CN212620013U - Boiling dryer - Google Patents
Boiling dryer Download PDFInfo
- Publication number
- CN212620013U CN212620013U CN202021225161.8U CN202021225161U CN212620013U CN 212620013 U CN212620013 U CN 212620013U CN 202021225161 U CN202021225161 U CN 202021225161U CN 212620013 U CN212620013 U CN 212620013U
- Authority
- CN
- China
- Prior art keywords
- fixedly connected
- chamber
- air
- boiling
- fan
- 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
Abstract
The utility model discloses a fluidized drying machine, including organism, boiling chamber and ejection of compact otter board, inner chamber of the body fixed mounting has the boiling chamber, inner chamber of the boiling chamber top fixed mounting has ejection of compact otter board, organism one end fixed mounting has the swirl air pump, the material jar is gone up in the pipeline fixedly connected with vacuum in swirl air pump top, material jar bottom fixedly connected with feeding fan is gone up in the vacuum. The utility model discloses an air cleaner can carry out filtration purification to the air, avoid the dust in the air to cause the pollution to the raw materials, through the pneumatic rotatory governing valve of control, adjust the size of discharge gate, by the preceding board mode of taking out, change present arc pneumatic regulating device into, to the regulation size of dry discharge gate in the ejection of compact, thereby can adjust the discharge rate of raw materials, it is more convenient to use, and can be to dry discharge gate self-closing in the dry time, thereby can play sealed effect, high durability and convenient use, and the operation is simple.
Description
Technical Field
The utility model relates to a drying equipment technical field specifically is a fluidized drying machine.
Background
The fluidized dryer can improve the fluidity and reduce the flying of dust by powder granulation; the dissolution performance of the powder is improved by granulation; mixing, granulating and drying to complete one-step granulation in one machine; the antistatic filter cloth is adopted, so that the equipment is safe to operate; a pressure relief hole is arranged, so that equipment personnel are not injured once explosion happens; the equipment has no dead angle, the loading and unloading are light and quick, the washing is clean, and the GMP standard is met.
However, the existing boiling dryer has the following disadvantages in the use process:
boiling dryer is when carrying out the drying to the raw materials, and the air of injection into in the boiling chamber does not filter to there is a large amount of dusts in the guide pillar boiling chamber, thereby influences the quality of raw materials, and what ordinary horizontal boiling dryer discharging device adopted simultaneously is to take out the board mode from top to bottom, and manual work or cylinder operation are difficult to the size of control ejection of compact, use very inconvenient.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a fluidized drying machine to solve the problem among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: a boiling dryer comprises a dryer body, a boiling chamber and a discharge screen plate, wherein the boiling chamber is fixedly arranged in an inner cavity of the dryer body, the discharge screen plate is fixedly arranged at the top of the inner cavity of the boiling chamber, a vortex air pump is fixedly arranged at one end of the dryer body, the top of the vortex air pump is fixedly connected with a vacuum feeding tank through a pipeline, the bottom of the vacuum feeding tank is fixedly connected with a feeding fan, the air outlet end of the feeding fan is fixedly connected with the boiling chamber, an air supply fan is fixedly arranged at one side of the dryer body, the air outlet end of the air supply fan is fixedly connected with a steam heater through a pipeline, the air outlet end of the steam heater is fixedly connected with a hot air inlet hopper through a pipeline, the hot air inlet hoppers are provided with a plurality of groups and are all connected to the bottom of the boiling chamber, a main air pipe is fixedly connected to, one end of the machine body is fixedly provided with a drying discharge port, the vortex air pump is connected with a vacuum feeding tank through a pipeline, the vortex air pump generates high-speed airflow, so that the inner cavity of the vacuum feeding tank generates negative pressure, the raw material in the conveying pipeline can be discharged into the inner cavity of the boiling chamber under the action of the negative pressure, a feeding fan is arranged at the joint of the vacuum feeding tank and the boiling chamber, forward thrust can be applied to the raw material through the feeding fan, so that the injection speed of the raw material can be effectively increased, the raw material is connected and held through a discharge screen plate after entering the inner cavity of the boiling chamber, air can be injected into the inner cavity of the boiling chamber through an air supply fan, one end of the air supply fan is connected with an air filter, air can be filtered and purified through the air filter, the pollution of dust in the air to the raw material is avoided, the, the hot air is blown into the boiling chamber through the hot air inlet hopper, so that the raw materials can be heated and baked through hot steam, the raw materials are dried quickly, the air blocking balls are arranged in the inner cavities of the hot air inlet hopper, when air enters the hot air inlet hopper, the air blocking balls are blown by the air, when the air inlet is stopped, the air blocking balls fall under the action of gravity, the hot air inlet hopper can be sealed, the heat loss of the inner cavity of the boiling chamber is reduced, the energy loss can be effectively reduced, after the raw materials are dried, hot air in the boiling chamber is guided into the settling chamber through the main air pipe, substances with larger particles in hot air flow can be settled through the settling chamber, the air flow flows into the cyclone separation chamber after the settlement, small particle substances in the air flow can be separated again through the cyclone separation chamber, the discharged air is cleaner, and the pollution to the environment is reduced.
Preferably, the air supply fan is provided with two sets of, but air filter purifies through air filter air intake end all through pipeline fixedly connected with air supply fan.
Preferably, the inner cavity of the hot air inlet hopper is movably provided with a wind blocking ball, the wind blocking ball is blown by wind when wind enters the hot air inlet hopper, and the wind blocking ball falls under the action of gravity when air inlet is stopped, so that the hot air inlet hopper can be sealed, the heat loss of the inner cavity of the boiling chamber is reduced, and the energy loss can be effectively reduced.
Preferably, the top of the cyclone separation chamber is fixedly connected with an induced draft fan through a pipeline, and the purified airflow can be discharged through the induced draft fan in an accelerated manner.
Preferably, dry discharge gate one side fixed mounting has out the hopper, go out hopper inner chamber fixed mounting and have pneumatic rotatory governing valve, through the pneumatic rotatory governing valve of control, adjust the size of discharge gate, by the preceding mode of taking out the board, change present arc pneumatic regulating device into, to the regulation size of dry discharge gate in the ejection of compact to can adjust the exhaust velocity of raw materials, it is more convenient to use, and can be to dry discharge gate self-closing in the time of dry, thereby can play sealed effect, high durability and convenient use, and easy operation.
Preferably, a discharge fan is fixedly mounted at the bottom of the discharge hopper, and the discharge speed can be increased through the discharge fan.
The utility model provides a fluidized drying machine possesses following beneficial effect:
(1) the utility model discloses an air cleaner can carry out filtration purification to the air, avoid the dust in the air to cause the pollution to the raw materials, the air supply fan other end has steam heater through the pipe connection, can heat the air through steam heater, and blow into the boiling chamber through hot air inlet fill, thereby accessible hot steam heats the raw materials and toasts, make the raw materials dry fast, hot air inlet fill inner chamber all is provided with the choke ball, the choke ball is blown by the wind when wind enters into hot air inlet fill, when the air inlet stops, the choke ball falls under the action of gravity, thereby can seal hot air inlet fill, with the heat loss in reduction boiling chamber inner chamber, can effectively reduce the loss of the energy like this.
(2) The utility model discloses a control pneumatic rotatory governing valve, adjust the size of discharge gate, by the preceding board mode of taking out, change present arc pneumatic adjusting device into, to the regulation size of dry discharge gate in the ejection of compact to can adjust the discharge velocity of raw materials, it is more convenient to use, and can be to dry discharge gate self-closing in the time of dry, thereby can play sealed effect, convenient to use, easy operation.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic side view of the present invention;
fig. 3 is a schematic top view of the present invention;
fig. 4 is a schematic view of the discharging structure of the present invention.
In the figure: 1. a body; 101. a boiling chamber; 102. a discharging screen plate; 2. a vortex air pump; 201. feeding the material in vacuum; 202. a feeding fan; 3. an air filter; 301. an air supply fan; 302. a steam heater; 303. a hot air inlet hopper; 304. a wind resistance ball; 4. a main air duct; 401. a settling chamber; 402. a cyclonic separation chamber; 403. an induced draft fan; 5 drying the discharge hole; 501. a discharge hopper; 502. a pneumatic rotary regulating valve; 503. and a discharge fan.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention.
As shown in fig. 1-4, the utility model provides a technical solution: a boiling dryer comprises a machine body 1, a boiling chamber 101 and a discharge screen plate 102, wherein the boiling chamber 101 is fixedly mounted in an inner cavity of the machine body 1, the discharge screen plate 102 is fixedly mounted at the top of the inner cavity of the boiling chamber 101, a vortex air pump 2 is fixedly mounted at one end of the machine body 1, the top of the vortex air pump 2 is fixedly connected with a vacuum charging bucket 201 through a pipeline, the bottom of the vacuum charging bucket 201 is fixedly connected with a feeding fan 202, the air outlet end of the feeding fan 202 is fixedly connected with the boiling chamber 101, an air supply fan 301 is fixedly mounted at one side of the machine body 1, the air outlet end of the air supply fan 301 is fixedly connected with a steam heater 302 through a pipeline, the air outlet end of the steam heater 302 is fixedly connected with a hot air inlet bucket 303 through a pipeline, the hot air inlet buckets 303 are provided with multiple groups and are all connected, one end of the main air pipe 4 is fixedly connected with a settling chamber 401, one end of the settling chamber 401 is fixedly connected with a cyclone separation chamber 402, one end of the machine body 1 is fixedly provided with a drying discharge hole 5, the vortex air pump 2 is connected with the vacuum feeding tank 201 through a pipeline, the vortex air pump 2 generates high-speed airflow so as to enable the inner cavity of the vacuum feeding tank 201 to generate negative pressure, raw materials in a conveying pipeline can be discharged into the inner cavity of the boiling chamber 101 under the action of the negative pressure, a feeding fan 202 is arranged at the joint of the vacuum feeding tank 201 and the boiling chamber 101, forward thrust can be exerted on the raw materials through the feeding fan 202, so that the injection speed of the raw materials can be effectively improved, the raw materials are received and held through a discharge screen plate 102 after entering the inner cavity of the boiling chamber 101, air can be injected into the inner cavity of the boiling chamber 101 through the air supply fan 301, one, the raw materials are prevented from being polluted by dust in the air, the other end of the air supply fan 301 is connected with a steam heater 302 through a pipeline, the air can be heated through the steam heater 302 and blown into the boiling chamber 101 through a hot air inlet hopper 303, so that the raw materials can be heated and baked through hot steam, the raw materials are dried quickly, the air blocking balls 304 are arranged in the inner cavities of the hot air inlet hopper 303, when air enters the hot air inlet hopper 303, the air blocking balls 304 are blown up by the air, when the air inlet stops, the air blocking balls 304 fall under the action of gravity, so that the hot air inlet hopper 303 can be sealed, the heat loss of the inner cavity of the boiling chamber 101 is reduced, the energy loss can be effectively reduced, after the raw materials are dried, hot air in the boiling chamber 101 is guided into a settling chamber 401 through a main air pipe 4, substances with larger particles in the hot air flow can be settled through the settling chamber 401, and the settled air flow enters a cyclone separation chamber 402, the cyclone chamber 402 can be used to separate the small particulate matter from the airflow again, thereby making the exhausted air cleaner and reducing environmental pollution.
The inner cavities of the hot air inlet hoppers 303 are movably provided with the wind blocking balls 304, when wind enters the hot air inlet hoppers 303, the wind blocking balls 304 are blown by the wind, and when the wind stops entering, the wind blocking balls 304 fall under the action of gravity, so that the hot air inlet hoppers 303 can be sealed, the heat loss of the inner cavities of the boiling chambers 101 is reduced, and the energy loss can be effectively reduced.
The top of the cyclone separation chamber 402 is fixedly connected with an induced draft fan 403 through a pipeline, and the purified airflow can be discharged through the induced draft fan 403 in an accelerated manner.
5 one side fixed mounting of dry discharge gate has a hopper 501, go out hopper 501 inner chamber fixed mounting and have pneumatic rotatory governing valve 502, through controlling pneumatic rotatory governing valve 502, adjust the size of discharge gate, by the preceding mode of taking out the board, change present arc pneumatic control device into, adjust size to drying discharge gate 5 in the ejection of compact, thereby can adjust the exhaust velocity of raw materials, it is more convenient to use, and can be to 5 self-closing of drying discharge gate in the dry time, thereby can play sealed effect, high durability and convenient use, and the operation is simple.
The bottom of the discharge hopper 501 is fixedly provided with a discharge fan 503, and the discharge speed of the raw materials can be accelerated by the discharge fan 503.
It should be noted that, in the boiling dryer, when working, the vortex air pump 2 generates high-speed air flow, so that the inner cavity of the vacuum charging bucket 201 generates negative pressure, the raw material in the conveying pipeline can be discharged into the inner cavity of the boiling chamber 101 under the action of the negative pressure, wherein the connecting part of the vacuum charging bucket 201 and the boiling chamber 101 is provided with the feeding fan 202, the feeding fan 202 can apply forward thrust to the raw material, so as to effectively improve the injection speed of the raw material, the raw material is received and held by the discharging screen plate 102 after entering the inner cavity of the boiling chamber 101, air can be injected into the inner cavity of the boiling chamber 101 by the air supply fan 301, one end of the air supply fan 301 is connected with the air filter 3, the air can be filtered and purified by the air filter 3, so as to avoid the pollution of dust in the air to the raw material, the other end of the air supply fan 301 is connected with, the raw materials are blown into the boiling chamber 101 through the hot air inlet hopper 303, so that the raw materials can be heated and baked through hot steam, the raw materials are dried quickly, the air blocking balls 304 are arranged in the inner cavities of the hot air inlet hopper 303, when air enters the hot air inlet hopper 303, the air blocking balls 304 are blown up by the air, when the air inlet is stopped, the air blocking balls 304 fall under the action of gravity, so that the hot air inlet hopper 303 can be sealed, the heat loss of the inner cavity of the boiling chamber 101 is reduced, the energy loss can be effectively reduced, after the raw materials are dried, hot air in the boiling chamber 101 is guided into the settling chamber 401 through the main air pipe 4, substances with larger particles in the air can be settled through the settling chamber 401, the airflow flows into the hot airflow separation chamber 402 after the settlement, small particle substances in the airflow can be separated again through the cyclone separation chamber 402, so that the discharged air is cleaner, and the pollution to the environment is reduced, through the pneumatic rotary control valve 502 of control, adjust the size of discharge gate, by the preceding board mode of taking out, change present arc pneumatic regulating device into, to the regulation size of dry discharge gate 5 in the ejection of compact to can adjust the exhaust velocity of raw materials, it is more convenient to use, and can be to 5 self-closing of dry discharge gate in the time of dry, thereby can play sealed effect, convenient to use, easy operation.
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.
Claims (6)
1. A fluidized dryer, characterized by: the machine comprises a machine body (1), a boiling chamber (101) and a discharge mesh plate (102), wherein the inner cavity of the machine body (1) is fixedly provided with the boiling chamber (101), the discharge mesh plate (102) is fixedly arranged at the top of the inner cavity of the boiling chamber (101), one end of the machine body (1) is fixedly provided with a vortex air pump (2), the top of the vortex air pump (2) is fixedly connected with a vacuum charging bucket (201) through a pipeline, the bottom of the vacuum charging bucket (201) is fixedly connected with a feeding fan (202), the gas outlet end of the feeding fan (202) is fixedly connected with the boiling chamber (101), one side of the machine body (1) is fixedly provided with a blowing fan (301), the gas outlet end of the blowing fan (301) is fixedly connected with a steam heater (302) through a pipeline, the gas outlet end of the steam heater (302) is fixedly connected with a heat air inlet bucket (, the cyclone separator is characterized in that the cyclone separator is connected to the bottom of a boiling chamber (101), a main air pipe (4) is fixedly connected to the top of the boiling chamber (101), a settling chamber (401) is fixedly connected to one end of the main air pipe (4), a cyclone separation chamber (402) is fixedly connected to one end of the settling chamber (401), and a drying discharge hole (5) is fixedly formed in one end of the machine body (1).
2. A boiling dryer as claimed in claim 1, wherein: the air supply fan (301) is provided with two sets of, the inlet end of air supply fan (301) all is through pipeline fixedly connected with air cleaner (3).
3. A boiling dryer as claimed in claim 1, wherein: and the inner cavities of the heat air inlet hoppers (303) are respectively and movably provided with a wind resistance ball (304).
4. A boiling dryer as claimed in claim 1, wherein: the top of the cyclone separation chamber (402) is fixedly connected with an induced draft fan (403) through a pipeline.
5. A boiling dryer as claimed in claim 1, wherein: drying discharge gate (5) one side fixed mounting has out hopper (501), go out hopper (501) inner chamber fixed mounting has pneumatic rotatory governing valve (502).
6. The ebullient dryer of claim 5, wherein: and a discharging fan (503) is fixedly arranged at the bottom of the discharging hopper (501).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021225161.8U CN212620013U (en) | 2020-06-29 | 2020-06-29 | Boiling dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021225161.8U CN212620013U (en) | 2020-06-29 | 2020-06-29 | Boiling dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212620013U true CN212620013U (en) | 2021-02-26 |
Family
ID=74743240
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021225161.8U Active CN212620013U (en) | 2020-06-29 | 2020-06-29 | Boiling dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212620013U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113768116A (en) * | 2021-09-02 | 2021-12-10 | 宁夏春升源生物科技有限公司 | Method for preparing meat-flavor essence by fluidized drying method |
-
2020
- 2020-06-29 CN CN202021225161.8U patent/CN212620013U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113768116A (en) * | 2021-09-02 | 2021-12-10 | 宁夏春升源生物科技有限公司 | Method for preparing meat-flavor essence by fluidized drying method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100579879C (en) | Delivery spray nozzle, polytetrafluoroethylene fine particle processing method and apparatus using the spray nozzle | |
| CN212620013U (en) | Boiling dryer | |
| CN106345192A (en) | Small-size pulse bag dust collector | |
| CN203342598U (en) | Cyclone-cloth bag dust removal and desulfuration integrated device | |
| CN204073763U (en) | A kind of double-cyclone flue gas preprocessor | |
| CN203534103U (en) | Pneumatic drying device | |
| CN103736572B (en) | There is the circulating fluidised bed apparatus of drying, pulverizing and sterilizing function | |
| CN203132306U (en) | Automatic smashing drying machine | |
| CN106268100B (en) | A kind of improvement type gravel bed filter | |
| CN110411171A (en) | A kind of stagewise roller biomass dryer | |
| CN206240190U (en) | A kind of small-sized pulsed jet cloth filter | |
| CN207222095U (en) | Automatic intelligent charging fluidized bed jet mill grader | |
| CN219318829U (en) | Circulating fluidized bed | |
| CN207716724U (en) | A kind of Pneumatic drying device | |
| CN103697662B (en) | A kind of equipment with pneumatic conveying drying and air-flow screening function | |
| CN104550127B (en) | Novel environment friendly particle, granular material surface cleaning system | |
| CN209605480U (en) | A kind of ebullated dryer with automatic charging | |
| CN206121360U (en) | High -efficient induced jetting device of dust remover and pulse bag dust collector ware | |
| CN208282533U (en) | Powder dries subpackage apparatus | |
| CN106422567B (en) | A kind of deduster efficiently induces blowing device and pulsed jet cloth filter | |
| CN208536498U (en) | A kind of fluid bed dryer extending residence time of material | |
| CN207973233U (en) | A kind of bulk material conveying equipment | |
| CN208087445U (en) | Sludge dry system | |
| CN206081978U (en) | Improved type grained layer dust remover | |
| CN206660843U (en) | A kind of cyclone dust collectors |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |