CN211798845U - Animal blood globulin heating and drying device - Google Patents
Animal blood globulin heating and drying device Download PDFInfo
- Publication number
- CN211798845U CN211798845U CN202020007099.9U CN202020007099U CN211798845U CN 211798845 U CN211798845 U CN 211798845U CN 202020007099 U CN202020007099 U CN 202020007099U CN 211798845 U CN211798845 U CN 211798845U
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- spiral separator
- primary
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- connecting pipeline
- mixer
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- 238000001035 drying Methods 0.000 title claims abstract description 22
- 238000010438 heat treatment Methods 0.000 title claims abstract description 15
- 102000006395 Globulins Human genes 0.000 title claims description 5
- 108010044091 Globulins Proteins 0.000 title claims description 5
- 210000004369 blood Anatomy 0.000 title claims description 5
- 239000008280 blood Substances 0.000 title claims description 5
- 238000000926 separation method Methods 0.000 claims abstract description 21
- 102000004169 proteins and genes Human genes 0.000 claims description 20
- 108090000623 proteins and genes Proteins 0.000 claims description 20
- 239000000428 dust Substances 0.000 claims description 16
- 102000001554 Hemoglobins Human genes 0.000 claims description 9
- 108010054147 Hemoglobins Proteins 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 210000000601 blood cell Anatomy 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 10
- 230000006872 improvement Effects 0.000 abstract description 2
- 239000006199 nebulizer Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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Abstract
The utility model discloses an animal blood cell albumen heating drying device, including air cleaner, switched heater, ultrasonic nebulizer, blender, separable set, collection storehouse and connecting line. The utility model belongs to the technical field of animal blood cell albumen processing, specifically be one kind can control the velocity of flow of albumen atomizing gas and heated air and the proportion between the two, guarantee albumen atomizing gas's drying effect, improve heated air and albumen atomizing gas's mixing uniformity, improvement mixing efficiency, through two-stage spiral separator, improve the animal blood cell albumen heat drying device of the separation effect of air and likepowder albumen.
Description
Technical Field
The utility model belongs to the technical field of animal blood cell albumen processing, specifically indicate an animal blood cell albumen heating drying device.
Background
The production of animal blood cell protein is to atomize the animal plasma stock solution, instantly dehydrate and dry after mixing with high-temperature hot air, the plasma stock solution atomization process in the traditional production process is complex, the mixing efficiency of atomized plasma and heated air is low, the mixing effect is poor, and the drying effect of blood cell protein is influenced; when the protein particles are separated from the air after drying, the separation process and equipment are complex, the energy consumption is high, and the actual protein yield is low.
SUMMERY OF THE UTILITY MODEL
To the above situation, for overcoming prior art's defect, the utility model provides a can control the velocity of flow of albumen atomizing gas and heated air and the proportion between the two, guarantee albumen atomizing gas's drying effect, improve heated air and albumen atomizing gas's mixing uniformity, improvement mixing efficiency, through two-stage spiral separator, improve the animal blood cell albumen heat drying device of the separation effect of air and likepowder albumen.
The utility model adopts the following technical scheme: an animal blood globulin heating and drying device comprises an air dust collector, an exchange type heater, an ultrasonic atomizer, a mixer, a separation component, a collection bin and a connecting pipeline, wherein an air inlet of the exchange type heater is connected with an outlet of the air dust collector through the connecting pipeline, an inlet of the mixer is connected with an outlet of the exchange type heater through the connecting pipeline, an outlet of the ultrasonic atomizer is connected with the connecting pipeline between the exchange type heater and the mixer, an inlet of the separation component is connected with an outlet of the mixer through the connecting pipeline, an inlet of the collection bin is connected with an outlet of the separation component through the connecting pipeline, the separation component comprises a primary spiral separator, a secondary spiral separator, a primary exhaust pipe, a secondary exhaust pipe, a primary collection pipe and a secondary collection pipe, an inlet of the primary spiral separator is connected with an outlet of the mixer through the connecting pipeline, the primary exhaust pipe is arranged between an outlet of the primary spiral separator and an inlet of the secondary spiral separator, the secondary exhaust pipe is arranged at the bottom of the secondary spiral separator, the primary collecting pipe is arranged between the outlet of the primary spiral separator and the collecting bin, and the secondary collecting pipe is arranged between the outlet of the secondary spiral separator and the primary collecting pipe.
Furthermore, the air dust remover is a hollow circular tube cavity, and a filter screen and an active carbon filter layer are sequentially arranged on the cross section of the air dust remover from the inlet to the outlet.
Furthermore, an air suction pump is arranged on a connecting pipeline between the exchange heater and the mixer, a protein suction pump is arranged on a connecting pipeline between the ultrasonic atomizer and the mixer, and an accelerating pump is arranged on a connecting pipeline between the mixer and the primary spiral separator, so that the accelerating pump can increase the flow velocity of the mixed gas and the mixed gas is easier to separate in the separator.
Furthermore, the primary spiral separator and the secondary spiral separator are arranged in a cylindrical structure with a conical bottom, inlets of the primary spiral separator and the secondary spiral separator are arranged on the arc-shaped side wall at the top, and the inlet directions of the primary spiral separator and the secondary spiral separator are along the tangential direction of the arc-shaped side wall.
Furthermore, outlets of the primary spiral separator and the secondary spiral separator are arranged at the top of a cone at the bottom, the primary collecting pipe is connected with the outlet of the primary spiral separator, and the primary exhaust pipe is arranged in the center of the outlet of the primary spiral separator; the secondary collecting pipe is connected with an outlet of the secondary spiral separator, and the secondary exhaust pipe is arranged in the center of the outlet of the secondary spiral separator.
Further, the pipe diameter of the first-stage collecting pipe is smaller than that of the first-stage exhaust pipe, and the pipe diameter of the second-stage collecting pipe is smaller than that of the second-stage exhaust pipe.
Further, the blender is vertical cylindric cavity setting, the top is located to the entry of blender, the bottom is located in the export of blender, the rotatory spiral mixing blade that is equipped with in top center of blender, when the air-mixing enters from the blender entry, can drive the rotation of spiral mixing blade, spiral mixing blade can increase the turbulent motion between heated air and the atomizing animal albumen, makes the mixed effect of atomizing animal albumen and heated air more even.
Adopt above-mentioned structure the utility model discloses the beneficial effect who gains as follows: the utility model provides an animal blood cell protein heating and drying device, which can control the flow rate of protein atomizing gas and heated air and the proportion between the two by arranging an air suction pump and a protein suction pump, and ensure the drying effect of the protein atomizing gas; the spiral mixing blades are added into the mixer, so that the mixing uniformity of the heated air and the protein atomization gas can be improved, and the mixing efficiency is improved; the two-stage spiral separator is arranged in the separation process, so that the separation effect of air and powdery protein can be improved, only one accelerating pump is needed to provide a power source for the separation assembly, the separation effect is improved, and the energy consumption required by the separation is reduced.
Drawings
Fig. 1 is a schematic view of the overall structure of the animal hemoglobin heating and drying device of the present invention.
The device comprises an air dust collector 1, an air dust collector 2, an exchange type heater 3, an ultrasonic atomizer 4, a mixer 5, a separation component 6, a collection bin 7, a connecting pipeline 8, a primary spiral separator 9, a secondary spiral separator 10, a primary exhaust pipe 11, a secondary exhaust pipe 12, a primary collection pipe 13, a secondary collection pipe 14, a filter screen 15, an active carbon filter layer 16, an air suction pump 17, a protein suction pump 18, an accelerating pump 19 and a spiral mixing blade.
The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the description serve to explain the invention and not to limit the invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments; based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
As shown in fig. 1, the technical solution adopted by the utility model is as follows: an animal blood globulin heating and drying device comprises an air dust collector 1, an exchange type heater 2, an ultrasonic atomizer 3, a mixer 4, a separation component 5, a collection bin 6 and a connecting pipeline 7, wherein an air inlet of the exchange type heater 2 is connected with an outlet of the air dust collector 1 through the connecting pipeline 7, an inlet of the mixer 4 is connected with an outlet of the exchange type heater 2 through the connecting pipeline 7, an outlet of the ultrasonic atomizer 3 is connected with the connecting pipeline 7 between the exchange type heater 2 and the mixer 4, an inlet of the separation component 5 is connected with an outlet of the mixer 4 through the connecting pipeline 7, an inlet of the collection bin 6 is connected with an outlet of the separation component 5 through the connecting pipeline 7, the separation component 5 comprises a primary spiral separator 8, a secondary spiral separator 9, a primary exhaust pipe 10, a secondary exhaust pipe 11, a primary collection pipe 12 and a secondary collection pipe 13, the inlet of the primary spiral separator 8 is connected with the outlet of the mixer 4 through a connecting pipeline 7, the primary exhaust pipe 10 is arranged between the outlet of the primary spiral separator 8 and the inlet of the secondary spiral separator 9, the secondary exhaust pipe 11 is arranged at the bottom of the secondary spiral separator 9, the primary collecting pipe 12 is arranged between the outlet of the primary spiral separator 8 and the collecting bin 6, and the secondary collecting pipe 13 is arranged between the outlet of the secondary spiral separator 9 and the primary collecting pipe 12.
The air dust collector 1 is a hollow circular tube cavity, and a filter screen 14 and an active carbon filter layer 15 are sequentially arranged on the cross section of the air dust collector 1 from an inlet to an outlet.
An air suction pump 16 is arranged on a connecting pipeline 7 between the exchange type heater 2 and the mixer 4, a protein suction pump 17 is arranged on the connecting pipeline 7 between the ultrasonic atomizer 3 and the mixer 4, and an accelerating pump 18 is arranged on the connecting pipeline 7 between the mixer 4 and the primary spiral separator 8.
The primary spiral separator 8 and the secondary spiral separator 9 are arranged in a cylindrical structure with a conical bottom, inlets of the primary spiral separator 8 and the secondary spiral separator 9 are arranged on a top circular arc-shaped side wall, and the inlet directions of the primary spiral separator 8 and the secondary spiral separator 9 are along the tangential direction of the circular arc-shaped side wall.
Outlets of the primary spiral separator 8 and the secondary spiral separator 9 are arranged at the top of a cone at the bottom, the primary collecting pipe 12 is connected with the outlet of the primary spiral separator 8, and the primary exhaust pipe 10 is arranged at the center of the outlet of the primary spiral separator 8; the secondary collecting pipe 13 is connected with the outlet of the secondary spiral separator 9, and the secondary exhaust pipe 11 is arranged in the center of the outlet of the secondary spiral separator 9.
The pipe diameter of the first-stage collecting pipe 12 is smaller than that of the first-stage exhaust pipe 10, and the pipe diameter of the second-stage collecting pipe 13 is smaller than that of the second-stage exhaust pipe 11.
Mixer 4 is vertical cylindric cavity setting, the top is located to the entry of mixer 4, the bottom is located to the export of mixer 4, the top center rotation of mixer 4 is equipped with helical mixing blade 19.
When the device is used specifically, an air suction pump 16, a protein suction pump 17, an ultrasonic atomizer 3 and an accelerating pump 18 are started, dust particles in air pass through an air dust collector 1, are adsorbed by a filter screen 14 and an active carbon filter layer 15, clean air passes through an exchange type heater 2, is heated and is pumped into a mixer 4 through the air suction pump 16, the ultrasonic atomizer 3 atomizes animal hemoglobin in liquid, the animal hemoglobin is pumped into the mixer 4 through the protein suction pump 17, the heated air and atomized protein gas can be fully mixed through a spiral mixing blade 19, the liquid in a blood cell separator is dried, the atomized protein becomes particles suspended in the heated air, the mixed gas is added into a primary spiral separator 8 through the accelerating pump 18, and the mixed air enters at a high speed along the tangential direction of the side wall of the primary spiral separator 8, due to the action of centrifugal force, protein particles will attach to the conical side wall of the primary spiral separator 8 and move downwards until falling into the primary collecting pipe 12, gas will be discharged from the primary exhaust pipe 10 in the middle of the bottom and enter the secondary spiral separator 9, the gas which is also primarily separated is separated again in the secondary spiral separator 9, and the protein particles separated from the primary spiral separator 8 and the secondary spiral separator 9 will enter the collecting bin 6.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
The present invention and the embodiments thereof have been described above, but the description is not limited thereto, and the embodiment shown in the drawings is only one of the embodiments of the present invention, and the actual structure is not limited thereto. In summary, those skilled in the art should understand that they should not be limited to the embodiments described above, and that they can design the similar structure and embodiments without departing from the spirit of the invention.
Claims (7)
1. An animal blood globulin heating and drying device is characterized in that: the device comprises an air dust collector, an exchange type heater, an ultrasonic atomizer, a mixer, a separation component, a collection bin and a connecting pipeline, wherein an air inlet of the exchange type heater is connected with an outlet of the air dust collector through the connecting pipeline, an inlet of the mixer is connected with an outlet of the exchange type heater through the connecting pipeline, an outlet of the ultrasonic atomizer is connected with the connecting pipeline between the exchange type heater and the mixer, an inlet of the separation component is connected with an outlet of the mixer through the connecting pipeline, an inlet of the collection bin is connected with an outlet of the separation component through the connecting pipeline, the separation component comprises a primary spiral separator, a secondary spiral separator, a primary exhaust pipe, a secondary exhaust pipe, a primary collection pipe and a secondary collection pipe, an inlet of the primary spiral separator is connected with an outlet of the mixer through the connecting pipeline, and the primary exhaust pipe is arranged between an outlet of the primary spiral separator and an inlet of the secondary spiral separator, the secondary exhaust pipe is arranged at the bottom of the secondary spiral separator, the primary collecting pipe is arranged between the outlet of the primary spiral separator and the collecting bin, and the secondary collecting pipe is arranged between the outlet of the secondary spiral separator and the primary collecting pipe.
2. The apparatus for heating and drying animal hemoglobin according to claim 1, wherein: the air dust remover is a hollow circular tube cavity, and a filter screen and an active carbon filter layer are sequentially arranged on the cross section of the air dust remover from an inlet to an outlet.
3. The apparatus for heating and drying animal hemoglobin according to claim 2, wherein: an air suction pump is arranged on a connecting pipeline between the exchange heater and the mixer, a protein suction pump is arranged on a connecting pipeline between the ultrasonic atomizer and the mixer, and an accelerating pump is arranged on a connecting pipeline between the mixer and the primary spiral separator.
4. The apparatus for heating and drying animal hemoglobin according to claim 3, wherein: the primary spiral separator and the secondary spiral separator are arranged in a cylindrical structure with a conical bottom, inlets of the primary spiral separator and the secondary spiral separator are arranged on a top arc-shaped side wall, and the inlet directions of the primary spiral separator and the secondary spiral separator are along the tangential direction of the arc-shaped side wall.
5. The apparatus for heating and drying animal hemoglobin according to claim 4, wherein: outlets of the primary spiral separator and the secondary spiral separator are arranged at the top of the cone at the bottom, the primary collecting pipe is connected with the outlet of the primary spiral separator, and the primary exhaust pipe is arranged in the center of the outlet of the primary spiral separator; the secondary collecting pipe is connected with an outlet of the secondary spiral separator, and the secondary exhaust pipe is arranged in the center of the outlet of the secondary spiral separator.
6. The apparatus for heating and drying animal hemoglobin according to claim 5, wherein: the pipe diameter of the first-stage collecting pipe is smaller than that of the first-stage exhaust pipe, and the pipe diameter of the second-stage collecting pipe is smaller than that of the second-stage exhaust pipe.
7. The apparatus for heating and drying animal hemoglobin according to claim 6, wherein: the blender is vertical cylindric cavity setting, the top is located to the entry of blender, the bottom is located to the export of blender, the top center rotation of blender is equipped with helical mixing blade.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020007099.9U CN211798845U (en) | 2020-01-02 | 2020-01-02 | Animal blood globulin heating and drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020007099.9U CN211798845U (en) | 2020-01-02 | 2020-01-02 | Animal blood globulin heating and drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211798845U true CN211798845U (en) | 2020-10-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020007099.9U Expired - Fee Related CN211798845U (en) | 2020-01-02 | 2020-01-02 | Animal blood globulin heating and drying device |
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| Country | Link |
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| CN (1) | CN211798845U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114181815A (en) * | 2021-12-06 | 2022-03-15 | 清华大学 | Large-flow ambient air bioaerosol sampling device and method |
-
2020
- 2020-01-02 CN CN202020007099.9U patent/CN211798845U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114181815A (en) * | 2021-12-06 | 2022-03-15 | 清华大学 | Large-flow ambient air bioaerosol sampling device and method |
| CN114181815B (en) * | 2021-12-06 | 2023-10-20 | 清华大学 | Large-flow ambient air biological aerosol sampling device and method |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| 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: 20201030 |