wherein: the bottom of each vinegar pouring tank is connected with a steam pipe through a steam valve.

8. An automated vinegar production system according to any one of claims 1 to 7, wherein: the wine mash feeding pipe is connected with an inlet of a wine mash tank, an outlet of the wine mash tank is connected with a wine mash conveying pipe through a wine mash pump, the wine mash conveying pipe and a mixed auxiliary material air conveying pipe are jointly connected with feed inlets of the fermentation tanks, liquid inlets of the fermentation tanks are connected with a clear water pipe and the wine mash conveying pipe, and steam inlets of the fermentation tanks are connected with a steam pipe.

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