CN208104414U - A kind of production system of fermented maize paste dry powder - Google Patents
A kind of production system of fermented maize paste dry powder Download PDFInfo
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- CN208104414U CN208104414U CN201820307011.8U CN201820307011U CN208104414U CN 208104414 U CN208104414 U CN 208104414U CN 201820307011 U CN201820307011 U CN 201820307011U CN 208104414 U CN208104414 U CN 208104414U
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- fermentor
- agitating shaft
- froth breaker
- dry powder
- production system
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Abstract
A kind of production system of fermented maize paste dry powder, including fermentor, fermentor motor is equipped with above the fermentor, the fermentor is provided with agitating shaft, stirring blade is provided on the agitating shaft, the rotary shaft and agitating shaft of the fermentor motor are drivingly connected, a through-hole is offered at the axle center of the agitating shaft, and in the gas vent for being also provided with interval and being evenly arranged of agitating shaft, water inlet pipe is additionally provided in the through-hole, the water inlet pipe is equipped with hole corresponding with gas vent, froth breaker is installed above the agitating shaft, it is connect with the outer froth breaker of tank by bubble collecting tube road at the top of the fermentor.The utility model improves the utilization rate of product, by thorn part and tank outside froth breaker combine by the removal of foam it is abundant, drying effect is enhanced using the simple supply air system of structure, reduces the wall sticking phenomenon of material.
Description
Technical field
The utility model relates to corn pulp technical field, in particular to a kind of production system of fermented maize paste dry powder.
Background technique
Fermented maize slurry is that first corn pulp is put into fermentor, then fermenting microbe and corn pulp mixed fermentation 48 is small
When more than, during fermentation, need to be passed through a certain amount of oxygen, keep certain constant temperature and uninterrupted stirring to improve fermentation effect
Fruit, the corn pulp fermented at present is more thick, is easy to cause fermentor not easy cleaning.In fermentation process, since saccharomycete etc. is micro-
Biological effect generates many bubbles, influences ferment effect.It is in liquid condition additionally, due to fermented maize slurry, preservation term is short, is
It increases operation rate, needs to be further dried into powder and utilized again, and corn pulp moisture content is higher, directly carries out
Drying efficiency is lower.
Summary of the invention
The technical issues of the utility model solves is to provide a kind of fermented maize slurry concentrate drying system, improves fermented maize
The utilization rate of slurry.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is：
A kind of production system of fermented maize paste dry powder, including fermentor, the fermentor top are equipped with fermentor motor,
The fermentor is provided with agitating shaft, is provided with stirring blade on the agitating shaft, the rotary shaft of the fermentor motor with stir
Axis drive connection is mixed, offers a through-hole at the axle center of the agitating shaft, and be evenly arranged at the interval that is also provided with of agitating shaft
Gas vent, water inlet pipe is additionally provided in the through-hole, the water inlet pipe is equipped with hole corresponding with gas vent, the agitating shaft
Top is equipped with froth breaker, is connect with the outer froth breaker of tank by bubble collecting tube road at the top of the fermentor.
Preferably, the froth breaker includes horizontal part and rake, is provided with the first spine part on horizontal part, on rake
It is provided with the second spine part, the froth breaker bottom is equipped with rake teeth, the rake teeth irregular arrangement triangular in shape.
It is further preferred that the outer froth breaker of the tank is by froth breaker motor driven outside tank, the bubble collecting tube road position
In the top of stirring blade, the end in bubble collecting tube road is equipped with layer 2-3 strainer, is equipped with defoaming inside the outer froth breaker of the tank and stirs
Mix axis.
Preferably, the fermentor is connected to blender, is equipped with stirring motor, the blender above the blender
Inside is equipped with screw agitation shaft, and the blender passes through pipeline respectively and connect with the first inspissator, the second inspissator, and described
Second strainer is installed inside one inspissator, the second inspissator, the first inspissator, the second inspissator the second strainer under set respectively
There are the first recycling bins, the second recycling bins, first recycling bins, the second recycling bins are connected to by pipeline with atomizer, the mist
Change and be equipped with drying cylinder below device, is equipped with hot air intake system at the top of the drying cylinder, the hot air intake system is successively by first
Filter, the first dehumidifier and heater are connected to form by pipeline, and the filter is equipped with air inlet port, the heater
Connect the drying cylinder.
It is further preferred that first recycling bins, the second recycling bins are connected to drain pipe.
It is further preferred that the drain pipe is connect with fermentor, the outer froth breaker bottom of the tank is connected to fermentor.
It is further preferred that the bottom of the drying cylinder is connected to natural wind air inlet system, the natural wind air inlet system
Successively it is connected to form by the second filter, the second dehumidifier by pipeline.
The beneficial effects of the utility model：
1, the utility model carries out again after fermented maize is starched progress initial concentration using the first inspissator, the second inspissator
It is dry, the product quality of fermented maize slurry is improved, the utilization rate of product is improved.
2, it is combined by thorn part and the outer froth breaker of tank the removal of foam is abundant, the first spine part is set and the second spine part will
Part bubble punctures, and the rake teeth irregular arrangement triangular in shape can reduce the drag reduction power consumption of rake teeth, and can be bright
It is aobvious to improve defoaming effect.The foam not punctured enters tank after the multistorey strainer mesh of the end in bubble collecting tube road is sheared again
In outer froth breaker, shearing force caused by the stirring blade using froth breaker outside tank and impact force are further defoamed, the portion of generation
Sub-material liquid flows into fermentor by reflux line.
3, it is distributed the first inspissator, the second inspissator up and down by being equipped with, can carries out and is separately concentrated simultaneously,
The working efficiency of the device is improved, to increase economic benefit, by recycling bins, the water of generation can be recycled again
It utilizes, saves water resource.
4, using the simple supply air system of structure, hot air intake system enters the first dehumidifying after first passing through first filter
Device, absolute humidity reduce, then enter back into drying cylinder and be dried after being heated, provide the gas of high temperature low humidity a kind of in
In drying cylinder, more moisture in drying cylinder are taken away, drying effect is enhanced, reduce the wall sticking phenomenon of material, while can also
The moisture for reducing product, improves the yield and quality of product.
Detailed description of the invention
The utility model is described further with reference to the accompanying drawing：
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the structural schematic diagram of the utility model froth breaker；
Fig. 3 is the structural schematic diagram of the utility model rake teeth；
In figure：Fermentor 1, fermentor motor 2, agitating shaft 3, gas vent 4, water inlet pipe 5, froth breaker 6, horizontal part 61 incline
Inclined portion 62, the first spine part 63, the second spine part 64, rake teeth 65, the outer froth breaker 7 of tank, bubble collecting tube road 71 defoams agitating shaft
72, blender 8, stirring motor 9, screw agitation shaft 10, the first inspissator 11, the second inspissator 12, the second strainer 13, first time
Receipts case 14, the second recycling bins 15, atomizer 16, drain pipe 17, first filter 18, the first dehumidifier 19, heater 20, second
Filter 21, the second dehumidifier 22.
Specific embodiment
As shown in Figure 1-3, a kind of production system of fermented maize paste dry powder, including fermentor 1, it is characterised in that：It is described
Fermentor motor 2 is equipped with above fermentor 1, the fermentor 1 is provided with agitating shaft 3, is provided with paddle on the agitating shaft 3
Piece, the rotary shaft and agitating shaft 3 of the fermentor motor 2 are drivingly connected, and offer a through-hole at the axle center of the agitating shaft 3,
And water inlet pipe 5, the water inlet are additionally provided in the gas vent 4 for being also provided with interval and being evenly arranged of agitating shaft 3, the through-hole
Pipe 5 is equipped with hole corresponding with gas vent 4, is equipped with froth breaker 6 above the agitating shaft 3,1 top of fermentor with outside tank
Froth breaker 7 is connected by bubble collecting tube road 71.
Preferably, the froth breaker 6 includes horizontal part 61 and rake 62, is provided with the first spine part on horizontal part 61
63, the second spine part 64 is provided on rake 62,6 bottom of froth breaker is equipped with rake teeth 65, and the rake teeth 65 is triangular in shape
Irregular arrangement.
It is further preferred that the outer froth breaker 7 of the tank is driven by froth breaker motor 23 outside tank, the bubble collecting tube road
71 are located at the top of stirring blade, and the end in bubble collecting tube road 71 is equipped with layer 2-3 strainer, sets inside the outer froth breaker 7 of the tank
There is defoaming agitating shaft 72.
Preferably, the fermentor 1 is connected to blender 8, and stirring motor 9 is equipped with above the blender 8, described to stir
It mixes and screw agitation shaft 10 is installed inside device 8, the blender 8 passes through pipeline and the first inspissator 11, the second inspissator respectively
12 connect, and are equipped with the second strainer 13 inside first inspissator 11, the second inspissator 12, the first inspissator 11, second is dense
The first recycling bins 14, the second recycling bins 15, first recycling bins 14, second times are respectively equipped under second strainer 13 of contracting device 12
It receives case 15 to be connected to by pipeline with atomizer 16, by flow control knob, can control dense into the first inspissator 11, second
The flow velocity of corn pulp in contracting device 12 guarantees that the first inspissator 11 is capable of efficient stable and be concentrated, and passes through and is equipped with up and down point
Cloth the first inspissator 11, the second inspissator 12 can be carried out simultaneously and be separately concentrated, and improve the work effect of the device
The water of generation, by recycling bins, can be carried out recycling and reusing, save water resource by rate to increase economic benefit.
Be equipped with drying cylinder below the atomizer 16, be equipped with hot air intake system at the top of the drying cylinder, the hot wind into
Wind system is successively connected to form by first filter 18, the first dehumidifier 19 and heater 20 by pipeline, the filter 18
Equipped with air inlet port, the heater 20 connects the drying cylinder.
It is further preferred that first recycling bins 14, the second recycling bins 15 are connected to drain pipe 17.
It is further preferred that the drain pipe 17 is connect with fermentor 1, outer 7 bottom of froth breaker of the tank and fermentor 1
Connection.The liquid that concentration, the outer froth breaker 7 of tank are discharged directly is recycled to fermenting corn steep liquor tank, solvable inside abundant withdrawal liquid
Property substance, including amino acid, monosaccharide substance improves ferment effect.
It is further preferred that the bottom of the drying cylinder is connected to natural wind air inlet system, the natural wind air inlet system
Successively it is connected to form by the second filter 21, the second dehumidifier 22 by pipeline.Hot air intake system first passes through first filter
Enter the first dehumidifier afterwards, absolute humidity reduces, then enters back into drying cylinder and be dried after being heated, and provides a kind of high
The gas of warm low humidity enhances drying effect in drying cylinder, taking away more moisture in drying cylinder, reduces the viscous wall of material
Phenomenon, while the moisture of product can also be reduced, improve the yield and quality of product.In addition it from the top of drying cylinder into hot wind, keeps away
Exempt from corn starch and the phenomenon that returning top occurs.
Claims (7)
1. a kind of production system of fermented maize paste dry powder, including fermentor（1）, it is characterised in that：The fermentor（1）Top
Equipped with fermentor motor（2）, the fermentor（1）It is provided with agitating shaft（3）, the agitating shaft（3）On be provided with stirring blade,
The fermentor motor（2）Rotary shaft and agitating shaft（3）It is drivingly connected, the agitating shaft（3）Axle center to offer one logical
Hole, and in agitating shaft（3）Be also provided with the gas vent that is evenly arranged of interval（4）, water inlet pipe is additionally provided in the through-hole
（5）, the water inlet pipe（5）It is equipped with and gas vent（4）Corresponding hole, the agitating shaft（3）Top is equipped with froth breaker（6）,
The fermentor（1）Top and the outer froth breaker of tank（7）Pass through bubble collecting tube road（71）Connection.
2. a kind of production system of fermented maize paste dry powder according to claim 1, it is characterised in that：The froth breaker
（6）Including horizontal part（61）And rake（62）, horizontal part（61）On be provided with the first spine part（63）, rake（62）On set
It is equipped with the second spine part（64）, the froth breaker（6）Bottom is equipped with rake teeth（65）, the rake teeth（65）Irregular cloth triangular in shape
It sets.
3. a kind of production system of fermented maize paste dry powder according to claim 2, it is characterised in that：It is defoamed outside the tank
Device（7）By froth breaker motor outside tank（23）Driving, the bubble collecting tube road（71）Positioned at the top of stirring blade, foam is received
Collect pipeline（71）End be equipped with layer 2-3 strainer, the outer froth breaker of the tank（7）Inside is equipped with defoaming agitating shaft（72）.
4. a kind of production system of fermented maize paste dry powder according to claim 1, it is characterised in that：The fermentor
（1）With blender（8）Connection, the blender（8）Top is equipped with stirring motor（9）, the blender（8）Inside is equipped with
Screw agitation shaft（10）, the blender（8）Pass through pipeline and the first inspissator respectively（11）, the second inspissator（12）Connection,
First inspissator（11）, the second inspissator（12）Inside is equipped with the second strainer（13）, the first inspissator（11）, it is second dense
Contracting device（12）The second strainer（13）Under be respectively equipped with the first recycling bins（14）, the second recycling bins（15）, first recycling bins
（14）, the second recycling bins（15）Pass through pipeline and atomizer（16）Connection, the atomizer（16）Lower section is equipped with drying cylinder, described
Hot air intake system is equipped at the top of drying cylinder, the hot air intake system is successively by first filter（18）, the first dehumidifier
（19）And heater（20）It is connected to form by pipeline, the filter（18）Equipped with air inlet port, the heater（20）
Connect the drying cylinder.
5. a kind of production system of fermented maize paste dry powder according to claim 4, it is characterised in that：First recycling
Case（14）, the second recycling bins（15）With drain pipe（17）Connection.
6. a kind of production system of fermented maize paste dry powder according to claim 5, it is characterised in that：The drain pipe
（17）With fermentor（1）Connection, the outer froth breaker of the tank（7）Bottom and fermentor（1）Connection.
7. a kind of production system of fermented maize paste dry powder according to claim 4, it is characterised in that：The drying cylinder
Bottom is connected to natural wind air inlet system, and the natural wind air inlet system is successively by the second filter（21）, the second dehumidifier
（22）It is connected to form by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820307011.8U CN208104414U (en) | 2018-03-06 | 2018-03-06 | A kind of production system of fermented maize paste dry powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820307011.8U CN208104414U (en) | 2018-03-06 | 2018-03-06 | A kind of production system of fermented maize paste dry powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208104414U true CN208104414U (en) | 2018-11-16 |
Family
ID=64126672
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820307011.8U Active CN208104414U (en) | 2018-03-06 | 2018-03-06 | A kind of production system of fermented maize paste dry powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208104414U (en) |
-
2018
- 2018-03-06 CN CN201820307011.8U patent/CN208104414U/en active Active
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