CN219596563U - Feather hydrolysis reaction tank - Google Patents
Feather hydrolysis reaction tank Download PDFInfo
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- CN219596563U CN219596563U CN202322045306.6U CN202322045306U CN219596563U CN 219596563 U CN219596563 U CN 219596563U CN 202322045306 U CN202322045306 U CN 202322045306U CN 219596563 U CN219596563 U CN 219596563U
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- tank body
- feather
- hydrolysis reaction
- reaction tank
- discharge hole
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Abstract
The utility model is suitable for the technical field of feather hydrolysis equipment, and provides a feather hydrolysis reaction tank, which comprises a tank body, a stirring assembly and an external high-temperature high-pressure source; the top of the tank body is provided with a feed inlet, the outer wall of the tank body is provided with a hydrolysis pipe, the hydrolysis pipe is communicated with an external high-temperature high-pressure source, the hydrolysis pipe is connected with a plurality of connecting pipes, the connecting pipes extend into the tank body after penetrating through the tank body, the bottom of the tank body is provided with a discharge hole, the discharge hole is internally provided with a crushing assembly, and the crushing assembly is used for crushing feathers entering the discharge hole; the stirring assembly comprises a first driving piece arranged at the side end of the tank body, an output shaft of the first driving piece is rotationally connected between the two side ends of the tank body, and stirring blades are arranged on the output shaft of the first driving piece; therefore, the utility model can hydrolyze the feather in the tank body uniformly, and can dry and crush the hydrolyzed feather, thereby shortening the post-processing time.
Description
Technical Field
The utility model relates to the technical field of feather hydrolysis equipment, in particular to a feather hydrolysis reaction tank.
Background
Currently, the main treatment methods of feathers include high temperature and high pressure hydrolysis, chemical hydrolysis, enzymatic hydrolysis, puffing and microbial degradation. The common high-temperature high-pressure hydrolysis method is to introduce hot steam generated by a boiler into a hydrolysis tank, change the structure of feathers in the hydrolysis tank under the high-temperature high-pressure environment, hydrolyze protein, and then dry, crush, test and package the hydrolyzed feathers into a finished product.
The utility model provides a double-end-enclosure feather hydrolysis tank in application number CN202223410428.2, it can increase the heat transfer area of the jar body through setting up first head, second head, outer half pipe clamp cover and interior half pipe clamp cover, improves feather decomposition efficiency.
According to the technical scheme, although the heat exchange area of the tank body is increased through the outer half-pipe jacket and the inner half-pipe jacket, the feather in the center of the tank body cannot be contacted with the inner surface of the tank body, so that the feather cannot be heated uniformly, and insufficient hydrolysis or prolonged hydrolysis time of the feather in the tank body is caused.
As is known, the prior art has obvious inconvenience and defects in practical use, so that improvement is needed.
Disclosure of Invention
In view of the above-mentioned drawbacks, an object of the present utility model is to provide a feather hydrolysis reaction tank, which can hydrolyze feathers in the tank uniformly, and can dry and crush the hydrolyzed feathers, thereby shortening the post-processing time.
In order to achieve the aim, the utility model provides a feather hydrolysis reaction tank which comprises a tank body, a stirring assembly and an external high-temperature high-pressure source;
the top of the tank body is provided with a feed inlet, the outer wall of the tank body is provided with a hydrolysis pipe, the hydrolysis pipe is communicated with an external high-temperature high-pressure source, the hydrolysis pipe is connected with a plurality of connecting pipes, the connecting pipes extend into the tank body after penetrating through the tank body, the bottom of the tank body is provided with a discharge hole, the discharge hole is internally provided with a crushing assembly, and the crushing assembly is used for crushing feathers entering the discharge hole;
the stirring assembly comprises a first driving piece arranged at the side end of the tank body, an output shaft of the first driving piece is rotationally connected between the two side ends of the tank body, and stirring blades are arranged on the output shaft of the first driving piece.
According to the feather hydrolysis reaction tank disclosed by the utility model, the drying pipe is arranged on the outer wall of the tank body, the feather hydrolysis reaction tank is also provided with an external hot air source, the drying pipe is communicated with the external hot air source, the drying pipe is connected with a plurality of air inlet pipes, and the air inlet pipes extend into the tank body after penetrating through the tank body.
According to the feather hydrolysis reaction tank disclosed by the utility model, the crushing assembly comprises two mutually matched crushing teeth, the two crushing teeth are both rotationally connected to the side wall of the discharge hole, the outer wall of the discharge hole is provided with the second driving piece and the third driving piece, one of the two crushing teeth is connected with the output shaft of the second driving piece, and the other crushing tooth is connected with the output shaft of the third driving piece.
According to the feather hydrolysis reaction tank disclosed by the utility model, the stirring blade comprises the inner stirring piece and the outer stirring piece, the inner stirring piece is connected with the output shaft of the first driving piece, a connecting rod is arranged between the inner stirring piece and the outer stirring piece, and the inner stirring piece is connected with the outer stirring piece through the connecting rod.
According to the feather hydrolysis reaction tank disclosed by the utility model, the bottom of the discharge hole is provided with the movable collecting box, the opening of the collecting box is matched with the discharge hole, the side wall of the collecting box is provided with the pump body, and the extraction hole of the pump body extends into the collecting box.
According to the feather hydrolysis reaction tank disclosed by the utility model, the bottom of the collecting box is provided with the movable wheels, two sliding blocks are oppositely arranged at the opening of the collecting box, and the bottom of the discharge hole is provided with the sliding rail matched with the sliding blocks.
According to the feather hydrolysis reaction tank disclosed by the utility model, the cover plate is arranged at the feed inlet in a sliding manner, the feed inlet is completely plugged by the cover plate, and a sealing gasket is arranged on one surface, which is attached to the feed inlet, of the cover plate.
According to the feather hydrolysis reaction tank disclosed by the utility model, the sealing plate is inserted at the discharge hole, the discharge hole is completely sealed by the sealing plate, and the sealing gasket is wrapped on the surface of the sealing plate.
The utility model provides a feather hydrolysis reaction tank, which has the beneficial effects that:
1. the hydrolysis pipe is communicated with an external high-temperature high-pressure source, and a plurality of connecting pipes are connected to the hydrolysis pipe; the outside high temperature and high pressure enter the tank body through the connecting pipe, and the feather in the tank body is hydrolyzed; the side end of the tank body is provided with a first driving piece, an output shaft of the first driving piece is rotationally connected between the two side ends of the tank body, and the output shaft of the first driving piece is provided with stirring blades; when the connecting pipe hydrolyzes the feathers, the stirring blades continuously stir the feathers in the tank body, and the feathers are uniformly hydrolyzed in the tank body.
2. The drying pipe is arranged on the outer wall of the tank body and is communicated with an external hot air source; after the hydrolysis is completed, the device can directly dry the hydrolyzed feathers in the tank body through the air inlet pipe on the drying pipe, so that the subsequent drying process is omitted, and the cost is saved; and stirring vane can stir the feather when the stoving, and supplementary feather stoving shortens the duration that the feather was dried, and the stoving effect is better.
3. The passing feathers can be crushed by rotationally connecting two mutually matched crushing teeth on the side wall of the discharge hole; when the dried feathers are discharged from the discharge hole, the two crushing teeth continuously crush and crush the passed feathers, so that the dried feathers are directly crushed, the subsequent crushing treatment process is omitted, and the cost is saved.
4. The bottom of the discharge hole is provided with a collecting box, a pump body is arranged on the side wall of the collecting box, and an extraction hole of the pump body extends into the collecting box; after the pump body is opened, negative pressure is generated in the collecting box, air flow is generated between the collecting box and the tank body, and feathers in the tank body are attracted into the collecting box, so that the collecting effect is achieved.
Drawings
FIG. 1 is a schematic view of the overall structure of the present utility model;
FIG. 2 is a schematic view of the semi-sectional structure of the present utility model;
FIG. 3 is a schematic view of the pulverizing assembly of the present utility model;
FIG. 4 is a schematic diagram of the connection between the collecting box and the discharge port according to the present utility model;
in the figure, the tank body 1, the feed inlet 11, the cover plate 111, the discharge outlet 12, the slide rail 121, the sealing plate 122, the stirring assembly 2, the driving part I21, the stirring blade 22, the hydrolysis tube 3, the air inlet tube 4, the drying tube 5, the crushing assembly 6, the crushing teeth 61, the driving part II 62, the driving part III 63, the collecting box 7, the pump body 71 and the sliding block 72 are arranged.
Detailed Description
For the purpose of making apparent the objects, technical solutions and advantages of the present utility model, the present utility model will be further described in detail with reference to the accompanying drawings and examples, it being understood that the specific examples described herein are for illustration only and are not intended to limit the present utility model.
It should be noted that, in the description of the present utility model, terms such as "upper," "lower," "left," "right," "inner," "outer," and the like indicate directions or positional relationships based on the directions or positional relationships shown in the drawings, which are merely for convenience of description, and do not indicate or imply that the apparatus or elements must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
Furthermore, it should be noted that, in the description of the present utility model, unless explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model can be understood by those skilled in the art according to the specific circumstances.
Referring to fig. 1 and 2, the utility model provides a feather hydrolysis reaction tank, which comprises a tank body 1, a stirring assembly 2 and an external high-temperature high-pressure source; the top of the tank body 1 is provided with a feed inlet 11, the bottom center of the tank body 1 is provided with a discharge outlet 12, and both ends of the bottom of the tank body 1 are provided with pressure relief openings; the outer wall of the tank body 1 is provided with a hydrolysis pipe 3, the hydrolysis pipe 3 is communicated with an external high-temperature high-pressure source, the hydrolysis pipe 3 is connected with a plurality of connecting pipes, and the connecting pipes extend into the tank body 1 after penetrating through the tank body 1; therefore, the outside high temperature and high pressure enter the tank body 1 through the connecting pipe to hydrolyze the feathers in the tank body 1; the stirring assembly 2 comprises a first driving piece 21 arranged at the side end of the tank body 1, an output shaft of the first driving piece 21 is rotationally connected between the two side ends of the tank body 1, and a stirring blade 22 is arranged on the output shaft of the first driving piece 21; therefore, when the connecting pipe hydrolyzes the feathers in the tank body 1, the stirring blades 22 continuously stir the feathers in the tank body 1, so that the feathers are uniformly hydrolyzed in the tank body 1, and the time for hydrolyzing the feathers is shortened.
Specifically, the first driving member 21 of the present utility model is a gear motor, and one skilled in the art can select other driving members 21 according to practical situations.
Specifically, seven connecting pipes are equidistantly distributed and connected to the hydrolysis pipe 3, and a person skilled in the art can choose to arrange other numbers of connecting pipes on the hydrolysis pipe 3 according to practical situations.
Referring to fig. 1 and 2, specifically, a drying pipe 5 is installed on the outer wall of the tank body 1, the drying pipe 5 is communicated with an external hot air source, a plurality of air inlet pipes 4 are connected to the drying pipe 5, and the plurality of air inlet pipes 4 extend into the tank body 1 after penetrating through the tank body 1; therefore, after the hydrolysis of the feathers in the tank body 1 is finished, the hydrolyzed feathers in the tank body 1 can be directly dried through the air inlet pipe 4 on the drying pipe 5, so that the subsequent drying process is omitted, and the cost is saved; and stirring vane 22 can constantly stir the feather when the stoving, and supplementary feather stoving shortens the length of feather stoving, makes the stoving effect better.
Specifically, seven air inlet pipes 4 are equidistantly connected to the drying pipe 5, and a person skilled in the art can choose to arrange other numbers of air inlet pipes 4 on the drying pipe 5 according to actual conditions.
Referring to fig. 1 to 3, in particular, the crushing assembly 6 comprises two mutually cooperating crushing teeth 61, both crushing teeth 61 being rotatably connected to the side wall of the discharge opening 12; the outer wall of the discharge hole 12 is provided with a second driving piece 62 and a third driving piece 63, one of the two crushing teeth 61 is connected with the output shaft of the second driving piece 62, and the other crushing tooth is connected with the output shaft of the third driving piece 63; therefore, when the dried feathers are discharged from the discharge hole 12, the crushing teeth 61 connected with the output shaft of the second driving piece 62 are driven by the second driving piece 62 to rotate towards the third driving piece 63, and the crushing teeth 61 connected with the output shaft of the third driving piece 63 are driven by the third driving piece 63 to rotate towards the second driving piece 62; so that the passing feathers are continuously crushed by means of the two crushing teeth 61, the subsequent crushing treatment process is omitted, and the cost is saved.
Specifically, the second driving member 62 and the third driving member 63 of the present utility model are all gear motors, and a person skilled in the art can select other second driving member 62 and third driving member 63 according to practical situations.
Referring to fig. 1 and 2, specifically, a movable collecting box 7 is arranged at the bottom of a discharge hole 12, an opening of the collecting box 7 is matched with the discharge hole 12, a pump body 71 is mounted on the side wall of the collecting box 7, and an extraction hole of the pump body 71 extends into the collecting box 7; therefore, after the pump body 71 is opened, negative pressure can be generated in the collecting box 7, air flow is generated between the collecting box 7 and the tank body 1, the feathers in the tank body 1 are attracted into the collecting box 7, the collecting effect is achieved, and the feathers are assisted to be discharged from the discharge hole 12.
Referring to fig. 2 and 4, it is preferable that a moving wheel is arranged at the bottom of the collecting box 7, so that the collecting box 7 can move, and the collected feathers can be conveniently moved; two sliding blocks 72 are symmetrically arranged at the opening of the collecting box 7 based on the center of the opening, and a sliding rail 121 matched with the sliding blocks 72 is arranged at the bottom of the discharging hole 12; therefore, after the sliding blocks 72 of the collecting box 7 slide into the sliding rails 121 of the discharge hole 12, the collecting box 7 can be connected with the discharge hole 12, and the collecting box 7 is prevented from displacing when collecting feathers.
Preferably, the stirring blade 22 comprises an inner stirring sheet and an outer stirring sheet, the inner stirring sheet is connected with the output shaft of the first driving piece 21, a connecting rod is arranged between the inner stirring sheet and the outer stirring sheet, and the inner stirring sheet is connected with the outer stirring sheet through the connecting rod; thereby, the stirring blade 22 has a wider stirring range, a better stirring effect and assists in the hydrolysis of the feathers, so that the hydrolysis of the feathers is more complete.
Preferably, two opposite sides of the feed inlet 11 are provided with slide ways, the cover plate 111 is arranged between the two slide ways in a sliding manner, and the cover plate 111 completely seals the feed inlet 11; therefore, after the feathers enter the tank body 1, the feed inlet 11 can be completely closed through the cover plate 111, so that the feathers are prevented from flying out of the feed inlet 11 when the stirring blades 22 stir; and a sealing gasket is arranged on one surface of the cover plate 111, which is attached to the feed inlet 11, so that high-pressure gas in the tank body 1 is prevented from leaking.
Referring to fig. 1 and 2, preferably, a sealing plate 122 is inserted at the discharge port 12, and the discharge port 12 is completely sealed after the sealing plate 122 is inserted; thereby, the discharge hole 12 can be completely closed by the sealing plate 122, and feathers are prevented from flying out of the discharge hole 12 when the stirring blades 22 stir; and the surface of the sealing plate 122 is wrapped with a sealing gasket to prevent the leakage of the high-pressure gas in the tank 1.
The working process of the utility model is as follows: adding pretreated feathers into the tank body 1 from a feed inlet 11, and closing the feed inlet 11 by using a cover plate 111; then the outside high-temperature high-pressure source is opened, and the high-temperature high-pressure source is led into the tank body 1 through the connecting pipe after passing through the hydrolysis pipe 3; at the moment, the first driving part 21 is started, and the output shaft of the first driving part 21 drives the stirring blade 22 to continuously stir the feathers in the tank body 1, so that the feathers start to generate hydrolysis reaction in the tank body 1; after the hydrolysis of the feathers is completed, closing an external high-temperature high-pressure source, opening pressure relief openings at two ends of the bottom of the tank body 1, and discharging high pressure; then an external hot air source is started, hot air is guided into the tank body 1 through the drying pipe 5 and then is guided into the air inlet pipe 4, the hydrolyzed feathers in the tank body 1 are dried, and meanwhile, the stirring blades 22 continuously stir the feathers during drying to assist in drying the feathers; after the feathers are dried, the first driving piece 21 and an external hot air source are closed, and the second driving piece 62 and the third driving piece 63 are opened; the second driving part 62 drives the crushing teeth 61 connected with the output shaft of the second driving part to rotate to the third driving part 63 side, the third driving part 63 drives the crushing teeth 61 connected with the output shaft of the second driving part 62 to rotate to the second driving part side, at the moment, the sealing plate 122 is pulled out, the feathers in the tank body 1 drop downwards, and the feathers drop into the collecting box 7 after being crushed by the crushing teeth 61; the pump body 71 can be opened after the sealing plate 122 is pulled out, the pump body 71 generates flowing air flow between the collecting box 7 and the tank body 1, the feathers in the tank body 1 are assisted to move into the discharge hole 12, the feathers falling into the discharge hole 12 are crushed by the crushing teeth 61 and then fall into the collecting box 7, and finally the collecting box 7 is dragged to take away the crushed feathers.
In summary, the utility model provides a feather hydrolysis reaction tank, which is characterized in that a hydrolysis pipe is communicated with an external high-temperature high-pressure source, and a plurality of connecting pipes are connected to the hydrolysis pipe; the outside high temperature and high pressure enter the tank body through the connecting pipe, and the feather in the tank body is hydrolyzed; the side end of the tank body is provided with a first driving piece, an output shaft of the first driving piece is rotationally connected between the two side ends of the tank body, and the output shaft of the first driving piece is provided with stirring blades; the feather in the tank body is continuously stirred by the stirring blade while the feather is hydrolyzed by the connecting pipe, so that the feather is uniformly hydrolyzed in the tank body; the drying pipe is arranged on the outer wall of the tank body and is communicated with an external hot air source; after the hydrolysis is completed, the device can directly dry the hydrolyzed feathers in the tank body through the air inlet pipe on the drying pipe, so that the subsequent drying process is omitted, and the cost is saved; the stirring blade can stir the feathers during drying, assist in drying the feathers, shorten the drying time of the feathers and achieve better drying effect; the passing feathers can be crushed by rotationally connecting two mutually matched crushing teeth on the side wall of the discharge hole; when the dried feathers are discharged from the discharge hole, the two crushing teeth continuously crush and crush the passed feathers, so that the dried feathers are directly crushed, the subsequent crushing treatment process is omitted, and the cost is saved; the bottom of the discharge hole is provided with a collecting box, a pump body is arranged on the side wall of the collecting box, and an extraction hole of the pump body extends into the collecting box; after the pump body is opened, negative pressure is generated in the collecting box, air flow is generated between the collecting box and the tank body, and feathers in the tank body are attracted into the collecting box, so that the collecting effect is achieved.
Of course, the present utility model is capable of other various embodiments and its several details are capable of modification and variation in light of the present utility model, as will be apparent to those skilled in the art, without departing from the spirit and scope of the utility model as defined in the appended claims.
Claims (8)
1. The feather hydrolysis reaction tank is characterized by comprising a tank body, a stirring assembly and an external high-temperature high-pressure source;
the top of the tank body is provided with a feed inlet, the outer wall of the tank body is provided with a hydrolysis pipe, the hydrolysis pipe is communicated with an external high-temperature high-pressure source, the hydrolysis pipe is connected with a plurality of connecting pipes, the connecting pipes extend into the tank body after penetrating through the tank body, the bottom of the tank body is provided with a discharge hole, the discharge hole is internally provided with a crushing assembly, and the crushing assembly is used for crushing feathers entering the discharge hole;
the stirring assembly comprises a first driving piece arranged at the side end of the tank body, an output shaft of the first driving piece is rotationally connected between the two side ends of the tank body, and stirring blades are arranged on the output shaft of the first driving piece.
2. The feather hydrolysis reaction tank of claim 1, wherein a drying pipe is arranged on the outer wall of the tank body, the feather hydrolysis reaction tank is further provided with an external hot air source, the drying pipe is communicated with the external hot air source, the drying pipe is connected with a plurality of air inlet pipes, and a plurality of air inlet pipes extend into the tank body after penetrating through the tank body.
3. The feather hydrolysis reaction tank of claim 1 wherein the crushing assembly comprises two mutually matched crushing teeth, wherein the two crushing teeth are both rotatably connected to the side wall of the discharge port, a second driving member and a third driving member are mounted on the outer wall of the discharge port, one of the two crushing teeth is connected with the output shaft of the second driving member, and the other crushing tooth is connected with the output shaft of the third driving member.
4. The feather hydrolysis reaction tank of claim 1 wherein the stirring blade comprises an inner stirring blade and an outer stirring blade, the inner stirring blade is connected with an output shaft of the first driving element, a connecting rod is arranged between the inner stirring blade and the outer stirring blade, and the inner stirring blade is connected with the outer stirring blade through the connecting rod.
5. The feather hydrolysis reaction tank of claim 1 wherein a movable collection box is arranged at the bottom of the discharge hole, an opening of the collection box is matched with the discharge hole, a pump body is mounted on the side wall of the collection box, and an extraction hole of the pump body extends into the collection box.
6. The feather hydrolysis reaction tank of claim 5 wherein a moving wheel is arranged at the bottom of the collecting box, two sliding blocks are oppositely arranged at the opening of the collecting box, and a sliding rail matched with the sliding blocks is arranged at the bottom of the discharging hole.
7. The feather hydrolysis reaction tank of claim 1, wherein a cover plate is slidably arranged at the feed inlet, the cover plate completely seals the feed inlet, and a sealing gasket is arranged on one surface of the cover plate, which is attached to the feed inlet.
8. The feather hydrolysis reaction tank of claim 1 wherein a sealing plate is inserted at the discharge port, the sealing plate completely seals the discharge port, and a sealing gasket is wrapped on the surface of the sealing plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322045306.6U CN219596563U (en) | 2023-08-01 | 2023-08-01 | Feather hydrolysis reaction tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322045306.6U CN219596563U (en) | 2023-08-01 | 2023-08-01 | Feather hydrolysis reaction tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219596563U true CN219596563U (en) | 2023-08-29 |
Family
ID=87741938
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322045306.6U Active CN219596563U (en) | 2023-08-01 | 2023-08-01 | Feather hydrolysis reaction tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219596563U (en) |
-
2023
- 2023-08-01 CN CN202322045306.6U patent/CN219596563U/en active Active
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