CN109000466A - Vertical powder wet feed dryer - Google Patents
Vertical powder wet feed dryer Download PDFInfo
- Publication number
- CN109000466A CN109000466A CN201810975370.5A CN201810975370A CN109000466A CN 109000466 A CN109000466 A CN 109000466A CN 201810975370 A CN201810975370 A CN 201810975370A CN 109000466 A CN109000466 A CN 109000466A
- Authority
- CN
- China
- Prior art keywords
- feed
- holding chamber
- material holding
- drying
- drying materials
- 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.)
- Pending
Links
- 239000000843 powder Substances 0.000 title claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 111
- 238000001035 drying Methods 0.000 claims abstract description 73
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 239000002828 fuel tank Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 5
- 230000009977 dual effect Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 4
- 230000002906 microbiologic effect Effects 0.000 description 4
- 235000008708 Morus alba Nutrition 0.000 description 3
- 240000000249 Morus alba Species 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 235000019750 Crude protein Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 241000219793 Trifolium Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000019621 digestibility Nutrition 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 235000020776 essential amino acid Nutrition 0.000 description 1
- 239000003797 essential amino acid Substances 0.000 description 1
- 239000004459 forage Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000019629 palatability Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/02—Heating arrangements using combustion heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
- F26B23/06—Heating arrangements using electric heating resistance heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/02—Applications of driving mechanisms, not covered by another subclass
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses vertical powder wet feed dryers, comprising: drying materials room, drying chamber enclosure, heating device, material holding chamber, feed conveyer.Vertical powder wet feed dryer provided by the invention passes through the electric dual system energy supply of oil, drying materials room is designed to horn-like, heating device separates the circulation drying that high-moisture feed is realized by feed conveyer with feed, good drying effect, it can uninterruptedly work long hours, improve drying efficiency.
Description
Technical field
The present invention relates to feed manufacturing machine fields.More specifically to a kind of vertical powder wet feed dryer.
Background technique
Folium et Ramulus Mori microbiological fermented feed is a kind of microbiological fermented feed for carrying out processing mixed fermentation by Folium et Ramulus Mori and obtaining, feed battalion
It is high to support value, in terms of dry, 20% or more crude protein content, protein content is similar with clover, higher than graminous pasture by 80%
~100%, specific heat band leguminous forage is high by 40%~50%;Folium et Ramulus Mori biological yield is high, can cut receipts 6 within generally per acre mulberry tree 1 year
It is secondary, 750 kilograms of branches and leaves or so are produced every time, and 1 year yield of mulberry reaches 4.5 tons or so per acre;It is good to the animals such as ox, sheep palatability,
Digestibility is high;Fourth is that containing 18 kinds of amino acid in mulberry leaf, wherein the ratio of essential amino acid is up to 43%;Folium et Ramulus Mori is micro- in summary
Storage feed is a kind of feed for having very much dynamogenetic value, but ramulus mori leaf feed can also encounter some problems during processing,
Ramulus mori leaf water content is very high, and the water content of the Folium et Ramulus Mori microbiological fermented feed after processing fermentation is bigger, and traditional dryer can only
The low feed of common water content is dried, when drying high-moisture Folium et Ramulus Mori microbiological fermented feed, the time it takes is longer, and production efficiency is too
It is low.
Summary of the invention
Vertical powder wet feed dryer provided by the invention, it is intended to overcome in the prior art traditional dryer cannot quickly and
The deficiency of the big feed of a large amount of processing water content, and the advantages of at least will be described later, is provided.
In order to solve the above-mentioned technical problem, the present invention adopts the following technical scheme:
Vertical powder feed dryer, comprising:
Drying materials room, shape be it is tubaeform, upper diameter is big, and lower diameter is small, and top is equipped with steam (vapor) outlet and to enter
Material mouth, lower part osculum are discharge port;
Chamber enclosure is dried, for cylinder, is set in the outside of drying materials room, it is highly contour with drying materials room;
Heating device is located between spiral material drying room and drying chamber enclosure.
Preferably, the vertical powder wet feed dryer, further includes:
Material holding chamber, it is cylindrical, positioned at the underface of drying materials room, the discharge port of drying materials room and the top of material holding chamber
It is connected, a wet feed entrance is additionally provided at the top of the material holding chamber, material holding chamber's sidewall bottom is equipped with discharge port, described to deposit
Material chamber interior is provided with poking device, and feed inside material holding chamber is discharged from material holding chamber's discharge port;
Feed conveyer, feed inlet is corresponding with the discharge port of material holding chamber, the discharge port and object of feed conveyer
The feeding inlet of material drying room is connected.
Preferably, the steam outlet on drying materials room top is connected with a round tube, and the circular tube external wall is provided with
Multiple electrothermal tubes, electrothermal tube are uniformly distributed circumferentially.
Preferably, the feeding inlet of drying materials room is located at drying materials room side wall upper part, and the feeding inlet is connected with one
Feed pipe, feed pipe are arranged along the horizontal tangent direction of side wall.
Preferably, the poking device includes:
Material separating disc, lower surface are connected with a shaft;
The connecting rod of more arcs, the circumferential uniform intervals along shaft arrange that one end of each connecting rod and the shaft connect
It connects, the other end of each connecting rod close to material holding chamber bottom and is connected with a vertical plectrum;
Driving device, is set to below material holding chamber, and there are a through-hole, the driving device and shaft in bottom centre of material holding chamber
Connection, and drive shaft rotates.
Preferably, the feed conveyer includes:
Blower, the air inlet of blower are equipped with hopper, and hopper is located at below material holding chamber's discharge port, and hopper is for accepting material stock
The feed of room discharge port discharge;
The air outlet of conduit, one end and blower connects, and the other end is connect with drying materials room feeding inlet.
Preferably, there are two the discharge ports of material holding chamber, one is drier outlet, and one exports for circulation powder, wherein
The feed inlet of the lower section face feed conveyer of circulation powder outlet, is provided with one piece of movable baffle at drier outlet.
Preferably, heating device is a combustion furnace, passes through the external fuel tank of conduit.
Preferably, drying room outer casing underpart is equipped with an openable and closable door, the door face heating device.
The present invention is include at least the following beneficial effects: it is heated by oily electric hybrid system, so that heating speed is faster, drying
It is more efficient;Blower by using positive wine pressure is driving force, runs feed in the shape of a spiral in drying materials room again, and drying
Shuttling movement effectively extends drying time in dry machine so that drying it is more abundant, in machine operation procedure can midway filling,
Production efficiency can be effectively ensured with long time running in blowing, machine.
Further advantage, target and feature of the invention will be partially reflected by the following instructions, and part will also be by this
The research and practice of invention and be understood by the person skilled in the art.
Detailed description of the invention
Fig. 1 is Facad structure cut-away view of the invention;
Specific embodiment
Present invention will be described in further detail below with reference to the accompanying drawings, to enable those skilled in the art referring to specification text
Word can be implemented accordingly.
It should be noted that in the description of the present invention, term " transverse direction ", " longitudinal direction ", "upper", "lower", "front", "rear",
The orientation or positional relationship of the instructions such as "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is based on attached drawing institute
The orientation or positional relationship shown, is merely for convenience of description of the present invention and simplification of the description, and is not the dress of indication or suggestion meaning
It sets or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to limit of the invention
System.
As shown in Figure 1, the present invention provides a kind of vertical powder wet feed dryer, comprising:
Vertical powder feed dryer, comprising:
Drying materials room 2, shape be it is tubaeform, upper diameter is big, and lower diameter is small, top be equipped with 17 He of steam (vapor) outlet
Feeding inlet 16, lower part osculum are discharge port;
Chamber enclosure 3 is dried, for cylinder, is set in the outside of drying materials room, it is highly contour with drying materials room;
Heating device 4 is located between drying materials room 2 and drying chamber enclosure 3;
Feed from the feeding inlet 16 of drying materials room 2 enter, along skew wall break away fall drying, by by heating device 4 with
Feed separation, is conducted heat by outer wall and is dried, drying materials room is set as horn-like, extends feed in the stop of drying materials room
Time so that feed is dried more sufficiently in drying materials room 2, and can be adapted for the drying of a large amount of feeds.
In another embodiment, vertical powder wet feed dryer, further includes:
Material holding chamber 13, it is cylindrical, positioned at the underface of drying materials room 2, the discharge port of drying materials room 2 and material holding chamber 13
Top be connected, the top of the material holding chamber 13 is additionally provided with a wet feed entrance 15, and 13 sidewall bottom of material holding chamber is equipped with
Discharge port, the material holding chamber 13 are internally provided with poking device, and feed inside material holding chamber is discharged from material holding chamber's discharge port;
Feed conveyer, feed inlet is corresponding with the discharge port of material holding chamber 13, the discharge port of feed conveyer with
The feeding inlet 16 of drying materials room 2 is connected;
Feed is released by the discharge port of material holding chamber 13, and into feed conveyer, feed conveyer leads feed again
Enter drying materials room 2, allows feed to realize circulation drying in dryer, drying effect has been effectively ensured.
In another embodiment, a round tube is connected at the steam (vapor) outlet 17 on drying materials room top, outside the round tube
Wall is provided with multiple electrothermal tubes 1, and electrothermal tube 1 is uniformly distributed along axial direction;
By the double heating systems of oily electricity, so that the temperature of drying materials room 2 rises quickly, evaporation rate is bigger, effectively mentions
High drying efficiency can select single energy supply side when drying the few feed of moisture compared to traditional single powered mode
Method energizes drying simultaneously for two kinds in the big feed of drying water content, rationally effectively utilizes resource, energy conservation and environmental protection.
In another embodiment, the feeding inlet 16 of drying materials room 2 is located at drying materials room side wall upper part, the feeding inlet
16 are connected with a feed pipe, and feed pipe is arranged along the horizontal tangent direction of side wall;
Feed pipe is placed along the horizontal tangent direction of side wall, when feed enters dry materials room by feed conveying device
When, make feed that there is certain kinetic energy, feed can be moved along the loudspeaker inner wall of drying materials room 2 with the track that spiral declines,
Along feed has been grown in 3 residence time of drying materials room, so that evaporation effect is more preferable, it is also beneficial to the evaporation of vapor.
In another embodiment, the poking device in material holding chamber 13 includes:
Material separating disc 14, lower surface are connected with a shaft;
The connecting rod 12 of more arcs, along shaft 19 circumferential uniform intervals arrange, one end of each connecting rod 12 with it is described
Shaft 19 connects, and the other end of each connecting rod 12 close to 13 bottom of material holding chamber and is connected with a vertical plectrum 20;
Driving device, is set to below material holding chamber, and there are a through-hole, the driving device and shaft in bottom centre of material holding chamber
19 connections, and drive shaft 19 rotates, wherein driving device can be a stepless time adjustment motor, drive shaft and shaft 19
It is directly connected to, drive shaft rotation;
Alternatively, driving device may include: ordinary motor, the first flywheel, the second flywheel, first gear and second gear,
Shaft 19 pass through bottom centre of material holding chamber through-hole, shaft 19 and first gear it is concentric connect and it is affixed, first gear is located at
The bottom of shaft 19 is equipped with fixed bracket in the lower part of material holding chamber, and ordinary motor is fixedly connected with bracket, in the drive shaft of motor
Be connected with the first flywheel, the second flywheel and second gear are located at below material holding chamber, the second flywheel and the concentric connection of second gear and
Affixed, the first flywheel is connect with the second flywheel by belt, and first gear is connected with second gear;Motor rotation drives the
One flywheel turns, the first flywheel drive the second flywheel and affixed below second gear to rotate by belt, second gear with
The operating of poking device is realized in the rotation of first gear bite strap turn axis.
One poking device is set in material holding chamber 13, and wherein material separating disc 14 can lead to the wet feed for initially entering material holding chamber
It crosses centrifugal force to scatter, increases distribution area, so that moisture evaporation is more evenly;The feeding that one setting gauge can will dry is set
Material is automatically drained out material holding chamber 13 by plectrum, not will cause the feed accumulation problem in material holding chamber 13, on the other hand can make machine
The continual carry out drying operation of device, and machine does not have to shut down discharging;Motor 8 can be stepless time adjustment motor, in different works
Friction speed is adjusted under the conditions of work, revolving speed is slowed down when unloading dry feed, and uniform discharging revs up in drying, flash baking
It improves efficiency.
In another embodiment, the feed conveyer includes:
Blower 9, the air inlet of blower 9 are equipped with hopper, and hopper is located at below 13 discharge port of material holding chamber, and hopper is for accepting
The feed that material holding chamber's discharge port 10 is discharged;
Conduit 18, one end are connect with the air outlet of blower 9, and the other end is connect with drying materials room feeding inlet 16.
Feed is transported by using blower, it, can be with when entering material drying machine so that feed has a bigger kinetic energy
Guaranteeing that material is bound to helical orbital movement, kinetic energy is bigger, and relative retention time is longer, it ensure that certain drying effect,
And the wind of blower by near the steam (vapor) outlet at top when can have certain heat, so that feed is continued not in drying materials room
Intermittent holding evaporating state, preferably guarantees drying effect.
In another embodiment, there are two the discharge ports of material holding chamber 13, one is drier outlet 7, and one is circulation powder
Outlet 10, wherein circulation powder exports the feed inlet of 10 lower section face feed conveyer, is provided with one piece at drier outlet 7
Movable baffle;
Two outlets are arranged in material holding chamber 13, can make machine that can uninterruptedly recycle baking material, another side when operating
Also it can continue to discharge, 7 discharging of drier outlet can be opened after the feed drying degree in machine reaches standard, while machine is not
It shuts down, after most siccative is unsnatched, passes through wet feed by flapper closure drier outlet 7, while in the material holding chamber of machine 13
Entrance 15 is fed, it is ensured that the continuous running of machine.
In another embodiment, heating device 4 is a combustion furnace, passes through the external fuel tank 6 of conduit;
In another embodiment, drying 3 lower part of chamber enclosure is equipped with an openable and closable door 5, the door face heating device
4。
External fuel tank 6, which is arranged, ensure that machine while guaranteeing dryer operating with the type of refuelling
Safety is arranged an openable and closable door 5 in drying 3 lower part of chamber enclosure, the case where for checking combustion furnace, to avoid meaning
Outside.
Although the embodiments of the present invention have been disclosed as above, but its is not only in the description and the implementation listed
With it can be fully applied to various fields suitable for the present invention, for those skilled in the art, can be easily
Realize other modification, therefore without departing from the general concept defined in the claims and the equivalent scope, the present invention is simultaneously unlimited
In specific details and legend shown and described herein.
Claims (9)
1. vertical powder wet feed dryer characterized by comprising
Drying materials room, shape be it is tubaeform, upper diameter is big, and lower diameter is small, top be equipped with steam (vapor) outlet and feeding inlet,
Lower part osculum is discharge port;
Chamber enclosure is dried, for cylinder, is set in the outside of drying materials room, it is highly contour with drying materials room;
Heating device is located between drying materials room and drying chamber enclosure.
2. vertical powder wet feed dryer according to claim 1, which is characterized in that further include:
Material holding chamber, cylindrical, positioned at the underface of drying materials room, the discharge port of drying materials room is connected with the top of material holding chamber
It is logical, a wet feed entrance is additionally provided at the top of the material holding chamber, material holding chamber's sidewall bottom is equipped with discharge port, the material holding chamber
It is internally provided with poking device, feed inside material holding chamber is discharged from material holding chamber's discharge port;
Feed conveyer, feed inlet is corresponding with the discharge port of material holding chamber, and the discharge port and material of feed conveyer dry
The feeding inlet of dry chamber is connected.
3. vertical powder wet feed dryer according to claim 1, which is characterized in that the steam on drying materials room top goes out
It is connected with a round tube at mouthful, the circular tube external wall is provided with multiple electrothermal tubes, and electrothermal tube is uniformly distributed circumferentially.
4. vertical powder wet feed dryer according to claim 1, which is characterized in that the feeding inlet of drying materials room is located at
Drying materials room side wall upper part, the feeding inlet are connected with a feed pipe, and feed pipe is arranged along the horizontal tangent direction of side wall.
5. vertical powder wet feed dryer according to claim 2, which is characterized in that the poking device includes:
Material separating disc, lower surface are connected with a shaft;
The connecting rod of more arcs, the circumferential uniform intervals along shaft arrange that one end of each connecting rod is connect with the shaft, often
The other end of one connecting rod is close to material holding chamber bottom and is connected with a vertical plectrum;
Driving device is set to below material holding chamber, and there is a through-hole in bottom centre of material holding chamber, and the driving device and shaft connect
It connects, and drive shaft rotates.
6. vertical powder wet feed dryer according to claim 2, which is characterized in that the feed conveyer includes:
Blower, the air inlet of blower are equipped with hopper, and hopper is located at below material holding chamber's discharge port, and hopper goes out for accepting material holding chamber
The feed of material mouth discharge;
The air outlet of conduit, one end and blower connects, and the other end is connect with drying materials room feeding inlet.
7. vertical powder wet feed dryer according to claim 2, which is characterized in that there are two the discharge ports of material holding chamber,
One be drier outlet, one for circulation powder export, wherein circulation powder outlet lower section face feed conveyer into
Material mouth is provided with one piece of movable baffle at drier outlet.
8. vertical powder wet feed dryer according to claim 1, which is characterized in that heating device is a combustion furnace,
It passes through the external fuel tank of conduit.
9. vertical powder wet feed dryer according to claim 1, which is characterized in that drying room outer casing underpart is equipped with one
Openable and closable door, the door face heating device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810975370.5A CN109000466A (en) | 2018-08-24 | 2018-08-24 | Vertical powder wet feed dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810975370.5A CN109000466A (en) | 2018-08-24 | 2018-08-24 | Vertical powder wet feed dryer |
Publications (1)
Publication Number | Publication Date |
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CN109000466A true CN109000466A (en) | 2018-12-14 |
Family
ID=64594434
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201810975370.5A Pending CN109000466A (en) | 2018-08-24 | 2018-08-24 | Vertical powder wet feed dryer |
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CN (1) | CN109000466A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113251765A (en) * | 2021-04-21 | 2021-08-13 | 安徽晶华电子基材有限公司 | Drying equipment is used in silica micropowder production |
Citations (5)
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EP1440625A2 (en) * | 2003-01-27 | 2004-07-28 | Dinnissen B.V. | Batch-cycle type heat-treatment apparatus for treating of material like mash fodder as well as a method using such an apparatus for treatment of material |
CN205980682U (en) * | 2016-07-19 | 2017-02-22 | 王加福 | Fodder circulation drying device |
CN206478995U (en) * | 2016-11-16 | 2017-09-08 | 天津市浩生农牧科技有限公司 | A kind of feed granules circulate drying plant |
CN107356072A (en) * | 2017-06-30 | 2017-11-17 | 徐州市贾汪区泰瑞农业科技有限公司 | A kind of Feed Manufacturing dryer |
CN107617353A (en) * | 2017-10-25 | 2018-01-23 | 杨红娜 | A kind of stirring and drying integrated device |
-
2018
- 2018-08-24 CN CN201810975370.5A patent/CN109000466A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1440625A2 (en) * | 2003-01-27 | 2004-07-28 | Dinnissen B.V. | Batch-cycle type heat-treatment apparatus for treating of material like mash fodder as well as a method using such an apparatus for treatment of material |
CN205980682U (en) * | 2016-07-19 | 2017-02-22 | 王加福 | Fodder circulation drying device |
CN206478995U (en) * | 2016-11-16 | 2017-09-08 | 天津市浩生农牧科技有限公司 | A kind of feed granules circulate drying plant |
CN107356072A (en) * | 2017-06-30 | 2017-11-17 | 徐州市贾汪区泰瑞农业科技有限公司 | A kind of Feed Manufacturing dryer |
CN107617353A (en) * | 2017-10-25 | 2018-01-23 | 杨红娜 | A kind of stirring and drying integrated device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113251765A (en) * | 2021-04-21 | 2021-08-13 | 安徽晶华电子基材有限公司 | Drying equipment is used in silica micropowder production |
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