CN215741838U - Centrifugal atomization drying equipment is used in plasma powder production - Google Patents
Centrifugal atomization drying equipment is used in plasma powder production Download PDFInfo
- Publication number
- CN215741838U CN215741838U CN202122404608.9U CN202122404608U CN215741838U CN 215741838 U CN215741838 U CN 215741838U CN 202122404608 U CN202122404608 U CN 202122404608U CN 215741838 U CN215741838 U CN 215741838U
- Authority
- CN
- China
- Prior art keywords
- tower body
- pipe
- plasma powder
- powder production
- centrifugal atomization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
The utility model discloses centrifugal atomization drying equipment for plasma powder production, which comprises a tower body, an atomization nozzle mechanism, a driving mechanism and a heat recovery mechanism, wherein the atomization nozzle mechanism is arranged at the top of the inner side of the tower body, the driving mechanism is arranged at the top of the outer side of the tower body and is in transmission connection with the atomization nozzle mechanism, a spiral heating pipe is arranged on the inner wall of the tower body, an air inlet pipe connected with the spiral heating pipe is arranged at the upper part of the tower body, an air outlet pipe is arranged at the lower part of the tower body, and the heat recovery mechanism is connected with the air inlet pipe and the air outlet pipe. On one hand, the centrifugal atomization drying equipment of the utility model conveys the used hot air back to the tower body again for recycling through the heat recovery mechanism, thereby reducing the energy consumption; on the other hand has promoted the spray drying efficiency of plasma powder through atomizer mechanism, and then has promoted production efficiency.
Description
Technical Field
The utility model relates to the technical field of atomization drying, in particular to centrifugal atomization drying equipment for plasma powder production.
Background
The spray drier is a drying device commonly used in the production process of plasma powder, blood is added with anticoagulant in a slaughterhouse and collected, then the blood is put into a tank to be refrigerated to below 10 ℃, and the blood is transported back to a factory by a stainless steel heat-preservation tank. Detecting raw material sense organ and water content after arriving at factory, filtering, refrigerating at temperature below 10 deg.C, drying raw blood in spray dryer, weighing, and packaging.
The existing spray dryer usually adopts a natural gas burner to heat air, then the air is introduced into a drying tower to dry blood droplets, and the dried hot air is directly discharged, so that energy waste is caused; in addition, most of the existing spray dryers are of a single-nozzle structure, and the atomization drying efficiency is low.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model discloses centrifugal atomization drying equipment for plasma powder production, which comprises a tower body, an atomization nozzle mechanism, a driving mechanism and a heat recovery mechanism, wherein the atomization nozzle mechanism is arranged at the top of the inner side of the tower body, the driving mechanism is arranged at the top of the outer side of the tower body and is in transmission connection with the atomization nozzle mechanism, a spiral heating pipe is arranged on the inner wall of the tower body, an air inlet pipe connected with the spiral heating pipe is arranged at the upper part of the tower body, an air outlet pipe is arranged at the lower part of the tower body, and the heat recovery mechanism is connected with the air inlet pipe and the air outlet pipe.
Further, the heat recovery mechanism comprises a low-pressure fan and a gas pipe, an air inlet of the low-pressure fan is connected with the gas outlet pipe, and an air outlet of the low-pressure fan is connected with the gas inlet pipe through the gas pipe.
Furthermore, a one-way valve is arranged on the air inlet pipe and positioned on the outer side of the joint of the air delivery pipe and the air inlet pipe.
Further, atomizer mechanism includes inlet pipe, feed tray and atomizer group, the inlet pipe sets up feed tray top and the two communicates each other, atomizer group equipartition is in the feed tray below.
Further, the atomizing nozzle group comprises a first nozzle arranged in the center of the feeding disc, a plurality of second nozzles arranged around the first nozzle, and a plurality of third nozzles arranged around the first nozzle and positioned outside the second nozzles.
Furthermore, the first spray head is arranged along the vertical direction, the second spray heads are arranged at an angle alpha to the vertical direction, and the third spray heads are arranged at an angle beta to the vertical direction.
Further, actuating mechanism includes driving motor, first helical gear and second helical gear, driving motor through first helical gear with the transmission of second helical gear is connected, the second helical gear sets up on the outer wall of inlet pipe.
Furthermore, a plurality of air outlet holes are formed in the spiral heating pipe.
Furthermore, the junction of outlet duct and tower body is equipped with detachable and crosses filter pulp.
Further, tower body bottom is equipped with the case that gathers materials, it is equipped with shock dynamo to gather materials the case lateral wall.
The utility model has the beneficial effects that:
on one hand, the centrifugal atomization drying equipment of the utility model conveys the used hot air back to the tower body again for recycling through the heat recovery mechanism, thereby reducing the energy consumption; on the other hand has promoted the spray drying efficiency of plasma powder through atomizer mechanism, and then has promoted production efficiency.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without inventive labor.
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of a partial structure of the atomizer mechanism according to the present invention;
fig. 3 is a schematic view of the bottom structure of the feed tray of the present invention.
Reference numerals:
1-a tower body; 2-a spiral heating pipe; 3, an air inlet pipe; 4-air outlet pipe; 5-air outlet holes; 6-filtering cotton; 7-collecting box; 8-a vibration motor; 9-a discharge hole; 10-low pressure fan; 11-gas pipe; 12-a one-way valve; 13-a drive motor; 14-a first bevel gear; 15-a second bevel gear; 16-a feed pipe; 17-a feed tray; 18-a first spray head; 19-a second spray head; 20-third spray head.
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 a part of the embodiments of the present invention, and not all of the embodiments.
It should be noted that all the directional indicators (such as up, down, left, right, front, and rear … …) in the embodiment of the present invention are only used to explain the relative position relationship between the components, the movement situation, etc. in a specific posture (as shown in the drawing), and if the specific posture is changed, the directional indicator is changed accordingly.
In addition, the descriptions related to "first", "second", etc. in the present invention are for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature.
In the description of the embodiments, the terms "disposed," "connected," and the like are to be construed broadly unless otherwise explicitly specified or limited. For example, the connection can be fixed, detachable or integrated; can be mechanically or electrically connected; either directly or through an intervening medium, or through internal communication between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As shown in fig. 1, the centrifugal atomization drying device for plasma powder production of this embodiment includes tower body 1, atomizer mechanism, actuating mechanism and heat recovery mechanism, and atomizer mechanism sets up at the inboard top of tower body 1, and actuating mechanism sets up at the 1 outside top of tower body and is connected with atomizer mechanism transmission.
The inner wall of the tower body 1 is provided with a spiral heating pipe 2, the upper part of the tower body 1 is provided with an air inlet pipe 3 connected with the spiral heating pipe 2, the lower part of the tower body 1 is provided with an air outlet pipe 4, and the heat recovery mechanism is connected with the air inlet pipe 3 and the air outlet pipe 4.
A plurality of air outlet holes 5 are arranged on the spiral heating pipe 2, and detachable filter cotton 6 is arranged at the joint of the air outlet pipe 4 and the tower body 1.
The bottom of the tower body 1 is provided with a material collecting box 7, and the side wall of the material collecting box 7 is provided with a vibration motor 8 so as to shake off materials attached to the inside of the material collecting box 7; the bottom of the material collecting box 7 is provided with a material outlet 9 so as to collect materials.
The heat recovery mechanism comprises a low-pressure fan 10 and a gas pipe 11, an air inlet of the low-pressure fan 10 is connected with the gas outlet pipe 4, and an air outlet of the low-pressure fan 10 is connected with the gas pipe 3 through the gas pipe 11; the outside that is located gas-supply pipe 11 and 3 junctions of intake pipe on the intake pipe 3 is equipped with check valve 12 to guarantee that steam can only circulate to inside from the outside of tower body 1.
The driving mechanism comprises a driving motor 13, a first bevel gear 14 and a second bevel gear 15, and the driving motor 13 is in transmission connection with the second bevel gear 15 through the first bevel gear 14.
As shown in fig. 2-3, the atomizer mechanism includes a feeding pipe 16, a feeding tray 17, and atomizer groups, the feeding pipe 16 is disposed above the feeding tray 17 and is communicated with the feeding tray 17, and the atomizer groups are uniformly distributed below the feeding tray 17.
The atomizing nozzle group includes a first nozzle 18 disposed at the center of the feed tray 17, a plurality of second nozzles 19 disposed around the first nozzle 18, and a plurality of third nozzles 20 disposed around the first nozzle 18 and located outside the second nozzles 19.
The first spray head 18 is arranged along the vertical direction, the plurality of second spray heads 19 are arranged at an angle alpha to the vertical direction, and the plurality of third spray heads 20 are arranged at an angle beta to the vertical direction; wherein the alpha angle is set to be 5-10 degrees, and the beta angle is set to be 15-30 degrees.
The second bevel gear 17 is arranged on the outer wall of the feeding pipe 16, so that the driving motor 13 drives the feeding disc 17 to rotate at a high speed, and blood is changed into tiny fogdrops by the spraying of the atomizing nozzle group and the action of centrifugal force and is dispersed in the tower body 1. Hot air enters the tower body 1 through the spiral heating pipe 2, and the fog drops are dried into powdery small particles and are settled in a material collecting box 7 below. The used hot air is sucked by the low-pressure fan 10 and then returns to the tower body 1 through the air outlet pipe 4, the air delivery pipe 11 and the air inlet pipe 3 for cyclic utilization, so that the energy consumption is reduced, and the energy conservation and the environmental protection are facilitated.
The filter cotton 6 can prevent blood powder from entering the air outlet pipe 4, and can be replaced when the filtering efficiency of the filter cotton 6 is reduced.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the utility model, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein. In addition, the technical solutions between the various embodiments can be combined with each other, but must be based on the realization of those skilled in the art; where combinations of features are mutually inconsistent or impractical, such combinations should not be considered as being absent and not within the scope of the claimed invention.
Claims (10)
1. The utility model provides a plasma powder production is with centrifugation atomizing drying equipment which characterized in that: including tower body, atomizer mechanism, actuating mechanism and heat recovery mechanism, atomizer mechanism sets up the inboard top of tower body, actuating mechanism sets up tower body outside top and with atomizer mechanism transmission is connected, the tower body inner wall is equipped with the spiral heating pipe, tower body upper portion be equipped with the intake pipe that the spiral heating pipe is connected, the tower body lower part is equipped with the outlet duct, heat recovery mechanism connects the intake pipe with the outlet duct.
2. The centrifugal atomization drying device for plasma powder production according to claim 1, characterized in that: the heat recovery mechanism comprises a low-pressure fan and a gas pipe, the air inlet of the low-pressure fan is connected with the gas outlet pipe, and the air outlet of the low-pressure fan is connected with the gas inlet pipe through the gas pipe.
3. The centrifugal atomization drying device for plasma powder production according to claim 2, characterized in that: and a one-way valve is arranged on the air inlet pipe and positioned at the outer side of the joint of the air delivery pipe and the air inlet pipe.
4. The centrifugal atomization drying device for plasma powder production according to claim 1, characterized in that: atomizer mechanism includes inlet pipe, feed tray and atomizer group, the inlet pipe sets up feed tray top and the two communicates each other, atomizer group equipartition is in feed tray below.
5. The centrifugal atomization drying device for plasma powder production according to claim 4, characterized in that: the atomizing nozzle group comprises a first nozzle arranged at the center of the feeding disc, a plurality of second nozzles arranged around the first nozzle, and a plurality of third nozzles arranged around the first nozzle and positioned outside the second nozzles.
6. The centrifugal atomization drying device for plasma powder production according to claim 5, characterized in that: the first spray head is arranged along the vertical direction, the second spray heads are arranged at an alpha angle with the vertical direction, and the third spray heads are arranged at a beta angle with the vertical direction.
7. The centrifugal atomization drying device for plasma powder production according to claim 4, characterized in that: the driving mechanism comprises a driving motor, a first bevel gear and a second bevel gear, the driving motor is in transmission connection with the second bevel gear through the first bevel gear, and the second bevel gear is arranged on the outer wall of the feeding pipe.
8. The centrifugal atomization drying device for plasma powder production according to claim 1, characterized in that: the spiral heating pipe is provided with a plurality of air outlet holes.
9. The centrifugal atomization drying device for plasma powder production according to claim 1, characterized in that: the junction of outlet duct and tower body is equipped with detachable and crosses the filter pulp.
10. The centrifugal atomization drying device for plasma powder production according to claim 1, characterized in that: the tower body bottom is equipped with the case that gathers materials, it is equipped with shock dynamo to gather materials the case lateral wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122404608.9U CN215741838U (en) | 2021-09-30 | 2021-09-30 | Centrifugal atomization drying equipment is used in plasma powder production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122404608.9U CN215741838U (en) | 2021-09-30 | 2021-09-30 | Centrifugal atomization drying equipment is used in plasma powder production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215741838U true CN215741838U (en) | 2022-02-08 |
Family
ID=80092832
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122404608.9U Active CN215741838U (en) | 2021-09-30 | 2021-09-30 | Centrifugal atomization drying equipment is used in plasma powder production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215741838U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116474641A (en) * | 2023-03-29 | 2023-07-25 | 山东托普医药科技有限公司 | Injection mechanism and intelligent medicine preparation device |
-
2021
- 2021-09-30 CN CN202122404608.9U patent/CN215741838U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116474641A (en) * | 2023-03-29 | 2023-07-25 | 山东托普医药科技有限公司 | Injection mechanism and intelligent medicine preparation device |
| CN116474641B (en) * | 2023-03-29 | 2024-01-16 | 山东托普医药科技有限公司 | Injection mechanism and intelligent medicine preparation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN215741838U (en) | Centrifugal atomization drying equipment is used in plasma powder production | |
| CN107398084A (en) | Atomizing liquid drying machine | |
| CN206715885U (en) | Fluidbedgranulatingdrier | |
| CN108302907A (en) | A kind of onboard integrated Grain drier and its drying means | |
| CN207871566U (en) | A kind of centrifugal spray drying device | |
| CN214763345U (en) | Drying tower | |
| CN207981459U (en) | A kind of centrifugal atomization apparatus | |
| CN207126149U (en) | Spray drier for Chinese medicine extract | |
| CN216571561U (en) | Spray drying tower and equipment for producing protein powder by using leather waste | |
| CN110075652A (en) | A kind of grain drier exhaust gas Combined dust-cleaning apparatus | |
| CN206478799U (en) | A kind of middle spray axial fan | |
| CN211752552U (en) | High-speed centrifugal spraying device | |
| CN210473081U (en) | Centrifugal spray drier | |
| CN208465208U (en) | A kind of centrifugal spray dryer | |
| CN209185109U (en) | A kind of condensing hot air furnace humidifier | |
| CN208599197U (en) | Prepare the spray-drying installation of nano material | |
| CN208320021U (en) | A kind of vegetation water extraction drying device | |
| CN208893650U (en) | A kind of Chinese medicinal material extract spray-drying installation | |
| CN211353754U (en) | Centrifugal spray dryer special for formula milk powder | |
| CN207286712U (en) | A kind of spray dryer of centrifugal atomizer | |
| CN207734623U (en) | A kind of highly effective drying tower | |
| CN207941214U (en) | A kind of Highspeedcentrifugingandsprayingdrier | |
| CN208482198U (en) | Deduster and cleaner | |
| CN212566751U (en) | Spray dryer for collagen powder or collagen peptide | |
| CN206063817U (en) | A kind of novel atomizing drying machine with filtering function |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |