CN208406124U - A kind of span amino acid mother liquor drying device - Google Patents
A kind of span amino acid mother liquor drying device Download PDFInfo
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- CN208406124U CN208406124U CN201820834626.6U CN201820834626U CN208406124U CN 208406124 U CN208406124 U CN 208406124U CN 201820834626 U CN201820834626 U CN 201820834626U CN 208406124 U CN208406124 U CN 208406124U
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- lower hopper
- amino acid
- tower body
- mother liquor
- coarse granule
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Abstract
The utility model discloses a kind of span amino acid mother liquor drying devices, belong to amino acids production apparatus field, in order to solve the problem of that the low occupied space of drying device of amino acid mother liquor integration degree existing in the prior art is big, there are meaningless process.The utility model includes tower body, it is provided with feed pathway at the top of the tower body, atomizer is provided in the feed pathway, the sidewall upper of the tower body is additionally provided with hot wind inlet, the tower body bottom is provided with lower hopper, is provided with cyclone collector in the lower hopper.The utility model is for drying span amino acid mother liquor, and compared to existing complete set of equipments, the utility model significantly reduces production cost.
Description
Technical field
The utility model belongs to amino acids production apparatus field, and in particular to arrives a kind of drying device of amino acid mother liquor.
Background technique
Amino acid is the basic unit for constituting protein, assigns the specific molecular morphosis of protein, makes its molecule
With biochemical activity.Amino acid broadly refers to the not only organic compound containing a basic amine group but also containing an acidic carboxypolymer
Object, as described in its name.With the sustainable development of science and technology, the demand of amino acid is also constantly increased.It is all kinds of
Amino acid is widely used in the fields such as medication chemistry, food, feed, cosmetics, Biochemical Research.Such as Fig. 2, use in the prior art
Hydrolysis feather produces amino acid and its by-product and dries mother liquor frequently with set of equipment often, and volume is excessive, degree of integration
It is relatively low, it has been correspondingly improved production cost.
The Chinese utility model of notification number CN201557538U discloses a kind of equipment for processing amino acid mother liquid, including efficient
Strengthen and is concentrated and dried device, underflow pump, auxiliary material charging system, efficient underflow formula batch mixer, screw rod transmission feeder, DJZL type extrusion
Machine, DW type straight line cooler, broken granulator, bucket type feeder, finished product bin and autometering packaging machine.The utility model mentions
The span amino acid mother liquor equipment for drying of confession will be applied in combination with covering equipment, but not be integrated into an equipment, integrated level
It is low, it is big to occupy delivery room space, and midway also uses multiple conveying equipment, increases meaningless process, increases energy consumption,
The time is wasted, production cost is increased, reduces production efficiency.
Utility model content
The purpose of this utility model is that: it is integrated in order to solve drying device of amino acid mother liquor existing in the prior art
Degree is low, and occupied space is big, there are problems that meaningless process, provides a kind of span amino acid mother liquor drying device, realizes one
Platform equipment completes the span amino acid mother liquor drying process that the prior art could be completed in red a set of equipment.
The technical solution adopted in the utility model is as follows:
A kind of span amino acid mother liquor drying device, including tower body, the tower body top are provided with atomizer, and atomizer is being atomized
The feed inlet chain of machine is connected to feed pathway, and the sidewall upper of the tower body is additionally provided with hot wind inlet, the tower body bottom setting
There is lower hopper, is provided with cyclone collector in the lower hopper.
Further, the tower body bottom is additionally provided with coarse granule lower hopper, the axis of the coarse granule lower hopper and institute
The axis for stating lower hopper is parallel；The maximum gauge of the coarse granule lower hopper, the maximum gauge for being highly all larger than the lower hopper,
Highly.
Further, communicating pipe, the other end of the communicating pipe and institute are additionally provided in the middle part of the coarse granule lower hopper
The side wall connection of lower hopper is stated, the coarse granule lower hopper with the lower hopper by being connected to the communicating pipe.
Further, the tower body bottom is additionally provided with third lower hopper, the axis of the third lower hopper and it is described under
The axis of hopper is parallel, is provided with expansion chamber at the top of the third lower hopper；Exhaust fan is provided on the side wall of the expansion chamber.
Further, it was additionally provided with for the second communicating pipe on the side wall of the expansion chamber, one end of second communicating pipe is stretched
Enter in lower hopper, the expansion chamber with the lower hopper by being connected to second communicating pipe.
Further, the lower hopper, third lower hopper, the top of coarse granule lower hopper are concordant.
In conclusion by adopting the above-described technical solution, the beneficial effects of the utility model are:
1, the utility model uses integrated design, and the top of tower body is the feed pathway for being provided with atomizer, tower body
Hot wind inlet is provided on side wall, span amino acid mother liquor is atomized machine atomization after feed pathway entrance, and then is covered with entire tower body
Inside, the span amino acid mother liquor of atomization come into full contact with and wink-dry by the hot wind entered from hot wind inlet, isolates amino acid
Coarse granule out, coarse granule are entered under the effect of gravity in the lower hopper of tower body bottom, and rotation is provided in lower hopper
Wind collector, amino acid coarse granule is driven in cyclone collector by high-speed flow and high speed, high frequency mutually collide, or high speed
It striking on lower hopper side wall, amino acid coarse granule becomes fine powder and goes out from lower hopper bottom, achieve the effect that uniform discharge,
Amino acid fine powder is cooled by high speed airflow influence realization during this.Compared to the prior art, the utility model will be existing
Drying tower and cyclone separator it is integrated on the same device, and while preparing amino acid using the utility model, eliminates extrusion
The equipment such as machine, cooler.Good amino acid fine powder can be obtained using the utility model, and device integration is high, it is empty to occupy
Between it is small, simplify amino acid manufacturing process.
2, in the utility model, because can inevitably there is coarse granule after span amino acid mother liquor atomization drying, and thick
Grain, which is mingled in amino acid fine powder, can reduce final product quality, while influence amino acid subsequent machining technology, and therefore, it is necessary to will dry
The upper coarse granule and fine powder separate collection generated afterwards, so tower body bottom is additionally provided with coarse granule lower hopper, coarse granule lower hopper
Axis it is parallel with the axis of the lower hopper.The maximum gauge of coarse granule lower hopper is highly all larger than the lower hopper most
Major diameter, height, therefore, in dropping process, the coarse granule not attracted by the high-speed flow in cyclone collector will be from thick
In the amino acid fine powder gone out, rather than be mixed into lower hopper in particle blanking bucket.The setting significantly improves amino acid fine powder
The uniformity and quality, while subsequent process steps are simplified, to reduce production cost.
3, in the utility model, in order to avoid generating a large amount of coarse granule, the company of being additionally provided in the middle part of coarse granule lower hopper
Siphunculus, the other end of communicating pipe are connect with the side wall of the lower hopper, coarse granule lower hopper by the communicating pipe and it is described under
Hopper connection.The coarse granule having more than needed in coarse granule lower hopper will be drawn onto whirlwind by communicating pipe by the cyclone collector in lower hopper
It is separated into amino acid fine powder in collector, improves the yield of amino acid fine powder, reduces the coarse grained yield of amino acid, into
And improve productivity effect.
4, in the utility model, because there are the steamings of a large amount of water in tower body by heated-air drying after span amino acid mother liquor atomization
Gas, and there is also a large amount of amino acid fine powders in vapor, therefore, tower body bottom is additionally provided with third lower hopper, third blanking
The axis of bucket and the axis of lower hopper are parallel, are provided with expansion chamber at the top of third lower hopper.The ammonia being mingled in vapor in tower body
Base acid fine powder enters expansion chamber, and then the natural subsidence in expansion chamber under the suction function of exhaust fan, passes through third lower hopper
Discharging.Exhaust fan is provided on the side wall of expansion chamber.Exhaust fan takes the intracorporal vapor of tower away, while facilitating expansion chamber suction
Receive the amino acid fine powder in vapor.
5, it in the utility model, for the amino acid fine powder being further dried in lower hopper, while will be generated in tower body
A large amount of vapor remove, and are additionally provided with for the second communicating pipe on the side wall of expansion chamber, and one end of the second communicating pipe is arranged in lower hopper
Interior, the second communicating pipe described in expansion chamber is connected to lower hopper.Vapor in lower hopper enters expansion chamber by the second communicating pipe
In.
6, in the utility model, in order to avoid the discharging of amino acid fine powder is uneven, under lower hopper, third lower hopper, coarse granule
The top of hopper is concordant.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the schematic diagram of the prior art；
Marked in the figure: 1- tower body, 101- hot wind inlet, 102- lower hopper, 103- coarse granule lower hopper, 104- third blanking
Bucket, 2- feed pathway, 3- atomizer, 4- cyclone collector, 5- communicating pipe, 6- expansion chamber, 7- exhaust fan, the second communicating pipe of 8-.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only to explain this
Utility model is not used to limit the utility model.
A kind of span amino acid mother liquor drying device, including tower body 1 are provided with atomizer 3 at the top of tower body 1, and atomizer 3 is being atomized
The feed inlet chain of machine 3 is connected to feed pathway 2, and the sidewall upper of tower body 1 is additionally provided with hot wind inlet 101, and 1 bottom of tower body is provided with
Lower hopper 102 is provided with cyclone collector 4 in lower hopper 102.
Further, 1 bottom of tower body is additionally provided with coarse granule lower hopper 103, the axis of coarse granule lower hopper 103 and blanking
The axis of bucket 102 is parallel；The maximum gauge of coarse granule lower hopper 103, the maximum gauge for being highly all larger than lower hopper 102, height.
Further, the middle part of coarse granule lower hopper 103 is additionally provided with communicating pipe 5, the other end and lower hopper of communicating pipe 5
102 side wall connection, coarse granule lower hopper 103 with lower hopper 102 by being connected to communicating pipe 5.
Further, 1 bottom of tower body is additionally provided with third lower hopper 104, the axis and lower hopper of third lower hopper 104
102 axis is parallel, and expansion chamber 6 is provided at the top of third lower hopper 104；Exhaust fan 7 is provided on the side wall of expansion chamber 6.
Further, it was additionally provided with for the second communicating pipe 8 on the side wall of expansion chamber 6, blanking is protruded into one end of the second communicating pipe 8
In bucket 102, expansion chamber 6 with lower hopper 102 by being connected to the second communicating pipe 8.
Further, lower hopper 102, third lower hopper 104, the top of coarse granule lower hopper 103 are concordant.
The utility model uses integrated design, and the top of tower body 1 is the feed pathway 2 for being provided with atomizer 3, tower body 1
Side wall on be provided with hot wind inlet 101, span amino acid mother liquor is atomized machine 3 after the entrance of feed pathway 2 and is atomized, and then is covered with whole
The span amino acid mother liquor of the inside of a tower body 1, atomization is come into full contact with and wink-dry by the hot wind entered from hot wind inlet 101, point
Amino acid coarse granule is separated out, coarse granule is entered under the effect of gravity in the lower hopper 102 of 1 bottom of tower body, in blanking
Cyclone collector 4 is provided in bucket 102, amino acid coarse granule is driven and high speed, high frequency in cyclone collector 4 by high-speed flow
Mutually in collision or high-speed impact to 102 side wall of lower hopper, amino acid coarse granule becomes fine powder and goes out from 102 bottom of lower hopper
It goes, achievees the effect that uniform discharge, amino acid fine powder is cooled by high speed airflow influence realization in the process.Exhausting simultaneously
Vapor in tower body 1, lower hopper 102, coarse granule lower hopper 103 is drawn onto expansion chamber 6 by machine 7, and the amino acid of vapor is thin
It is come out from third lower hopper 104 after powder natural subsidence.Compared to the prior art, the present embodiment is by existing drying tower and whirlwind
Separator is integrated on the same device, and the present embodiment is used to eliminate the equipment such as banded extruder, cooler when preparing amino acid.
Good amino acid fine powder can be obtained using the drying device of the present embodiment, and device integration is high, occupies little space, and simplifies
Amino acid manufacturing process.
Embodiment 1
A kind of span amino acid mother liquor drying device, including tower body 1 are provided with atomizer 3 at the top of tower body 1, and atomizer 3 is being atomized
The feed inlet chain of machine 3 is connected to feed pathway 2, and the sidewall upper of tower body 1 is additionally provided with hot wind inlet 101, and 1 bottom of tower body is provided with
Lower hopper 102 is provided with cyclone collector 4 in lower hopper 102.
The present embodiment uses integrated design, and the top of tower body 1 is the feed pathway 2 for being provided with atomizer 3, tower body 1
Hot wind inlet 101 is provided on side wall, span amino acid mother liquor is atomized machine 3 after the entrance of feed pathway 2 and is atomized, and then is covered with entire
The span amino acid mother liquor of the inside of tower body 1, atomization is come into full contact with and wink-dry by the hot wind entered from hot wind inlet 101, separates
Amino acid coarse granule out, coarse granule is entered under the effect of gravity in the lower hopper 102 of 1 bottom of tower body, in lower hopper
Cyclone collector 4 is provided in 102, amino acid coarse granule is driven and high speed, high frequency phase in cyclone collector 4 by high-speed flow
In mutual collision or high-speed impact to 102 side wall of lower hopper, amino acid coarse granule becomes fine powder and goes out from 102 bottom of lower hopper,
Achieve the effect that uniform discharge, amino acid fine powder is cooled by high speed airflow influence realization in the process.Compared to existing
Technology, the present embodiment are integrated on the same device by existing drying tower and cyclone separator, and are prepared using the present embodiment
The equipment such as banded extruder, cooler are eliminated when amino acid.Good amino acid can be obtained using the drying device of the present embodiment
Fine powder, and device integration is high, occupies little space, and simplifies amino acid manufacturing process.
Embodiment 2
On the basis of embodiment 1, because can inevitably there is coarse granule after span amino acid mother liquor atomization drying, and it is thick
Confusion can reduce final product quality in amino acid fine powder, while influence amino acid subsequent machining technology, and therefore, it is necessary to will do
The upper coarse granule and fine powder separate collection generated after dry, so 1 bottom of tower body is additionally provided with coarse granule lower hopper 103, coarse granule
The axis of lower hopper 103 is parallel with the axis of lower hopper 102；The maximum gauge of coarse granule lower hopper 103 is highly all larger than blanking
The maximum gauge of bucket 102, height.Therefore, in dropping process, not by thick of the high-speed flow attraction in cyclone collector
In the amino acid fine powder that grain will go out from coarse granule lower hopper 103, rather than be mixed into lower hopper 102.The setting significantly mentions
The high uniformity and quality of amino acid fine powder, while subsequent process steps are simplified, to reduce production cost.
Embodiment 3
On the basis of embodiment 2, in order to avoid generating a large amount of coarse granule, the middle part of coarse granule lower hopper 103 is also set
Be equipped with communicating pipe 5, the other end of communicating pipe 5 is connect with the side wall of lower hopper 102, coarse granule lower hopper 103 by communicating pipe 5 with
Lower hopper 102 is connected to.Cyclone collector 4 in lower hopper 102 will will be had more than needed in coarse granule lower hopper 103 by communicating pipe 5
Coarse granule, which is drawn onto cyclone collector 4, is separated into amino acid fine powder, improves the yield of amino acid fine powder, it is thick to reduce amino acid
The yield of particle, and then improve productivity effect.
Embodiment 4
On the basis of embodiment 3, because tower body 1 is interior to be existed largely by heated-air drying after span amino acid mother liquor atomization
Vapor, and there is also a large amount of amino acid fine powder in vapor, 1 bottom of tower body are additionally provided with third lower hopper 104, under third
The axis of hopper 104 is parallel with the axis of lower hopper 102, and expansion chamber 6 is provided at the top of third lower hopper 104；The side of expansion chamber 6
Exhaust fan 7 is provided on wall.The amino acid fine powder being mingled in vapor in tower body enters sedimentation under the suction function of exhaust fan 7
Room 6, and then the natural subsidence in expansion chamber 6 are discharged by third lower hopper 104.Exhaust fan 7 takes out the vapor in tower body 1
It walks, while facilitating the amino acid fine powder in the absorption vapor of expansion chamber 6.
Embodiment 5
On the basis of embodiment 4, for the amino acid fine powder being further dried in lower hopper 102, while will be in tower body 1
The a large amount of vapor generated remove, and are additionally provided with for the second communicating pipe 8 on the side wall of expansion chamber 6, one end of the second communicating pipe 8 is protruded into
In lower hopper 102, expansion chamber 6 with lower hopper 102 by being connected to the second communicating pipe 8.
Embodiment 6
On the basis of the above embodiments, in order to avoid the discharging of amino acid fine powder is uneven, lower hopper 102, third lower hopper
104, the top of coarse granule lower hopper 103 is concordant.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (6)
1. a kind of span amino acid mother liquor drying device, including tower body (1), it is characterised in that: be provided with atomization at the top of the tower body (1)
Machine (3), atomizer (3) are connected to feed pathway (2) in the feed inlet chain of atomizer (3), are provided in the feed pathway (2),
The sidewall upper of the tower body (1) is additionally provided with hot wind inlet (101), and tower body (1) bottom is provided with lower hopper (102),
Cyclone collector (4) are provided in the lower hopper (102).
2. a kind of span amino acid mother liquor drying device according to claim 1, it is characterised in that: tower body (1) bottom is also
It is provided with coarse granule lower hopper (103), the axis of the coarse granule lower hopper (103) and the axis of the lower hopper (102) are flat
Row；The maximum gauge of the coarse granule lower hopper (103), the maximum gauge for being highly all larger than the lower hopper (102), height.
3. a kind of span amino acid mother liquor drying device according to claim 2, it is characterised in that: the coarse granule lower hopper
(103) it is additionally provided in the middle part of communicating pipe (5), the other end of the communicating pipe (5) and the side wall of the lower hopper (102) connect
It connects, the coarse granule lower hopper (103) is connected to by the communicating pipe (5) with the lower hopper (102).
4. a kind of span amino acid mother liquor drying device according to claim 3, it is characterised in that: tower body (1) bottom is also
It is provided with third lower hopper (104), the axis of the third lower hopper (104) is parallel with the axis of the lower hopper (102), institute
It states and is provided with expansion chamber (6) at the top of third lower hopper (104)；Exhaust fan (7) are provided on the side wall of the expansion chamber (6).
5. a kind of span amino acid mother liquor drying device according to claim 4, it is characterised in that: the side of the expansion chamber (6)
It is additionally provided on wall the second communicating pipe (8), one end of second communicating pipe (8) is protruded into lower hopper (102), the expansion chamber
(6) it is connected to by second communicating pipe (8) with the lower hopper (102).
6. a kind of span amino acid mother liquor drying device according to claim 4, it is characterised in that: the lower hopper (102),
Three lower hoppers (104), the top of coarse granule lower hopper (103) are concordant.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820834626.6U CN208406124U (en) | 2018-05-31 | 2018-05-31 | A kind of span amino acid mother liquor drying device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820834626.6U CN208406124U (en) | 2018-05-31 | 2018-05-31 | A kind of span amino acid mother liquor drying device |
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| CN208406124U true CN208406124U (en) | 2019-01-22 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479094A (en) * | 2018-05-31 | 2018-09-04 | 峨眉山市龙腾生物科技有限公司 | A kind of span amino acid mother liquor drying device |
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2018
- 2018-05-31 CN CN201820834626.6U patent/CN208406124U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479094A (en) * | 2018-05-31 | 2018-09-04 | 峨眉山市龙腾生物科技有限公司 | A kind of span amino acid mother liquor drying device |
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