CN205821288U - A kind of compound saccharifying device for beer - Google Patents
A kind of compound saccharifying device for beer Download PDFInfo
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- CN205821288U CN205821288U CN201620570670.1U CN201620570670U CN205821288U CN 205821288 U CN205821288 U CN 205821288U CN 201620570670 U CN201620570670 U CN 201620570670U CN 205821288 U CN205821288 U CN 205821288U
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- pot
- convolution
- filter tank
- saccharifying
- beer
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The utility model discloses a kind of compound saccharifying device for beer, belong to technical field of beer fermentation equipment.Saccharifying device for beer includes saccharification boiling convolution pot, it is positioned at the heating interlayer outside saccharification boiling convolution pot bottom, it is positioned at the filter tank on saccharification boiling convolution pot top, convolution pot CIP system, filter tank CIP purging system and the centrifugal pump being connected with saccharification boiling convolution pot, filter tank, convolution pot CIP system and filter tank CIP purging system by pipeline.Wherein, the filter tank CIP purging system on filter tank top is connected with air pressure filtration system boost mouth；Described saccharification boiling convolution pot bottom is provided with a center discharging opening and an eccentric discharging opening.Heating interlayer is connected with the bottom of saccharification boiling convolution pot.It is little that saccharification apparatus of the present utility model has floor space, energy-efficient, the feature that filtration time is short, it is possible to production cost is greatly lowered, and improves production efficiency.
Description
Technical field
This utility model relates to a kind of compound saccharifying device for beer, belongs to brewery installation technical field.
Background technology
At present conventional beer brewing system, there is plane figure, to take plane space big；Use mechanical agitation mixing side
Formula, increases hardware cost high；External electricity steam boiler increases the technical problem such as hardware investment and occupation of land.Although being in saving space
Consideration, the brewing system of existing up-down structure, but existing conventional up-down structure brewing system, wort filtration is only
Self-flow filtering can be used, there is filtration time long, inefficiency, and there is saccharifying hot-spot in Electric heating,
Wheat wine with dregs and wheat juice easily boil paste phenomenon, and all pot devices are required to manually scrub, labor intensity and operation complexity.Additionally, it is existing
Conventional saccharifying system, because of structural reason after convolution terminates, the coarse sludge boiling generation is drawn into fermentation tank, reduces wine liquid
Quality.
Utility model content
For solving above-mentioned technical problem, this utility model provides a kind of compound saccharifying device for beer, the technology taked
Scheme is as follows:
The purpose of this utility model is to provide a kind of compound saccharifying device for beer, and this saccharifying device for beer includes that saccharifying is boiled
Boiling convolution pot 2, is positioned at the heating interlayer 1 of saccharification boiling convolution pot 2 bottom outside, is positioned at the mistake on saccharification boiling convolution pot 2 top
Filter pocket 6, pot CIP system 3 of circling round, filter tank CIP purging system 7 and by pipeline and saccharification boiling convolution pot 2, filter tank 6,
The centrifugal pump 15 that convolution pot CIP system 3 and filter tank CIP purging system 7 connect；Wherein, the filter tank CIP on filter tank 6 top
Purging system 7 is connected with air pressure filtration system boost mouth 8；It is provided with a center discharging opening bottom described saccharification boiling convolution pot 2
13 and an eccentric discharging opening 12；Described heating interlayer 1 is connected with the bottom of saccharification boiling convolution pot 2.
Preferably, the vertical height of described filter tank 6 is the height of saccharifying steaming and decocting convolution pot 2 straight tube, to ensure that mash exists
Filter under self gravitation effect.
Preferably, the side, top of described saccharifying steaming and decocting convolution pot 2 is provided with saccharifying dog-house 4.
Preferably, described filter tank 6 lower side be provided with filter tank go out grain mouth 5.
Preferably, the discharging opening bottom described filter tank 6 is connected with centrifugal pump 15 by being provided with the discharge nozzle of observation window 10.
Preferably, it is connected with the centrifugal pump 15 for sucking filtration bottom described filter tank 6, to realize sucking filtration or sucking filtration and gravity
The combination of effect.Additionally, can be with an ad hoc wheat juice pump for sucking filtration in the bottom of filter tank 6.
Preferably, the vertical pipeline bottom being connected with center discharging opening 13 is connected with centrifugal pump 15 by horizontal pipe, in
Portion is connected with the up-hill line of centrifugal pump 15 by axial return duct 14.
Preferably, the vertical pipeline being connected with eccentric discharging opening 12 is connected with centrifugal pump 15 by horizontal pipe.
Preferably, the up pipeline of centrifugal pump 15 is sequentially provided with the branch and saccharifying steaming and decocting being connected with axial return duct 14
The branch that the branch that the gyrotron 11 of convolution pot 2 connects is connected with convolution pot CIP system 3 is connected with filter tank side feeding mouth 9
Branch and the branch that is connected with filter tank CIP purging system 7.
Saccharifying device for beer described in claim 1, it is characterised in that separate pump 15 horizontal pipeline respectively with filter tank
The vertical connecting tube of 6 discharge nozzles, the eccentric vertical connecting tube of discharging opening 12 and center discharging opening 13 connects.
This utility model obtains and provides the benefit that:
This utility model uses duplex, reduces saccharifying system footprint area, improves unit are production capacity；Use
Radial and axial pressure outer circulation substitutes convention stir, it is achieved mash solid mixes, and reduces hardware cost, improves mixing efficiency；
Use interlayer self-produced steam heating technique, it is to avoid electric heating tube directly heats brought mash and easily boils paste problem, it is to avoid steaming
Electric steam boiler needed for vapour heating, meanwhile, heated sealed realizes the backflow certainly of condensed water, reduces power consumption；Use CIP system,
Realize pot automatization to clean, reduce labor intensity, improve cleaning performance；Self-flow filtering, pumping filter, air pressure filter pressing triple filter
Mode is highly integrated, and flexible Application improves filter efficiency, reduces filtration time；Saccharifying-boil-circle round pot use eccentric double go out
Mouthful, realize coarse sludge in convolution end and completely separate.
The saccharifying of compound saccharifying device for beer provided by the utility model-boil-circle round the folders such as pot employing self-produced steam
Layer mode of heating, it is achieved the heating etc. to material, completes whole saccharifying and controls；Saccharifying mash completely passes through centrifugal pump by mash
It is pumped to the filter tank on upper strata；Mash in filter tank passes through, from one or more groups such as heavy filtration, pumping filter or pressure filtrations
Conjunction mode realizes the filtration of wheat juice, obtains the wheat juice of clarification and enters saccharifying-boil-circle round pot.The wheat juice of clarification is in saccharifying-boil
Boiling-convolution pot realizes stablizing of wheat juice by the way of interlayer self-produced steam voltage stabilizing filtration and boils；The wheat juice boiling end passes through
The mode of self-loopa convolution realizes convolution sedimentation；After convolution terminates, realized by the eccentric discharging opening of saccharifying-boil-circle round pot
The derivation of hot wheat juice, and without walking coarse sludge, improve the quality of wheat juice.After clarification wheat juice is derived completely, by CIP system
The cleaning of pot of having united, it is ensured that pot health.
Concrete has the beneficial effect that:
1., by interlayer self-produced steam, certainly it is heated at reflux mode, the mode of the most conventional external steam boiler heating, power consumption
Amount falls about 10% on a year-on-year basis；
2. filtered by pumping or the mode such as pressure filtration realizes filtration time reduction about 1h；
3. boiling part constant voltage is boiled, and stablizes boiling part, it is to avoid overflow pot；
4. eccentric discharging opening side discharging, is fully drawn out clarification wheat juice, and the loss of existing weaponry and equipment saccharification wort declines on year-on-year basis
5%；
5. the total tune cooperation integral production time falls about 2-4h on a year-on-year basis；
6. use self-produced steam Isobarically Control technique to realize heating process without row outside excess steam, reduction working place humidity
And temperature, improve operating environment, reduce energy consumption, improve processing safety.
Accompanying drawing explanation
Fig. 1 be compound mashing device of the present utility model face structural representation.
In figure: 1, heating interlayer；2, saccharifying steaming and decocting convolution pot；3, pot CIP system of circling round；4, saccharifying dog-house；5, filter
Groove goes out grain mouth；6, filter tank；7, filter tank CIP purging system；8, air pressure filtration system boost mouth；9, filter tank side feeding mouth；
10, observation window；11, gyrotron；12, eccentric discharging opening；13, center discharging opening；14, axial return duct；15, centrifugal pump.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is described in further details, but described further below be not new to this practicality
The restriction of type.
Fig. 1 be the compound mashing device in a kind of preferred version of this utility model face structural representation.From Fig. 1
In understand, this compound saccharifying device for beer mainly by saccharification boiling circle round pot 2, heating interlayer 1, filter tank 6, centrifugal pump 15 and
Connect the pipeline composition of each critical piece.Wherein, filter tank 6 and saccharification boiling convolution pot 2 are respectively equipped with filter tank CIP and clean 7
System and convolution pot CIP system 3, to realize the automatic cleaning of above-mentioned two parts, reduce labor intensity and cost of labor.Saccharifying is boiled
Boiling convolution pot 2 is positioned at the bottom of filter tank 6, and the lower outside at saccharification boiling convolution pot 2 is provided with one and possesses self-produced steam merit
The heating interlayer 1 of energy, in order to realize the efficient utilization of steam thermal energy.It is provided with one in the side, top of saccharification boiling convolution pot 2
For throwing in the saccharifying dog-house 4 of saccharifying material.Correspondingly, the side, bottom at filter tank 6 is provided with one and is easy to remove and does not filters
The filter tank crossing solids goes out grain mouth 5.
The vertical height of filter tank 6 is saccharification boiling convolution pot 2 straight tube height, in order to the deadweight of filtrate in filter tank 6
Filter.Wheat juice pump also can be provided with, in order to by the way of sucking filtration, accelerate filter course in the bottom of filter tank 6.Meanwhile, it is positioned at
The filter tank CIP purging system 7 at filter tank 6 top connects with air pressure filtration system boost mouth 8 also by pipeline, can realize mistake
Pressurized treatments is carried out, in order to improve filter efficiency above filter pocket 6.
The discharging opening of saccharifying steaming and decocting convolution pot 2 is connected with centrifugal pump 15 by being provided with the discharge nozzle of observation window 10.Meanwhile, from
The up pipeline of heart pump 15 is had and is connected with filter tank 6 by the branch connected with the side feeding mouth 9 of filter tank 6, to realize wheat
Wine with dregs is pumped in filter tank 6.
Centrifugal pump 15 is positioned at the bottom of saccharifying steaming and decocting convolution pot 2, is returned with saccharifying steaming and decocting by horizontal pipe and up-hill line
The rotation parts such as pot 2 and filter tank 6 connect.The up-hill line of centrifugal pump 15 is respectively equipped with from the bottom to top and connects with axial return duct 14
The branch that connects with gyrotron 11 of branch and the branch of convolution pot CIP system connectivity connect with filter tank side feeding mouth 9
The branch that branch connects with filter tank CIP purging system 7.The horizontal pipeline of centrifugal pump 15 respectively with the discharge nozzle of filter tank 6,
The vertical connecting tube of eccentric discharging opening 12 and the vertical connecting tube of center discharging opening 13 connect.
Above in association with accompanying drawing, detailed description of the invention of the present utility model is described, but these explanations can not be understood to
Limit scope of the present utility model.Protection domain of the present utility model is limited by appended claims, any in this reality
With the change on the basis of novel claim, it it is all protection domain of the present utility model.
Claims (10)
1. a compound saccharifying device for beer, it is characterised in that include saccharification boiling convolution pot (2), is positioned at saccharification boiling convolution
The heating interlayer (1) of pot (2) bottom outside, is positioned at the filter tank (6) on saccharification boiling convolution pot (2) top, pot CIP system of circling round
(3), filter tank CIP purging system (7) and by pipeline and saccharification boiling convolution pot (2), filter tank (6), convolution pot CIP system
The centrifugal pump (15) that system (3) and filter tank CIP purging system (7) connect；Wherein, the filter tank CIP on filter tank (6) top cleans
System (7) is connected with air pressure filtration system boost mouth (8)；Described saccharification boiling convolution pot (2) bottom is provided with a center discharging
Mouth (13) and an eccentric discharging opening (12)；Described heating interlayer (1) is connected with the bottom of saccharification boiling convolution pot (2).
2. the saccharifying device for beer described in claim 1, it is characterised in that the vertical height of described filter tank (6) is that saccharifying is steamed
Boil the height of convolution pot (2) straight tube.
3. the saccharifying device for beer described in claim 1, it is characterised in that the side, top of described saccharifying steaming and decocting convolution pot (2)
It is provided with saccharifying dog-house (4).
4. the saccharifying device for beer described in claim 1, it is characterised in that described filter tank (6) lower side is provided with filter tank
Go out grain mouth (5).
5. the saccharifying device for beer described in claim 1, it is characterised in that the discharging opening of described filter tank (6) bottom is by setting
The discharge nozzle having observation window (10) is connected with centrifugal pump (15).
6. the saccharifying device for beer described in claim 1, it is characterised in that described filter tank (6) bottom can also ad hoc for
The wheat juice pump of sucking filtration.
7. the saccharifying device for beer described in claim 1, it is characterised in that at the bottom of the vertical pipeline being connected with center discharging opening (13)
End is connected with centrifugal pump (15) by horizontal pipe, and middle part is connected by the up-hill line of axial return duct (14) with centrifugal pump (15)
Connect.
8. the saccharifying device for beer described in claim 1, it is characterised in that the vertical pipeline being connected with eccentric discharging opening (12) leads to
Cross horizontal pipe to be connected with centrifugal pump (15).
9. the saccharifying device for beer described in claim 1, it is characterised in that the up pipeline of centrifugal pump (15) is sequentially provided with and axle
Branch that the gyrotron (11) of the branch connected to return duct (14) and saccharifying steaming and decocting convolution pot (2) is connected and convolution pot CIP
Branch that the branch that system (3) connects is connected with filter tank side feeding mouth (9) and being connected with filter tank CIP purging system (7)
Branch.
10. the saccharifying device for beer described in claim 1, it is characterised in that the horizontal pipeline of centrifugal pump (15) respectively with filtration
Groove (6) discharge nozzle, the vertical connecting tube of eccentric discharging opening (12) vertically connecting tube and center discharging opening (13) connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620570670.1U CN205821288U (en) | 2016-06-14 | 2016-06-14 | A kind of compound saccharifying device for beer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620570670.1U CN205821288U (en) | 2016-06-14 | 2016-06-14 | A kind of compound saccharifying device for beer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205821288U true CN205821288U (en) | 2016-12-21 |
Family
ID=57569546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620570670.1U Expired - Fee Related CN205821288U (en) | 2016-06-14 | 2016-06-14 | A kind of compound saccharifying device for beer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205821288U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635581A (en) * | 2017-01-07 | 2017-05-10 | 杭州旷博机械设备有限公司 | Beer saccharifying tank |
| CN109097416A (en) * | 2018-08-17 | 2018-12-28 | 中国科学院青岛生物能源与过程研究所 | Lignocellulosic one kettle way bioconversion method |
-
2016
- 2016-06-14 CN CN201620570670.1U patent/CN205821288U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635581A (en) * | 2017-01-07 | 2017-05-10 | 杭州旷博机械设备有限公司 | Beer saccharifying tank |
| CN106635581B (en) * | 2017-01-07 | 2020-07-14 | 杭州旷博机械设备有限公司 | Beer saccharification jar |
| CN109097416A (en) * | 2018-08-17 | 2018-12-28 | 中国科学院青岛生物能源与过程研究所 | Lignocellulosic one kettle way bioconversion method |
| CN109097416B (en) * | 2018-08-17 | 2020-10-20 | 中国科学院青岛生物能源与过程研究所 | Lignocellulose one-pot biotransformation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161221 |