CN208711068U - A kind of milk powder producing low temperature spray drying system - Google Patents
A kind of milk powder producing low temperature spray drying system Download PDFInfo
- Publication number
- CN208711068U CN208711068U CN201820445351.7U CN201820445351U CN208711068U CN 208711068 U CN208711068 U CN 208711068U CN 201820445351 U CN201820445351 U CN 201820445351U CN 208711068 U CN208711068 U CN 208711068U
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- impurity
- discharge port
- atomization drying
- milk powder
- precipitator
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Abstract
The utility model discloses a kind of milk powder producing low temperature spray drying systems, including atomization drying bucket, atomization drying bucket lower end is equipped with finished product discharge port, the discharge port is equipped with material mouth baffle, atomization drying bucket side is equipped with feed pipe, the feeding-passage is equipped with the first impurity precipitator and the second impurity precipitator, the lower end of first impurity precipitator and the second impurity precipitator is respectively equipped with the first impurity discharge port and the second impurity discharge port, the side of second settling vessel is equipped with mateiral pump, the side of the mateiral pump is connected with filter, the feed pipe is equipped with main gas pipe, the main gas pipe is equipped with the first air blower, the side of first air blower is equipped with first gas heater, one end that the close atomization drying bucket of the main gas pipe has is equipped with atomizer.A kind of milk powder producing low temperature spray drying system disclosed by the utility model is saved thermal energy, is not easy to plug, environmentally protective.
Description
Technical field
The utility model relates to drying system, in particular to a kind of milk powder producing low temperature spray drying system.
Background technique
It is all many times by liquid progress raw material mixing in many powderies and granular process of producing product
And then the product of liquid state is become powdery or graininess by the drying of the drying system of drying system, in milk powder
It is also to be produced with this principle in production process, in process of production, need nutriment to be added is passed through liquid
The full and uniform mixing of form, more uniform can be mixed according to setting ratio, pass through spray drying system later
Powder is carried out into, can be good at the quality for guaranteeing milk powder, now, in the production process of milk powder, our common drying sides arrived
Formula is mostly high temperature spray-drying method, and for high temperature spray-drying method when liquid state milk powder is dried, speed is fast, dry effect
Fruit is good, but the heat consumed simultaneously is big, and excessive heat is all used for functions/drying, generates waste, excessively high in terms of quality of milk powder
Temperature be easy the beneficial bacterium killed in milk powder and keep benefit materials rotten, be unfavorable for the preservation of benefit materials in milk powder, in liquid
In state milk powder transmission process, easily block.
Utility model content
For above-mentioned deficiency in the prior art, the utility model provides a kind of milk powder producing low temperature spray drying system
System, it is compact-sized, it is easy to operate, it is not easy to plug.
In order to reach above-mentioned purpose of utility model, the technical solution adopted in the utility model are as follows:
A kind of milk powder producing low temperature spray drying system, including atomization drying bucket, atomization drying bucket lower end are equipped with
Finished product discharge port, the discharge port are equipped with material mouth baffle, and atomization drying bucket side is equipped with feed pipe, the feed pipe
Road is equipped with the first impurity precipitator and the second impurity precipitator, under first impurity precipitator and the second impurity precipitator
End is respectively equipped with the first impurity discharge port and the second impurity discharge port, and the side of second impurity precipitator is equipped with mateiral pump,
The side of the mateiral pump is connected with filter, and the feed pipe is equipped with main gas pipe, on the main gas pipe
Equipped with the first air blower, the side of first air blower is equipped with first gas heater, the close mist of the main gas pipe
One end that changing dry bucket has is equipped with atomizer, and the upper end of the atomization drying bucket is equipped with auxiliary gas pipeline, the auxiliary gas
Body pipeline is equipped with the second air blower, and the side of second air blower is equipped with second gas heater, the auxiliary flue
One end of the close atomization drying bucket in road is equipped with gas distributor, and the atomization drying bucket is equipped with wind pipe, the outlet air
Pipeline is equipped with knockout drum, and the knockout drum side is equipped with exhaust fan, and the side of the exhaust fan is equipped with separator, the outlet air
One end of the separate atomization drying bucket of pipeline is equipped with deduster.
The utility model has the following beneficial effects:
It is set at feed pipe there are two impurity precipitator, can first be sunk twice before liquid milk powder reaches filter
Drop, is filtered the impurity of some bulky grains except filter, guarantees smoothly pass through liquid milk at filter screen
Powder prevents from blocking, and has liquid or air transporting arrangement in each pipeline, guarantees the passage of liquids and gases, assists gas
Pipeline can help powdery milk powder to settle, and gas distributor can prevent blast intensity too big, milk powder is caused to fly upward, wind pipe one
End is equipped with deduster, can prevent the dust of milk powder from entering outside air, protects environment.
Further, first impurity precipitator and the second impurity precipitator shape are that bore is less than the flat of container diameter
Vase-like, the first impurity discharge port and the second impurity discharge port are located at the first impurity precipitator and the second contamination precipitation
Device bottom middle position, and pull baffles, bulky grain are respectively equipped on the first impurity discharge port and the second impurity discharge port
Impurity enters settling vessel, is not easy secondary into pipeline, easy despumation, easy cleaning.
Further, the middle part indent of the atomization drying bucket, atomizer setting are described in interior recess lower end
The middle position of atomization drying bucket upper end, auxiliary gas pipeline the stretching in atomization drying bucket is arranged in auxiliary gas pipeline
Enter amount to go out no more than indent, be conducive to the sedimentation of milk powder, prevents excessive milk powder from entering wind pipe.
Further, the feed pipe is connected to main gas pipe, the center of the atomizer and main gas
On the same axis, the wind that atomizer receives is more uniform for the center of pipeline.
Further, atomization drying bucket upper end can open, easy cleaning.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
The appended drawing reference table of comparisons:
1- atomization drying bucket, 2- finished product discharge port, 3- material mouth baffle, 4- feed pipe, the first impurity precipitator of 5-, 6-
Two impurity precipitators, the first impurity of 7- discharge port, the second impurity of 8- discharge port, 9- mateiral pump, 10- filter, the main gas of 11-
Pipeline, the first air blower of 12-, 13- first gas heater, 14- atomizer, 15- assist gas pipeline, the second air blast of 16-
Machine, 17- second gas heater, 18- gas distributor, 19- wind pipe, 20- knockout drum, 21- exhaust fan, 22- separation
Device, 23- deduster, 24- pull baffles.
Specific embodiment
Further illustrate specific embodiment of the present utility model with reference to the accompanying drawing.Wherein identical components phase
Same appended drawing reference indicates.It should be noted that word "front", "rear" used in the following description, "left", "right", "upper" and
"lower" refers to that the direction in attached drawing, word "inner" and "outside" refer respectively to the side towards or away from geometric center of specific component
To.
In order to make the content of the utility model be easier to be clearly understood, below in conjunction in the utility model embodiment
Attached drawing, the technical scheme in the utility model embodiment is clearly and completely described.
As shown in Figure 1, a kind of milk powder producing low temperature spray drying system, including atomization drying bucket 1, the atomization drying bucket
1 lower end is equipped with finished product discharge port 2, and the discharge port 2 is equipped with material mouth baffle 3, and 1 side of atomization drying bucket is equipped with charging
Pipeline 4, the feed pipe 4 are equipped with the first impurity precipitator 5 and the second impurity precipitator 6, first impurity precipitator 5
The first impurity discharge port 7 and the second impurity discharge port 8, second impurity are respectively equipped with the lower end of the second impurity precipitator 6
The side of settling vessel 6 is equipped with mateiral pump 9, and the side of the mateiral pump 9 is connected with filter 10, sets on the feed pipe 4
There is main gas pipe 11, the main gas pipe 11 is equipped with the first air blower 12, and the side of first air blower 12 is equipped with
First gas heater 13, one end that the close atomization drying bucket 1 of the main gas pipe 11 has is equipped with atomizer 14, described
The upper end of atomization drying bucket 1 is equipped with auxiliary gas pipeline 15, and the auxiliary gas pipeline 15 is equipped with the second air blower 16, described
The side of second air blower 16 is equipped with second gas heater 17, the close atomization drying bucket 1 of the auxiliary gas pipeline 14
One end is equipped with gas distributor 18, and the atomization drying bucket 1 is equipped with wind pipe 19, and the wind pipe 19 is equipped with separation
Tank 20,20 side of knockout drum are equipped with exhaust fan 21, and the side of the exhaust fan 21 is equipped with separator 22, the discharge pipe
One end of the separate atomization drying bucket 1 in road 19 is equipped with deduster 23.
First impurity precipitator 5 and 6 shape of the second impurity precipitator are the flat vase-like that bore is less than container diameter,
The first impurity discharge port 7 and the second impurity discharge port 8 are located at the first impurity precipitator 5 and the second impurity precipitator 6
Bottom middle position, and pull baffles 24 are respectively equipped on the first impurity discharge port 7 and the second impurity discharge port 8.
The middle part indent of the atomization drying bucket 1, the atomizer 14 are arranged in interior recess lower end, the auxiliary gas
The middle position of 1 upper end of atomization drying bucket, auxiliary the stretching in atomization drying bucket 1 of gas pipeline 15 is arranged in body pipeline 15
Enter amount to go out no more than indent.
The feed pipe 4 is connected to main gas pipe 11, the center of the atomizer 14 and main gas pipe
11 center is on the same axis.
1 upper end of atomization drying bucket can open.
In the device use process, air is passed through main gas pipe 11 first, liquid milk powder is then passed through feed pipe
Road 4, in liquid milk powder by pipeline deflecting, liquid milk powder impact tube wall, speed slows down, the large granular impurity in liquid milk powder
It can be deposited in the first impurity precipitator 5 and the second impurity precipitator 6, liquid milk powder is less prone to when by filter 10
Blocking, for liquid milk powder under the action of hot-air, by 14 spraying drying powder-forming of atomizer, the dry milk powder completed is heavy mostly
It forms sediment into atomization drying bucket 1, is come out by discharge port 2, small part can enter wind pipe 19, be settled in wind pipe
And separation, it recycles again, the impurity milk powder in remaining only a few gas is purified by deduster 23, last air
It is discharged into external environment.
The foregoing is merely the preferred embodiment of the utility model patent, it is not intended to limit the utility model specially
Benefit, all made any modifications, equivalent replacements, and improvements etc. within the spirit and principle of the utility model patent should all include
Within the protection scope of the utility model patent.
Claims (5)
1. a kind of milk powder producing low temperature spray drying system, which is characterized in that including atomization drying bucket (1), the atomization drying
(1) lower end struggle against equipped with finished product discharge port (2), the discharge port (2) is equipped with material mouth baffle (3), the atomization drying bucket (1)
Side is equipped with feed pipe (4), and the feed pipe (4) is equipped with the first impurity precipitator (5) and the second impurity precipitator
(6), the lower end of first impurity precipitator (5) and the second impurity precipitator (6) be respectively equipped with the first impurity discharge port (7) and
The side of second impurity discharge port (8), second impurity precipitator (6) is equipped with mateiral pump (9), and the one of the mateiral pump (9)
Side is connected with filter (10), and the feed pipe (4) is equipped with main gas pipe (11), on the main gas pipe (11)
Equipped with the first air blower (12), the side of first air blower (12) is equipped with first gas heater (13), the main gas
One end that the close atomization drying bucket (1) of pipeline (11) has is equipped with atomizer (14), and the upper end of the atomization drying bucket (1) is set
Have auxiliary gas pipeline (15), the auxiliary gas pipeline (15) is equipped with the second air blower (16), second air blower
(16) side is equipped with second gas heater (17), and the one of the close atomization drying bucket (1) of auxiliary gas pipeline (15)
End is equipped with gas distributor (18), and the atomization drying bucket (1) is equipped with wind pipe (19), sets on the wind pipe (19)
Have knockout drum (20), knockout drum (20) side is equipped with exhaust fan (21), and the side of the exhaust fan (21) is equipped with separator
(22), one end of the separate atomization drying bucket (1) of the wind pipe (19) is equipped with deduster (23).
2. a kind of milk powder producing low temperature spray drying system according to claim 1, it is characterised in that: first impurity
Settling vessel (5) and the second impurity precipitator (6) shape are the flat vase-like that bore is less than container diameter, the first impurity discharging
Mouth (7) and the second impurity discharge port (8) are located among the first impurity precipitator (5) and the second impurity precipitator (6) bottom
Position, and pull baffles (24) are respectively equipped on the first impurity discharge port (7) and the second impurity discharge port (8).
3. a kind of milk powder producing low temperature spray drying system according to claim 1, it is characterised in that: the atomization drying
The middle part indent of bucket (1), atomizer (14) setting exist in interior recess lower end, auxiliary gas pipeline (15) setting
The middle position of atomization drying bucket (1) upper end, protrude into amount of auxiliary gas pipeline (15) in atomization drying bucket (1) do not surpass
Indent is crossed to go out.
4. a kind of milk powder producing low temperature spray drying system according to claim 1, it is characterised in that: the feed pipe
(4) it is connected to main gas pipe (11), the center of the atomizer (14) and the center of main gas pipe (11)
On the same axis.
5. a kind of milk powder producing low temperature spray drying system according to claim 1, it is characterised in that: the atomization drying
Bucket (1) upper end can open.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820445351.7U CN208711068U (en) | 2018-03-31 | 2018-03-31 | A kind of milk powder producing low temperature spray drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820445351.7U CN208711068U (en) | 2018-03-31 | 2018-03-31 | A kind of milk powder producing low temperature spray drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208711068U true CN208711068U (en) | 2019-04-09 |
Family
ID=65969595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820445351.7U Expired - Fee Related CN208711068U (en) | 2018-03-31 | 2018-03-31 | A kind of milk powder producing low temperature spray drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208711068U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111071643A (en) * | 2019-12-28 | 2020-04-28 | 甘肃省敦煌种业果蔬制品有限公司 | Tomato ketchup preheats storage jar |
| CN114027433A (en) * | 2021-11-08 | 2022-02-11 | 上海赛瑞益升健康食品有限公司 | Slow-release biological preservative for fermentation product |
-
2018
- 2018-03-31 CN CN201820445351.7U patent/CN208711068U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111071643A (en) * | 2019-12-28 | 2020-04-28 | 甘肃省敦煌种业果蔬制品有限公司 | Tomato ketchup preheats storage jar |
| CN114027433A (en) * | 2021-11-08 | 2022-02-11 | 上海赛瑞益升健康食品有限公司 | Slow-release biological preservative for fermentation product |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190409 Termination date: 20200331 |
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| CF01 | Termination of patent right due to non-payment of annual fee |