CN108704581A - A kind of pharmaceutical purpose fluidised bed granulator - Google Patents
A kind of pharmaceutical purpose fluidised bed granulator Download PDFInfo
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- CN108704581A CN108704581A CN201810603897.5A CN201810603897A CN108704581A CN 108704581 A CN108704581 A CN 108704581A CN 201810603897 A CN201810603897 A CN 201810603897A CN 108704581 A CN108704581 A CN 108704581A
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- case
- granulation
- medicinal powder
- air
- granulation case
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Organic Chemistry (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
Abstract
The invention discloses a kind of pharmaceutical purpose fluidised bed granulators,Including granulation case and support plate,The granulation case side, which is equipped with, removes wet tank,It is described to be equipped with activated carbon adsorption net except wet tank is interior,It is described to be equipped with air-introduced machine far from granulation case side except wet tank,Bottom end is equipped with netted electric heating sheets in the granulation case,Sparge pipe is equipped in the granulation case,The outer both sides of the granulation case are respectively equipped with air compressor and binder case,The compression gas pipe passes through granulation case to be connect with air compressor output end,The diversion pipe passes through granulation case to be connect with the binder delivery pump on binder case,It is equipped with medicinal powder drying box below the air compressor and binder case,It is equipped with medicinal powder pipe between medicinal powder drying box bottom end and granulation case,The present invention,Equipped with dehumidification device,The air-flow used for granulation can carry out dehumidifying evolution,Improve granulating efficiency,And the powder used for granulation can first carry out drying and processing,Ensure powder drying,It is easy to pelletize.
Description
Technical field
The present invention relates to pharmacy granulator equipment technical field, specifically a kind of pharmaceutical purpose fluidised bed granulator.
Background technology
Fluidized bed granulation method is the fluidized state for keeping suspending under the airflow function for making drug powder from bottom to top, bonding
Agent liquid sprays into the method for making powder be agglomerated into particle into fluidising chamber from top or lower part.Boiling can be completed in an equipment
Mixing, spraying granulation, pneumatic conveying drying process (can also be coated), also known as one-step palletizing, most of existing fluidised bed granulator
Be not provided with dehumidification device, if with moist air enter the drying and granulating in granulator to material will produce it is prodigious
Influence, and the drug powder used of granulation in storage inside may make moist, if directly using material can be caused when granulation
A softening caking, the case where occurring collapsing bed.
Invention content
The purpose of the present invention is to provide a kind of pharmaceutical purpose fluidised bed granulators, do not have to solve granulator in the prior art
Dehumidification device is set, and drug powder makes moist and do not dry use and easily lead to the problems such as collapsing bed.
To achieve the above object, the present invention provides the following technical solutions:A kind of pharmaceutical purpose fluidised bed granulator, including granulation
Case and support plate, the granulation case are fixedly mounted on support plate upper end, and the granulation case side, which is equipped with, removes wet tank, described to remove wet tank
The second connecting tube is equipped between granulation case, it is described except wet tank is interior equipped with activated carbon adsorption net, it is described except wet tank is far from granulation case
Side between wet tank by the first connecting tube equipped with air-introduced machine, the air-introduced machine and except being connected, and bottom end is equipped in the granulation case
Netted electric heating sheets, the netted electric heating sheets top are equipped with dispersion plate, the granulation
Sparge pipe is equipped in case, the sparge pipe is located at the top of dispersion plate, and the sparge pipe bottom surface is equidistantly divided
It is laid with nozzle, the outer both sides of the granulation case are respectively equipped with air compressor and binder case, are equipped with outside the binder case
Binder delivery pump, the sparge pipe upper end are connected separately with compression gas pipe and diversion pipe, and the compression gas pipe passes through granulation case
It is connect with air compressor output end, the diversion pipe passes through granulation case to be connect with the binder delivery pump on binder case, institute
It states and is equipped with medicinal powder drying box below air compressor and binder case, agitating shaft is equipped in the medicinal powder drying box, it is described
Medicinal powder drying box side is equipped with stirring motor, and the stirring motor output end is equipped with and stirs with stirring axis connection, the agitating shaft
Blade is mixed, top both sides are equipped with air bells cap in the medicinal powder drying box, and air-heater, the heat are equipped with outside the medicinal powder drying box
Wind turbine is connect with hot wind cover stent by hot blast pipe, and medicinal powder pipe is equipped between medicinal powder drying box bottom end and granulation case, described
Support plate bottom end is equipped with pedestal.
Preferably, described except wet tank and air-introduced machine are fixedly mounted on support plate surface, the activated carbon except in wet tank
There are three adsorption net is set altogether.
Preferably, the outer left side lower end of the granulation case is equipped with ptc heater, the ptc heater and netted electrical heating
It is electrically connected between piece.
Preferably, liquid suction pipe is equipped between described adhesive delivery pump and binder case, the diversion pipe and binder are defeated
Send the outlet tube connection on pump.
Preferably, the medicinal powder drying box is fixedly mounted on granulation case both sides, and the agitating shaft both ends pass through rolling bearing
It is connect with medicinal powder drying chamber interior wall, the medicinal powder pipe is equipped with switch valve.
Preferably, the granulation case top is equipped with air outlet, and medicinal powder drying box upper end is equipped with feed inlet.
Compared with prior art, the beneficial effects of the invention are as follows:What is be arranged between granulation case and air-introduced machine removes wet tank energy
Enough moistures by air remove, and improve the effect of granulation, and except three pieces activated carbon adsorption net is equipped in wet tank altogether, effect on moisture extraction is good
And the impurity peculiar smell adsorption in air can be purified, clean level is high, in the netted electric heating sheets energy of granulation bottom end setting
It is enough to generate heat under the action of ptc heater, the air of entrance is heated, convenient for granulation drying, while strengthening dehumidifying effect
Fruit, the dispersion plate being arranged above netted electric heating sheets is used to support medicinal powder, while can uniformly divide the gas of importing
Cloth improves medicinal powder boiling fluidisation, is dried in the medicinal powder that the medicinal powder drying box of granulation case both sides setting can use granulation,
Medicinal powder internal wetted is avoided, the case where direct use causes to collapse bed, the agitating shaft being arranged in medicinal powder drying box can stir
It drives stirring blade rotation to be stirred medicinal powder under the action of motor to break up, improves heating speed and heating effect.
Description of the drawings
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is medicinal powder drying box internal structure schematic diagram of the present invention.
Fig. 3 is binder delivery pump of the present invention and binder case connection diagram.
In figure:1, air compressor;2, compression gas pipe;3, sparge pipe;4, air outlet;5, diversion pipe;6, nozzle;7, it pelletizes
Case;8, binder case;9, medicinal powder drying box;10, medicinal powder pipe;11, dispersion plate;12, netted electric heating sheets;13, PTC is heated
Device;14, support plate;15, pedestal;16, the second connecting tube;17, activated carbon adsorption net;18, wet tank is removed;19, the first connecting tube;
20, air-introduced machine;21, stirring blade;22, agitating shaft;23, stirring motor;24, air bells cap;25, feed inlet;26, hot blast pipe;27,
Air-heater;28, rolling bearing;29, binder delivery pump;30, liquid suction pipe;31, outlet tube.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Please refer to Fig.1-3, in the embodiment of the present invention, a kind of pharmaceutical purpose fluidised bed granulator, including granulation case 7 and support plate
14, granulation case 7 is fixedly mounted on 14 upper end of support plate, and 7 side of granulation case, which is equipped with, removes wet tank 18, except wet tank 18 can will be in air
Moisture removal, the effect of granulation is improved, except the second connecting tube 16 is equipped between wet tank 18 and granulation case 7, except being set in wet tank 18
Active charcoal adsorption net 17,17 effect on moisture extraction of activated carbon adsorption net is good and can be purified to the impurity peculiar smell adsorption in air, clean
Only degree is high, connects far from 7 side of granulation case equipped with air-introduced machine 20, air-introduced machine 20 and except passing through first between wet tank 18 except wet tank 18
19 connection of take over, pelletize case 7 in bottom end be equipped with netted electric heating sheets 12, netted electric heating sheets 12 can be in ptc heater 13
The lower fever of effect, heats the air of entrance, convenient for granulation drying, while strengthening effect on moisture extraction, netted electric heating sheets
12 tops are equipped with dispersion plate 11, and dispersion plate 11 is used to support medicinal powder, while can be uniformly distributed the gas of importing,
Medicinal powder boiling fluidisation is improved, is equipped with sparge pipe 3 in granulation case 7, sparge pipe 3 is located at the top of dispersion plate 11,3 bottom of sparge pipe
Face equidistantly distributed is equipped with nozzle 6, and granulation case 7 outer both sides are respectively equipped with air compressor 1 and binder case 8, outside binder case 8
Binder delivery pump 29 is installed, 3 upper end of sparge pipe is connected separately with compression gas pipe 2 and diversion pipe 5, and compression gas pipe 2 passes through system
Grain case 7 is connect with 1 output end of air compressor, and diversion pipe 5 passes through granulation case 7 and the binder delivery pump 29 on binder case 8
The lower section of connection, air compressor 1 and binder case 8 is equipped with medicinal powder drying box 9, and medicinal powder drying box 9 can use granulation
Medicinal powder dried, avoid medicinal powder internal wetted, the case where direct use causes to collapse bed is equipped in medicinal powder drying box 9 and stirs
Axis 22,9 side of medicinal powder drying box are equipped with stirring motor 23, and 23 output end of stirring motor is connect with agitating shaft 22, on agitating shaft 22
Equipped with stirring blade 21, agitating shaft 22 can drive the rotation of stirring blade 21 to stir medicinal powder under the action of stirring motor 23
It mixes and breaks up, improve heating speed and heating effect, top both sides are equipped with air bells cap 24, medicinal powder drying box 9 in medicinal powder drying box 9
Air-heater 27 is installed outside, air-heater 27 is connect with 24 holder of air bells cap by hot blast pipe 26,9 bottom end of medicinal powder drying box and granulation
Medicinal powder pipe 10 is equipped between case 7,14 bottom end of support plate is equipped with pedestal 15, except wet tank 18 and air-introduced machine 20 are fixedly mounted on support
14 surface of plate, set altogether except the activated carbon adsorption net 17 in wet tank 18 there are three, the outer left side lower end of granulation case 7 is equipped with PTC heating
Device 13 is electrically connected between ptc heater 13 and netted electric heating sheets 12, is set between adhesive delivery pump 29 and binder case 8
There are liquid suction pipe 30, diversion pipe 5 to be connect with the outlet tube on binder delivery pump 29, medicinal powder drying box 9 is fixedly mounted on granulation case 7
Both sides, 22 both ends of agitating shaft are connect by rolling bearing 28 with 9 inner wall of medicinal powder drying box, and medicinal powder pipe 10 is equipped with switch valve, system
7 top of grain case is equipped with air outlet 4, and 9 upper end of medicinal powder drying box is equipped with feed inlet 25.
The present invention operation principle be:External power supply is connected, the medicinal powder that granulation is used is waited for into medicinal powder from the addition of feed inlet 25
In drying box 9, start air-heater 27, air-heater 27, to blasting hot wind in medicinal powder drying box 9, starts stirring electricity by air bells cap 24
Machine 23, stirring motor 23 drive agitating shaft 22 rotate, agitating shaft 22 drive stirring blade 21 to the medicinal powder in medicinal powder drying box 9 into
Row stirring is broken up, and drying effect is improved, and the medicinal powder after drying enters the dispersion plate 11 in granulation case 7 by medicinal powder pipe 10
Surface, opens air-introduced machine 20, and air-introduced machine 20 is introduced air into except in wet tank 18, air will be empty after activated carbon adsorption net 17
Moisture in gas and the purification removal of peculiar smell impurity, the air of clean dried are entered along the second connecting tube 16 in granulation case 7,
Start ptc heater 13, so that netted electric heating sheets 12 generate heat, air becomes ptc heater 13 after passing through netted electric heating sheets 12
Using dispersion plate 11 medicinal powder is carried out agitating boiling at hot gas, medicinal powder is made to be boiled into fluidisation state, starts air compressor 1
With binder delivery pump 29, binder and compressed air enter 3 bottom end of sparge pipe by diversion pipe 5 and compression gas pipe 2 respectively
Nozzle 6 binder liquid mist chemical conversion fine drop is sprayed, the drop of ejection mixes with medicinal powder, is bonded to particle to complete to make
Grain.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie
In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power
Profit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent requirements of the claims
Variation is included within the present invention.Any reference signs in the claims should not be construed as limiting the involved claims.
Claims (6)
1. a kind of pharmaceutical purpose fluidised bed granulator, including granulation case (7) and support plate (14), it is characterised in that:The granulation case
(7) be fixedly mounted on support plate (14) upper end, granulation case (7) side, which is equipped with, removes wet tank (18), it is described except wet tank (18) with
The second connecting tube (16) is equipped between granulation case (7), it is described to be equipped with activated carbon adsorption net (17), the dehumidifying except wet tank (18) is interior
Case (18) far from granulation case (7) side be equipped with air-introduced machine (20), the air-introduced machine (20) with remove wet tank (18) between pass through first
Connecting tube (19) connects, and the interior bottom end of the granulation case (7) is equipped with netted electric heating sheets (12), on the netted electric heating sheets (12)
Side is equipped with dispersion plate (11), is equipped with sparge pipe (3) in the granulation case (7), the sparge pipe (3) is located at dispersion plate
(11) top, sparge pipe (3) bottom surface equidistantly distributed are equipped with nozzle (6), and the outer both sides of the granulation case (7) are respectively equipped with
Air compressor (1) and binder case (8), the binder case (8) are equipped with binder delivery pump (29), the sparge pipe outside
(3) upper end is connected separately with compression gas pipe (2) and diversion pipe (5), and the compression gas pipe (2) passes through granulation case (7) and air pressure
Contracting machine (1) output end connects, and the diversion pipe (5) passes through granulation case (7) and the binder delivery pump (29) on binder case (8)
It connects, medicinal powder drying box (9), the medicinal powder drying box is equipped with below the air compressor (1) and binder case (8)
(9) agitating shaft (22) is equipped in, medicinal powder drying box (9) side is equipped with stirring motor (23), and the stirring motor (23) is defeated
Outlet is connect with agitating shaft (22), and the agitating shaft (22) is equipped with stirring blade (21), the interior top of the medicinal powder drying box (9)
Both sides are equipped with air bells cap (24), and air-heater (27), the air-heater (27) and air bells cap are equipped with outside the medicinal powder drying box (9)
(24) holder is connected by hot blast pipe (26), and medicinal powder pipe is equipped between medicinal powder drying box (9) bottom end and granulation case (7)
(10), support plate (14) bottom end is equipped with pedestal (15).
2. a kind of pharmaceutical purpose fluidised bed granulator according to claim 1, it is characterised in that:It is described to remove wet tank (18) and air inducing
Machine (20) is fixedly mounted on support plate (14) surface, and the activated carbon adsorption net (17) except in wet tank (18) is equipped with three altogether
It is a.
3. a kind of pharmaceutical purpose fluidised bed granulator according to claim 1, it is characterised in that:The granulation case (7) outside left side
Lower end is equipped with ptc heater (13), is electrically connected between the ptc heater (13) and netted electric heating sheets (12).
4. a kind of pharmaceutical purpose fluidised bed granulator according to claim 1, it is characterised in that:Described adhesive delivery pump (29)
Liquid suction pipe (30), the diversion pipe (5) and the outlet tube (31) on binder delivery pump (29) are equipped between binder case (8)
Connection.
5. a kind of pharmaceutical purpose fluidised bed granulator according to claim 1, it is characterised in that:The medicinal powder drying box (9) is solid
Dingan County is connected mounted in granulation case (7) both sides, agitating shaft (22) both ends by rolling bearing (28) and medicinal powder drying box (9) inner wall
It connects, the medicinal powder pipe (10) is equipped with switch valve.
6. a kind of pharmaceutical purpose fluidised bed granulator according to claim 1, it is characterised in that:Granulation case (7) top is set
There are air outlet (4), medicinal powder drying box (9) upper end to be equipped with feed inlet (25).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810603897.5A CN108704581A (en) | 2018-06-12 | 2018-06-12 | A kind of pharmaceutical purpose fluidised bed granulator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810603897.5A CN108704581A (en) | 2018-06-12 | 2018-06-12 | A kind of pharmaceutical purpose fluidised bed granulator |
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CN108704581A true CN108704581A (en) | 2018-10-26 |
Family
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Family Applications (1)
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CN201810603897.5A Withdrawn CN108704581A (en) | 2018-06-12 | 2018-06-12 | A kind of pharmaceutical purpose fluidised bed granulator |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111895739A (en) * | 2020-08-02 | 2020-11-06 | 海南博成制药有限公司 | Rotary type drying machine for medicine production |
CN114322534A (en) * | 2021-12-22 | 2022-04-12 | 金华万里扬机械制造有限公司 | Purification cylinder and drying machine fixing structure |
CN114522616A (en) * | 2022-02-28 | 2022-05-24 | 江西高胜动物保健品有限公司 | Novel tilmicosin powder coating system and process |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2431948Y (en) * | 2000-06-16 | 2001-05-30 | 谢麟 | Continuous comminutor |
CN2454022Y (en) * | 2000-11-09 | 2001-10-17 | 武进市科创喷雾干燥设备厂 | Spray-drying granulating machine |
US20060124054A1 (en) * | 2003-05-16 | 2006-06-15 | Glatt Process Technology Gmbh | Fluidized bed reactor |
CN201324620Y (en) * | 2008-12-12 | 2009-10-14 | 正大青春宝药业有限公司 | One-step palletizing device |
CN101844053A (en) * | 2010-05-10 | 2010-09-29 | 重庆佳玛机械制造有限公司 | Spiral-flow type fluidized bed coater |
CN204193879U (en) * | 2014-11-06 | 2015-03-11 | 山东诺邦特生物工程有限公司 | Granulation sprayer unit in a kind of vitamine D3 microcapsule powder production |
CN206587709U (en) * | 2017-01-03 | 2017-10-27 | 江中药业股份有限公司 | A kind of novel gas hot type fluid bed granulator system |
CN206980668U (en) * | 2017-07-27 | 2018-02-09 | 江西博雅欣和制药有限公司 | A kind of preparation fluid bed granulator |
-
2018
- 2018-06-12 CN CN201810603897.5A patent/CN108704581A/en not_active Withdrawn
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2431948Y (en) * | 2000-06-16 | 2001-05-30 | 谢麟 | Continuous comminutor |
CN2454022Y (en) * | 2000-11-09 | 2001-10-17 | 武进市科创喷雾干燥设备厂 | Spray-drying granulating machine |
US20060124054A1 (en) * | 2003-05-16 | 2006-06-15 | Glatt Process Technology Gmbh | Fluidized bed reactor |
CN201324620Y (en) * | 2008-12-12 | 2009-10-14 | 正大青春宝药业有限公司 | One-step palletizing device |
CN101844053A (en) * | 2010-05-10 | 2010-09-29 | 重庆佳玛机械制造有限公司 | Spiral-flow type fluidized bed coater |
CN204193879U (en) * | 2014-11-06 | 2015-03-11 | 山东诺邦特生物工程有限公司 | Granulation sprayer unit in a kind of vitamine D3 microcapsule powder production |
CN206587709U (en) * | 2017-01-03 | 2017-10-27 | 江中药业股份有限公司 | A kind of novel gas hot type fluid bed granulator system |
CN206980668U (en) * | 2017-07-27 | 2018-02-09 | 江西博雅欣和制药有限公司 | A kind of preparation fluid bed granulator |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111895739A (en) * | 2020-08-02 | 2020-11-06 | 海南博成制药有限公司 | Rotary type drying machine for medicine production |
CN114322534A (en) * | 2021-12-22 | 2022-04-12 | 金华万里扬机械制造有限公司 | Purification cylinder and drying machine fixing structure |
CN114522616A (en) * | 2022-02-28 | 2022-05-24 | 江西高胜动物保健品有限公司 | Novel tilmicosin powder coating system and process |
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Application publication date: 20181026 |