CN205501261U - Beer saccharification system - Google Patents
Beer saccharification system Download PDFInfo
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- CN205501261U CN205501261U CN201620127575.4U CN201620127575U CN205501261U CN 205501261 U CN205501261 U CN 205501261U CN 201620127575 U CN201620127575 U CN 201620127575U CN 205501261 U CN205501261 U CN 205501261U
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- mash
- thick bamboo
- section
- boiling pot
- cylinder
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The utility model discloses a beer saccharification system, including a mash section of thick bamboo and with a mash section of thick bamboo is connected strains a section of thick bamboo, the output of straining a section of thick bamboo has the pot of boiling through the tube coupling, boil the pot and be connected with the mixing box through the pipeline, still include the hot -water tank, the hot -water tank with be provided with the heat exchanger between the mixing box a mash section of thick bamboo with boil and be provided with first wheat juice pump between the pot boil the pot with be provided with second wheat juice pump between the mixing box strain a section of thick bamboo with be provided with the rabbling mechanism in the mash section of thick bamboo respectively boil the inside heating mechanism that is provided with of pot a mash section of thick bamboo, strain a section of thick bamboo, boil and be provided with the manometer on the pot respectively. The utility model discloses an adopt a mash section of thick bamboo to carry out the saccharification gelatinization to the material to the adoption is strained transparency that a section of thick bamboo improves wheat juice and is gone out the juice rate, and adopts and boil the pot and realize the operation of boiling to wheat juice, and through the mixing box realize the coagulum subside condense, can improve the quality of beer.
Description
Technical field
This utility model relates to a kind of beer saccharification system.
Background technology
Existing beer saccharification device generally uses and is separately provided, and each step uses independent heat supply, causes the energy
Waste, production cost increases.
Summary of the invention
The purpose of this utility model is to provide a kind of beer saccharification system, it is possible to improve asking of prior art existence
Topic, by using mash cylinder that material carries out saccharifying gelatinizing, and uses filter cylinder improve the transparency of wheat juice and go out
Juice rate, and use boiling pot realization that wheat juice boils operation, and realize coagulative sedimentation by blending bin
Cohesion, by boiler and heat exchanger structure, it is achieved to system heat supply, it is possible to increase the quality of medicated beer.
This utility model is achieved through the following technical solutions:
A kind of beer saccharification system, including mash cylinder and the filter cylinder that is connected with described mash cylinder, described
The outfan of filter cylinder connected by pipeline and have boiling pot, described boiling pot is connected with blending bin by pipeline
Connect, also include boiler, between described boiler and described blending bin, be provided with heat exchanger, described
The first wheat juice pump it is provided with, in described boiling pot and described mixing between mash cylinder and described boiling pot
It is provided with the second wheat juice pump between case, in described filter cylinder and described mash cylinder, is respectively arranged with blender
Structure, is internally provided with heating arrangements at described boiling pot, on described mash cylinder, filter cylinder, boiling pot
It is respectively arranged with Pressure gauge.
Further, for this utility model is better achieved, on the output pipe of described mash cylinder respectively
It is provided with flowmeter for pipe.
Further, for this utility model is better achieved, described boiling pot is by pipeline and described heat exchange
Device is connected.
Further, for this utility model is better achieved, described boiling pot is by pipeline and described hot water
Case is connected.
Further, for this utility model is better achieved, described boiler is provided with heat-exchanger pump, institute
The hot water delivery side of pump stated is connected with described boiling pot and described heat exchanger respectively.
This utility model compared with prior art, has the advantages that
(1) this utility model is by being connected mash cylinder with filter cylinder, carries out saccharifying in mash cylinder
During gelatinizing, make the maximized conversion of biological activity and the catalysis of various enzyme such that it is able to be effectively improved
Product quality, improves the yield rate of product；
(2) this utility model is by processing wheat juice by boiling pot, makes to boil wheat juice real with polymer
Existing sharp separation, promotes the polymerization of the condensable materials such as protein, it is possible to be effectively improved product quality；
(3) this utility model can facilitate coagulative sedimentation and solidification by arranging blending bin, it is achieved more preferably
Ground separating effect, uses boiler heat exchanger conveying hot water simultaneously, utilizes heat exchanger to realize carrying out blending bin
Heat supply, it is possible to increase the recovery rate of wheat juice, reduces environmental pollution.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme of this utility model embodiment, below will be to required in embodiment
The accompanying drawing used is briefly described, it will be appreciated that the following drawings illustrate only some enforcement of the present utility model
Example, is therefore not construed as the restriction to scope, for those of ordinary skill in the art, is not paying
On the premise of creative work, it is also possible to obtain other relevant accompanying drawings according to these accompanying drawings.
Fig. 1 is this utility model overall structure schematic diagram.
Wherein: 101. mash cylinders, 102. filter cylinders, 103. boiling pots, 104. blending bins, 105. boilers,
106. first wheat juice pumps, 107. heat-exchanger pumps, 108. heat exchangers, 109. second wheat juice pumps, 110. flowmeter for pipe.
Detailed description of the invention
Below in conjunction with specific embodiment, this utility model is described in further detail, but reality of the present utility model
The mode of executing is not limited to this.
Embodiment 1:
As it is shown in figure 1, a kind of beer saccharification system, including mash cylinder 101 and with described mash cylinder
The filter cylinder 102 that 101 are connected, the outfan of described filter cylinder 102 is connected by pipeline boiling pot 103,
Described boiling pot 103 is connected with blending bin 104 by pipeline, also includes boiler 105, described heat
Be provided with heat exchanger 108 between water tank 105 and described blending bin 104, described mash cylinder 101 with
It is provided with the first wheat juice pump 106 between described boiling pot 103, mixes with described at described boiling pot 103
The second wheat juice pump 109 it is provided with, at described filter cylinder 102 and described mash cylinder 101 between mould assembling 104
Inside it is respectively arranged with rabbling mechanism, is internally provided with heating arrangements at described boiling pot 103, in described wheat
It is respectively arranged with Pressure gauge on bud slurry cylinder 101, filter cylinder 102, boiling pot 103.
This utility model, by being connected with filter cylinder by mash cylinder, carries out saccharifying and gelatinizing in mash cylinder
During, make the maximized conversion of biological activity and the catalysis of various enzyme such that it is able to be effectively improved product matter
Amount, improves the yield rate of product；This utility model, by being processed by boiling pot by wheat juice, makes to boil wheat
Juice and polymer realize sharp separation, promote the polymerization of the condensable materials such as protein, it is possible to be effectively improved product quality；
This utility model can facilitate coagulative sedimentation and solidification by arranging blending bin, it is achieved preferably separates effect
Really, use boiler heat exchanger conveying hot water simultaneously, utilize heat exchanger to realize blending bin is carried out heat supply, energy
Enough improve the recovery rate of wheat juice, reduce environmental pollution.
Embodiment 2:
The present embodiment is on the basis of embodiment 1, in order to preferably wheat juice output is controlled, this
In embodiment, it is preferable that be respectively arranged with flowmeter for pipe on the output pipe of described mash cylinder 101
110。
In order to make boiling pot can be maintained at certain heat so that it is have and preferably boil intensity, in the present embodiment,
Preferably, described boiling pot is connected with described heat exchanger by pipeline.Delivery due to boiler
To heat exchanger, between the pipeline and heat exchanger of boiling pot, carry out heat exchange, it is possible to make it keep higher temperature,
Conveniently boiling pot is heated.
In order to enable boiler to provide hot water for boiling pot, reduce the power consumption of its internal heating arrangements, this enforcement
In example, it is preferable that described boiling pot is connected with described boiler by pipeline.
In the present embodiment, in order to make the more efficient output of hot water, it is preferable that set on described boiler
Being equipped with heat-exchanger pump, described hot water delivery side of pump is connected with described boiling pot and described heat exchanger respectively
Connect.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model, right
For those skilled in the art, this utility model can have various modifications and variations.All at this utility model
Spirit and principle within, any modification, equivalent substitution and improvement etc. made, should be included in this practicality new
Within the protection domain of type.
Claims (5)
1. a beer saccharification system, including mash cylinder and the filter cylinder that is connected with described mash cylinder, institute
The outfan of the filter cylinder stated is connected by pipeline boiling pot, and described boiling pot is connected with blending bin by pipeline
Connect, also include boiler, between described boiler and described blending bin, be provided with heat exchanger, described
The first wheat juice pump it is provided with, in described boiling pot and described mixing between mash cylinder and described boiling pot
It is provided with the second wheat juice pump between case, in described filter cylinder and described mash cylinder, is respectively arranged with blender
Structure, is internally provided with heating arrangements at described boiling pot, on described mash cylinder, filter cylinder, boiling pot
It is respectively arranged with Pressure gauge.
A kind of beer saccharification system the most according to claim 1, it is characterised in that: in described mash
It is respectively arranged with flowmeter for pipe on the output pipe of cylinder.
A kind of beer saccharification system the most according to claim 1, it is characterised in that: described boiling pot leads to
Cross pipeline to be connected with described heat exchanger.
A kind of beer saccharification system the most according to claim 1, it is characterised in that: described boiling pot leads to
Cross pipeline to be connected with described boiler.
A kind of beer saccharification system the most according to claim 4, it is characterised in that: at described boiler
On be provided with heat-exchanger pump, described hot water delivery side of pump respectively with described boiling pot and described heat exchanger phase
Connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620127575.4U CN205501261U (en) | 2016-02-19 | 2016-02-19 | Beer saccharification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620127575.4U CN205501261U (en) | 2016-02-19 | 2016-02-19 | Beer saccharification system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205501261U true CN205501261U (en) | 2016-08-24 |
Family
ID=56725348
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620127575.4U Active CN205501261U (en) | 2016-02-19 | 2016-02-19 | Beer saccharification system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205501261U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115044428A (en) * | 2022-06-23 | 2022-09-13 | 华润雪花啤酒（中国）有限公司 | Beer saccharification system device and control method thereof |
-
2016
- 2016-02-19 CN CN201620127575.4U patent/CN205501261U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115044428A (en) * | 2022-06-23 | 2022-09-13 | 华润雪花啤酒（中国）有限公司 | Beer saccharification system device and control method thereof |
| CN115044428B (en) * | 2022-06-23 | 2024-06-11 | 华润雪花啤酒（中国）有限公司 | System device for saccharification of beer and control method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 311507 No. 551 Tangchuan Road, Tonglu Economic Development Zone, Tonglu County, Hangzhou City, Zhejiang Province Patentee after: Hangzhou Zhengjiu Machinery Manufacturing Co., Ltd. Address before: 311407 Shuizhukeng 82-18, Nanshan Village, Lushan Street, Fuyang District, Hangzhou City, Zhejiang Province Patentee before: Hangzhou Zhengjiu Machinery Manufacturing Co., Ltd. |
|
| CP03 | Change of name, title or address |