CN205279610U - Dustless production system of high viscosity material pelletization - Google Patents
Dustless production system of high viscosity material pelletization Download PDFInfo
- Publication number
- CN205279610U CN205279610U CN201521097441.4U CN201521097441U CN205279610U CN 205279610 U CN205279610 U CN 205279610U CN 201521097441 U CN201521097441 U CN 201521097441U CN 205279610 U CN205279610 U CN 205279610U
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- Prior art keywords
- viscosity material
- production system
- boiling drier
- dustless production
- granulation
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Abstract
The utility model discloses a dustless production system of high viscosity material pelletization. Including wet granulator, with wet granulator connects sway the granulation machine and with the fluidizing drying machine that the granulation machine is connected sways, it is equipped with a drying device in advance to sway between granulation machine and the fluidizing drying machine. This dustless production system of high viscosity material pelletization constitute and structure is simple, reasonable, can adapt to better and satisfy the technological requirement that the high viscosity material was pelletized, can effectively avoid granulation process's the blocking of hardening to and a dry run phenomenon of collapsing, help further optimization technological parameter.
Description
Technical field
Of the present utility model relate to a kind of pharmaceutical device. Particularly relate to a kind of high-viscosity material dustless production system of granulation.
Background technology
The main supplementary material of high viscosity Chinese medical concrete material pelletization such as Dalitong Granule etc. is extractum dextrin=1 1.2. Extractum ratio weighs about 1.285, extractum Property comparison thickness (solid content about 65%), complicated component, containing a large amount of water solublity and hydrophilic composition, absorbs and very capable in conjunction with moisture, at Mechanical entanglement, stereoeffect, electrostatic attraction, free fluid, the lower extract powder of the effect such as solid bridge is easily assembled, and bonding causes poor fluidity, pelletization easily hardens in bulk, and dry run is very easily collapsed bed.
10 orders that its granule is made at the appointed time want >=90% to the granule rate between 80 orders, and moisture content is less than 4.0%, and uniform color is consistent. The process units being currently used for this type of material pelletization is difficult to meet or reach above-mentioned manufacturing technique requirent mostly. Thus the quality of production improving product further is formed certain restriction.
Utility model content
The purpose of this utility model is the deficiency existed for prior art, it is provided that a kind of high-viscosity material dustless production system of granulation. This high-viscosity material granulation dustless production system composition is simple and reasonable for structure, can better adapt to and meet the technological requirement that high-viscosity material is granulated, can be prevented effectively from the in bulk that hardens of pelletization, and dry run is collapsed a phenomenon, contributes to further Optimizing Process Parameters.
The technical scheme of the high-viscosity material of the present utility model dustless production system of granulation includes the oscillating granulator that wet granulator is connected and the boiling drier being connected with described oscillating granulator with described wet granulator, it is characterized in that being provided with between described oscillating granulator and boiling drier a pre-drying device.
Described pre-drying device includes it and exports the predrying blower fan between hot blast process system and the discharging opening of oscillating granulator being connected to described boiling drier.
An air inducing Setting Tank it is provided with between described predrying blower fan and oscillating granulator.
Its feed pipe of described boiling drier is that an angle less than 90 degree extends in bucket with charging basket tangent line corresponding with this boiling drier.
Wall of this corresponding one side of its aperture, corresponding one end end face of the mesh of the corresponding web plate of described boiling drier and web plate is an angle less than 180 degree.
The mesh of described web plate is stamped and formed out by web plate wooden partition, and its lobe being stamped and formed out is fish scale-shaped on the wall of this corresponding one side of web plate.
The hot blast of described boiling drier processes system and is provided with corresponding dehydrating unit, described dehydrating unit includes the cold dehumidifier of table of the inlet side being located in the roughing efficiency air filter of the hot blast process system of boiling drier, and is located at the water fender of the air side of the cold dehumidifier of described table.
The hot blast of described boiling drier processes the cold heat wind air intake control valve of system and is provided with corresponding valve positioner.
The outfan of described boiling drier is connected to corresponding lifting vacuum pelletizing machine.
Being provided with multiple field cloth bag between described lifting vacuum pelletizing machine with corresponding turnover barrel, the internal layer of corresponding one end of described multiple field cloth bag stretches in turnover barrel, its outer layer is connected to the bundle cloth bag mouth having enough to meet the need barrel.
High-viscosity material of the present utility model granulates dustless production system due to the scientific structure, rationally of its system composition and each corresponding device, high-viscosity material granulation can be better adapted to produce, fundamentally improve product quality and production efficiency, and can effectively reduce energy resource consumption and production cost.
Accompanying drawing explanation
Fig. 1 is this utility model high-viscosity material dustless production system one example structure schematic diagram of granulation; Fig. 2 is pre-drying device structural representation of the present utility model; The hot blast that Fig. 3 is the boiling drier of utility model processes system structure schematic diagram; Fig. 4 is the attachment structure schematic diagram of vacuum pelletizing machine of the present utility model and corresponding turnover barrel; The charging basket feed pipe that Fig. 5 is boiling drier of the present utility model arranges structural representation; Fig. 6 is Fig. 5 top view; Fig. 7 is the mesh-plate structure schematic diagram of boiling drier of the present utility model; Fig. 8 is the mesh-structured schematic diagram of the web plate in Fig. 7.
Detailed description of the invention
Now pass through embodiment and the utility model is described in further detail in conjunction with accompanying drawing.
As shown in figures 1-8. The high-viscosity material of the present embodiment dustless production system of granulating includes the boiling drier 2 that the oscillating granulator 4 that wet granulator 1 is connected is connected with oscillating granulator 4 and the lifting vacuum pelletizing machine 3 etc. being connected with boiling drier 2 with wet granulator 1. Promoting vacuum pelletizing machine 3 and be provided with corresponding vacuum feeder 20, its wet granulator 1 is also associated with pressure and adds slurry tank 21.
A pre-drying device it is provided with between oscillating granulator 4 and boiling drier 2. Its pre-drying device includes a predrying blower fan 5 etc. Corresponding air inducing Setting Tank 6 it is provided with between described predrying blower fan and oscillating granulator; pre-drying device also includes the threeway 4a that one port is connected to the discharging opening of oscillating granulator 4; the two other port of threeway 4a is connected respectively in the material input (charging aperture) of the outlet of air inducing Setting Tank 6 and the corresponding charging basket 23 of boiling drier 2, and the hot blast that the entrance and exit of predrying blower fan 5 is connected respectively in boiling drier processes the hot blast cabinet 7 of system 8 and the entrance of air inducing Setting Tank 6. The particulate material that wet granulator 1 prepares is transported to before boiling drier through oscillating granulator to be undertaken predrying by its corresponding pre-drying device, can effectively solve to cause because material viscosity is high occurring in course of conveying the problem of blocking, being normally carried out of impact production.
Its feed pipe of boiling drier 2 (i.e. vacuum intake pipe) 24 on the radial section of the corresponding charging basket 23 of boiling drier 2, be that the angle 25 of 30 degree is downward-sloping or extend horizontally into charging basket 23 with the corresponding tangent line with this charging basket 23 of this boiling drier 2, and its feed pipe 24 is arranged at the upper end by charging basket 23. On web plate, block air channel to avoid the material making input directly to fall after charging aperture (or feed pipe), and make material to heat more fully.
The wall of its aperture, corresponding one end (import or export) end face of each mesh 10 of the corresponding web plate 9 of boiling drier 2 one side corresponding to web plate 9 (by import or export one side) is one or is equal to the angle less than 180 degree, namely the port of corresponding one end of this mesh is in the top, plate face of the corresponding one side of web plate, flow through each mesh 10 material flow to direction and the corresponding axial direction of web plate be one more than 0 degree less than 90 degree of angles. Each mesh 10 of web plate 9 is stamped and formed out by web plate 9 plate body, and its each lobe 10b being stamped and formed out is fish scale-shaped on a corresponding wall of web plate 9. The wind flowing through this web plate forms Scroll-tupe, extends the material route to corresponding dirt pocket, and then relatively extends the time of contact of material and hot blast, it is thus achieved that heats effect more fully.
The hot blast process system 8 of boiling drier 2 includes the roughing efficiency air filter 11 being located in the air intake vent of the hot blast process system 8 in the corresponding air channel of opposite upper parts, is respectively arranged on the medium effeciency filter 15 in the corresponding air channel of opposing lower portions, hi-temp hi-effective filter 18 and the heater between medium effeciency filter 15 and hi-temp hi-effective filter 18 16.
The hot blast of boiling drier 2 processes system 8 and is provided with corresponding dehydrating unit, described dehydrating unit includes the cold dehumidifier of table of the inlet side being located in the roughing efficiency air filter of the hot blast process system of boiling drier, and is located at the water fender of the air side (outlet side) of the cold dehumidifier of described table. Particularly as follows: dehydrating unit includes the cold dehumidifier 12 of table being located in the air channel of the opposite upper parts of the hot blast process system 8 of the air side (outlet side) of roughing efficiency air filter 11, and it is located at the water fender 13 of the air side (outlet side) of the cold dehumidifier 12 of table. Dehydrating unit (or the cold dehumidifier of its table) is provided with drain pipe 14, and its drain pipe 14 is stretched out by opposing lower portions air channel. Between heater 16 and hi-temp hi-effective filter 18, it is provided with cold heat wind controls valve 17. It can be prevented effectively from because of in air channel, relative humidity is too high and the bed that collapses that gets damp, and energy resource consumption can be reduced.
Wind enters air channel, bottom by the corresponding end entrance in air channel, top through roughing efficiency air filter, the cold dehumidifier of table, is heated by heater then through after medium effeciency filter, after after hi-temp hi-effective filter filters further boiling drier. Control valve 17 by cold heat wind air intake and can carry out the temperature of hot blast and/or air quantity is adjusted controlling.
The hot blast of boiling drier 2 processes the cold heat wind air intake control valve 17 of system 8 and is provided with corresponding valve positioner.
The outfan of described boiling drier is connected to corresponding lifting vacuum pelletizing machine. Being provided with multiple field cloth bag between described lifting vacuum pelletizing machine with corresponding turnover barrel, the internal layer of corresponding one end of described multiple field cloth bag stretches in turnover barrel, its outer layer is connected to the bundle cloth bag mouth having enough to meet the need barrel. Namely its lifting vacuum pelletizing machine 3 passes through a two-layer cloth bag 32 and corresponding turnover barrel connection, and barrel 31 inner chamber is had enough to meet the need in stretching to the internal layer 32b having enough to meet the need one end that barrel 31 is connected of multiple field cloth bag 32, its outer layer 32a is connected to the bundle cloth bag mouth having enough to meet the need barrel 31. Two-layer cloth bag is made up of anti-electrostatic filter cloth. On the basis of the tightness and reliability that improve system, it is possible to effectively prevent from promoting between vacuum pelletizing machine and turnover barrel and be detained material, it is to avoid the generation of variant products material is mixed, and quality problems occur.
The dustless production system of this utility model high-viscosity material granulation is to produce on conventional material technological parameter basis, by wet granulator stirring slurry speed reduction, improves cutter speed, and then adds the cutting times of cutter and material.
When the high-viscosity material of the present utility model dustless production system of granulation is run; startup system; by the powder vacuum feeding mode after weighing; add in the pot of wet granulator; open corresponding stirring at low speed and cutting; then adding slurry tank by pressure and be pressed in pot by slurry, open high-speed stirred, the visor that can pass through on pot cover observes material forming situation. Wet granulator of the present utility model is on conventional material production technological parameter basis, and reduction slurry is input to the slurry agitation speed of the homogenizer after pot, and improves corresponding cutter speed, increases the cutting times of cutter and material.
After granulation completes; open oscillating granulator; boiling drier heater, air-introduced machine (or predrying blower fan), open the discharge door of wet granulator; stirring slurry slowly runs and transports material to boiling drier; in dry run, carry out degree according to dry, constantly adjust blower fan frequency; air inlet valve (cold heat wind air intake controls valve) opening angle, and steam rates adjustment valve. After having dried; open the Vacuum discharge mouth of boiling drier, vacuum feeder and promote vacuum pelletizing machine; (production capacity of surge tank volume and boiling drier is supporting wouldn't to open the manual discharge valve of vacuum lifting pelletizing machine surge tank; ensure that material can disposable exhaust) material is delivered to vacuum lifting pelletizing machine surge tank, with performing fighting out pulse dust removal. After having carried, closing vacuum feeder and pulse dust removal, open pelletizing machine, pelletizing machine discharging opening is docked with turnover barrel by anti-quiet two-layer cloth bag, it is achieved closed dust-free. As putty and arch formation occur in blanking granulate process, hammer type vibrator can be opened and knock tank skin.
Claims (10)
1. the high-viscosity material dustless production system of granulation; the oscillating granulator being connected with described wet granulator including wet granulator and the boiling drier being connected with described oscillating granulator, is characterized in that being provided with between described oscillating granulator and boiling drier a pre-drying device.
2. high-viscosity material is granulated dustless production system according to claim 1, it is characterized in that described pre-drying device includes its outlet and is connected to the hot blast of described boiling drier and processes the predrying blower fan between system and the discharging opening of oscillating granulator.
3. according to claim 2 high-viscosity material granulate dustless production system, it is characterized in that being provided with between described predrying blower fan and oscillating granulator an air inducing Setting Tank.
4. the dustless production system of high-viscosity material according to claim 1 or claim 2 granulation, is characterized in that its feed pipe of described boiling drier is that an angle less than 90 degree extends in bucket with charging basket tangent line corresponding with this boiling drier.
5. high-viscosity material according to claim 1 or claim 2 is granulated dustless production system, it is characterized in that this corresponding wall simultaneously of its aperture, corresponding one end end face of the mesh of the corresponding web plate of described boiling drier and web plate is an angle less than 180 degree.
6. high-viscosity material is granulated dustless production system according to claim 5, it is characterized in that the mesh of described web plate is stamped and formed out by web plate wooden partition, its lobe being stamped and formed out on wall of this corresponding one side of web plate in fish scale-shaped.
7. the dustless production system of high-viscosity material according to claim 1 or claim 2 granulation, it is characterized in that the hot blast of described boiling drier processes system and is provided with corresponding dehydrating unit, described dehydrating unit includes the cold dehumidifier of table of the inlet side being located in the roughing efficiency air filter of the hot blast process system of boiling drier, and is located at the water fender of the air side of the cold dehumidifier of described table.
8. the dustless production system of high-viscosity material according to claim 1 or claim 2 granulation, is characterized in that the cold heat wind air intake of the hot blast of described boiling drier process system controls valve and is provided with corresponding valve positioner.
9. the dustless production system of high-viscosity material according to claim 1 or claim 2 granulation, is characterized in that the outfan of described boiling drier is connected to corresponding lifting vacuum pelletizing machine.
10. according to claim 9 high-viscosity material granulate dustless production system; it is characterized in that being provided with multiple field cloth bag between described lifting vacuum pelletizing machine with corresponding turnover barrel, the internal layer of corresponding one end of described multiple field cloth bag stretches in turnover barrel, its outer layer is connected to the bundle cloth bag mouth having enough to meet the need barrel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521097441.4U CN205279610U (en) | 2015-12-26 | 2015-12-26 | Dustless production system of high viscosity material pelletization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521097441.4U CN205279610U (en) | 2015-12-26 | 2015-12-26 | Dustless production system of high viscosity material pelletization |
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| Publication Number | Publication Date |
|---|---|
| CN205279610U true CN205279610U (en) | 2016-06-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521097441.4U Expired - Fee Related CN205279610U (en) | 2015-12-26 | 2015-12-26 | Dustless production system of high viscosity material pelletization |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205279610U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105423704A (en) * | 2015-12-26 | 2016-03-23 | 宜春万申制药机械有限公司 | Dust-free production system for granulating high-viscosity material |
| CN116116329A (en) * | 2023-04-13 | 2023-05-16 | 成都圣恩生物科技股份有限公司 | Seasoning processing production line |
-
2015
- 2015-12-26 CN CN201521097441.4U patent/CN205279610U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105423704A (en) * | 2015-12-26 | 2016-03-23 | 宜春万申制药机械有限公司 | Dust-free production system for granulating high-viscosity material |
| WO2017107836A1 (en) * | 2015-12-26 | 2017-06-29 | 宜春万申制药机械有限公司 | Hopper washing drying system |
| CN105423704B (en) * | 2015-12-26 | 2019-01-22 | 宜春万申制药机械有限公司 | The dustless production system of high-viscosity material granulation |
| CN116116329A (en) * | 2023-04-13 | 2023-05-16 | 成都圣恩生物科技股份有限公司 | Seasoning processing production line |
| CN116116329B (en) * | 2023-04-13 | 2023-07-11 | 成都圣恩生物科技股份有限公司 | Seasoning processing production line |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 Termination date: 20171226 |
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| CF01 | Termination of patent right due to non-payment of annual fee |