CN220328492U - Production line of fragrant washing sheets - Google Patents
Production line of fragrant washing sheets Download PDFInfo
- Publication number
- CN220328492U CN220328492U CN202321854439.1U CN202321854439U CN220328492U CN 220328492 U CN220328492 U CN 220328492U CN 202321854439 U CN202321854439 U CN 202321854439U CN 220328492 U CN220328492 U CN 220328492U
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- Prior art keywords
- speed mixer
- cold high
- dryer
- auger
- hot
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- 238000005406 washing Methods 0.000 title abstract description 25
- 239000003205 fragrance Substances 0.000 claims abstract description 31
- 238000005485 electric heating Methods 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 8
- 238000004064 recycling Methods 0.000 claims description 3
- 239000002994 raw material Substances 0.000 abstract description 25
- 239000002245 particle Substances 0.000 abstract description 17
- 238000001035 drying Methods 0.000 abstract description 14
- 239000000463 material Substances 0.000 abstract description 12
- 238000005265 energy consumption Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 description 24
- 239000002304 perfume Substances 0.000 description 9
- 239000011149 active material Substances 0.000 description 6
- 239000013543 active substance Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Detergent Compositions (AREA)
Abstract
The utility model relates to a washing sheet production's field especially relates to a fragrance washing sheet production line, and it includes blendor, desiccator, the cold high-speed mixer of heat and tablet press, and the discharge end of blendor is connected with the feed end of desiccator, and the discharge end of desiccator is connected with the cold high-speed mixer of heat through the second auger, is provided with the feeder hopper on the cold high-speed mixer of heat, and the discharge end of the cold high-speed mixer of heat is connected with the tablet press through the third auger. According to the method, the fragrance particles are firstly processed by the mixer and the dryer, then the dried fragrance particles are mixed with the raw materials of the washing active matters, the total amount of materials required to be dried is reduced, the energy consumption and time required by a drying step are reduced, and the method has the effects of improving the production efficiency and reducing the energy consumption.
Description
Technical Field
The application relates to the field of laundry sheet production, in particular to a production line of fragrant laundry sheets.
Background
The washing sheet is a novel multifunctional ecological washing product developed by adopting a nano super-concentration technology, and compared with the traditional mode, the washing sheet greatly improves the decontamination capability of the product, has no phosphorus and no addition and no hurt to hands, can be rapidly decomposed and dissolved after meeting water, releases nano-scale clean micromolecules, and further and thoroughly purifies stubborn stains deposited on clothes.
In order to increase the fragrance of the washing tablet, in the production and processing process of the washing tablet, the fragrance raw material and the washing active material with the decontamination effect are mixed by a mixer, and the fragrance raw material contains liquid essence, so that the uniformly mixed raw material is required to be conveyed into a dryer for drying, and finally, the finished powder after drying is conveyed into a tablet press for tablet forming.
With respect to the related art in the above, the inventors consider that there are the following drawbacks: the liquid-containing fragrance raw materials are directly mixed with the dry washing active material raw materials, so that all the raw materials are required to be dried finally, the production efficiency is reduced, and the dried finished product powder is required to be manually transferred into a tablet press, so that the time and the labor are wasted, the labor intensity is increased, and the production efficiency is reduced.
Disclosure of Invention
In order to solve the problem of low production efficiency of the laundry detergent tablet, the application provides a production line of the fragrant laundry detergent tablet.
The application provides a fragrance laundry piece production line adopts following technical scheme:
the utility model provides a fragrance laundry tablet production line, includes blendor, desiccator, the cold high-speed mixer of heat and tablet press, the discharge end of blendor with the feed end of desiccator is connected, the discharge end of desiccator pass through the second auger with the cold high-speed mixer of heat is connected, be provided with the feeder hopper on the cold high-speed mixer of heat, the discharge end of the cold high-speed mixer of heat pass through the third auger with the tablet press is connected.
By adopting the technical scheme, the fragrance raw materials are sent into a mixer for uniform mixing, the mixed raw materials enter a dryer for drying to obtain fragrance particles, the fragrance particles are sent into a hot-cold high-speed mixer through a second auger, meanwhile, the washing active material raw materials are sent into the hot-cold high-speed mixer from a feed hopper, the fragrance particles and the washing active material raw materials are uniformly mixed in the hot-cold high-speed mixer to obtain finished product powder, and the finished product powder is sent into a tablet press for tabletting through a third auger to obtain a finished product of the washing tablet; the fragrance particles are firstly processed by the mixer and the dryer, and then the dried fragrance particles are mixed with the raw materials of the washing active matters, so that the total amount of the materials to be dried is reduced, the energy consumption and the time required by the drying step are reduced, the effect of improving the production efficiency is realized, the energy consumption is reduced, and the environment is protected.
Optionally, a dehydrator is arranged between the mixer and the dryer, the discharge end of the mixer is fixed and communicated with the feed end of the dehydrator, and the discharge end of the dehydrator is fixed and communicated with the feed end of the dryer through a first auger.
Through adopting above-mentioned technical scheme, the raw materials after the blendor mixes get into the hydroextractor and dewater, and the semi-dry fragrance powder after the dehydration is sent into the desiccator through first auger and is dried, dehydrates to the semi-dry back with the hydroextractor earlier, and then is dried by the desiccator, has further improved drying efficiency, does benefit to improvement production efficiency.
Optionally, an electric heating air generator is arranged on the dryer, and an air outlet end of the electric heating air generator is fixed and communicated with the dryer.
Through adopting above-mentioned technical scheme, utilize electric hot air generator to send into hot-blast towards the desiccator in, do benefit to the air velocity of flow in the improvement desiccator, improve the drying efficiency of desiccator promptly.
Optionally, the dryer with be provided with fragrance recovery mechanism between the cold high-speed mixer of heat, fragrance recovery mechanism includes second pipeline, draught fan and third pipeline, the end of breathing in of draught fan pass through the second pipeline with the dryer is connected, the end of giving vent to anger of draught fan pass through the third pipeline with the cold high-speed mixer of heat is fixed and the intercommunication.
Through adopting above-mentioned technical scheme, the draught fan work for steam in the desiccator gets into in the hot cold high-speed mixer through second pipeline, draught fan and third pipeline, contains the essence that part is heated and evaporates in the steam and liquefies and mix with the powder after the cooling in the hot cold high-speed mixer, does benefit to the essence composition in the recycle steam, has reduced the waste of raw and other materials.
Optionally, a cyclone discharger is arranged between the second pipeline and the dryer, an air outlet pipe is fixed and communicated between the dryer and the air inlet end of the cyclone discharger, the second pipeline is fixed and communicated with the air outlet end of the cyclone discharger, and the discharging end of the cyclone discharger is fixed and communicated with the second auger.
Through adopting above-mentioned technical scheme, the draught fan work for steam in the desiccator gets into whirlwind tripper by the outlet duct, utilizes whirlwind tripper to hold back the powder that carries in the steam and carries the powder to the second auger in, then the steam gets into the draught fan through the second pipeline, does benefit to preventing that the powder from getting into the draught fan, improves the life of draught fan.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the fragrance particles are firstly processed by the mixer, the dehydrator and the dryer, and then the dried fragrance particles are mixed with the raw materials of the washing active matters, so that the total amount of the materials to be dried is reduced, the energy consumption and the time required by the drying step are reduced, the materials are dehydrated to be semi-dry by the dehydrator and then dried by the dryer, the drying efficiency is further improved, the effect of improving the production efficiency is realized, the energy consumption is reduced, and the energy is saved and the environment is protected;
2. the first auger, the second auger and the third auger are used for conveying materials, the first pump body and the second pump body are respectively beneficial to smooth conveying of powder in the first pipeline and the discharging pipe, manual material transferring is avoided, manual labor force is saved, manual labor intensity is reduced, the conveying efficiency of the materials is improved, and production efficiency is further improved;
3. the electric heating air generator is used for feeding hot air into the dryer, so that the drying efficiency of the dryer is improved, the hot air enters the hot-cold high-speed mixer through the second pipeline, the induced draft fan and the third pipeline, and evaporated essence contained in the hot air is cooled in the hot-cold high-speed mixer, liquefied and mixed with powder, so that the essence components in the hot air are recycled.
Drawings
Fig. 1 is a schematic overall structure of an embodiment of the present application.
Reference numerals: 1. a mixer; 2. a dryer; 3. a hot and cold high speed mixer; 4. a tablet press; 5. a dehydrator; 6. a first auger; 7. a second auger; 8. a first pipe; 9. a first pump body; 10. a feed hopper; 11. a third auger; 12. a discharge pipe; 13. a second pump body; 14. an electric heating wind generating furnace; 15. a second pipe; 16. an induced draft fan; 17. a third conduit; 18. a cyclone discharger; 19. and an air outlet pipe.
Detailed Description
The present application is described in further detail below in conjunction with fig. 1.
The embodiment of the application discloses a fragrance laundry sheet production line.
The utility model provides a fragrance laundry tablet production line, includes blendor 1, desiccator 2, hot and cold high-speed mixer 3 and tablet press 4, and blendor 1's discharge end is connected with desiccator 2's feed end, is provided with hydroextractor 5 between blendor 1 and the desiccator 2, and blendor 1's discharge end is fixed and the feed end of hydroextractor 5 communicates, and hydroextractor 5's discharge end is fixed and the feed end of desiccator 2 communicates through first auger 6.
The discharge end of the dryer 2 is connected with the hot and cold high-speed mixer 3 through a second auger 7, the hot and cold high-speed mixer 3 adopts SRL-Z series hot and cold high-speed mixer units, the discharge end of the dryer 2 is fixed and communicated with the feed end of the second auger 7, a first pipeline 8 is fixed and communicated between the discharge end of the second auger 7 and the hot and cold high-speed mixer 3, and a first pump body 9 for conveying powder is arranged on the first pipeline 8.
Be provided with feeder hopper 10 on the cold high-speed mixer 3 of heat, the discharge end of cold high-speed mixer 3 of heat is connected with tablet press 4 through third auger 11, and the discharge end of cold high-speed mixer 3 of heat is fixed and the intercommunication with the feed end of third auger 11, is fixed and the intercommunication has discharging pipe 12 between the discharge end of third auger 11 and the feed end of tablet press 4, is provided with the second pump body 13 that is used for carrying the powder on the discharging pipe 12.
The perfume raw materials are sent into a mixer 1 to be uniformly mixed, the mixed raw materials enter a dehydrator 5 to be dehydrated, the dehydrated semi-dry perfume powder is sent into a dryer 2 through a first auger 6 and is dried in a rotating way at the temperature of 60-70 ℃, and the semi-dry perfume powder is dried to obtain perfume particles with the diameter of 0.5-1.0 mm; and then the fragrance particles are conveyed into a hot and cold high-speed mixer 3 through a second auger 7 and a first pipeline 8, then the washing active material raw materials are conveyed into the hot and cold high-speed mixer 3 from a feed hopper 10, the fragrance particles and the washing active material raw materials are uniformly mixed by the hot and cold high-speed mixer 3 to obtain finished product powder, and the finished product powder is conveyed into a tablet press 4 through a third auger 11 and a discharge pipe 12 to be pressed into tablets, so that the finished product of the washing tablet is obtained.
The perfume particles are firstly processed by the mixer 1, the dehydrator 5 and the dryer 2, then the dried perfume particles are mixed with the raw materials of the washing active substances, and the total amount of the materials to be dried is reduced, so that the energy consumption and time required by the drying step are reduced, the dehydrator 5 is firstly used for dehydrating to be semi-dry and then the semi-dry is dried by the dryer 2, the drying efficiency is further improved, the effect of improving the production efficiency is realized, the energy consumption is reduced, and the energy conservation and the environmental protection are realized.
The materials are conveyed through the first auger 6, the second auger 7 and the third auger 11, the first pump body 9 and the second pump body 13 are respectively beneficial to smooth conveying of the powder in the first pipeline 8 and the discharging pipe 12, conveying efficiency of the first pipeline 8 and the discharging pipe 12 is guaranteed, manual material conveying is avoided, labor force is saved, labor intensity is reduced, conveying efficiency of the materials is improved, and production efficiency is improved.
Further, an electric heating air generator 14 is arranged on the dryer 2, an air outlet end of the electric heating air generator 14 is fixed and communicated with the dryer 2, a fragrance recycling mechanism is arranged between the dryer 2 and the hot and cold high-speed mixer 3 and comprises a second pipeline 15, an induced draft fan 16 and a third pipeline 17, and an air suction end of the induced draft fan 16 is connected with the dryer 2 through the second pipeline 15.
A cyclone discharger 18 is arranged between the second pipeline 15 and the dryer 2, an air outlet pipe 19 is fixed and communicated between the dryer 2 and the air inlet end of the cyclone discharger 18, the second pipeline 15 is fixed and communicated between the air outlet end of the cyclone discharger 18 and the air suction end of the induced draft fan 16, the discharging end of the cyclone discharger 18 is fixed and communicated with the second auger 7, and the air outlet end of the induced draft fan 16 is fixed and communicated with the hot-cold high-speed mixer 3 through a third pipeline 17.
The electric heating air generator 14 is used for feeding hot air into the dryer 2, so that the air flow rate in the dryer 2 is improved, namely the drying efficiency of the dryer 2 is improved, the induced draft fan 16 works, hot air in the dryer 2 enters the cyclone discharger 18 through the air outlet pipe 19, powder carried in the hot air is trapped by the cyclone discharger 18 and conveyed into the second auger 7, and the powder is prevented from entering the induced draft fan 16, and the service life of the induced draft fan 16 is prolonged.
The steam enters the hot-cold high-speed mixer 3 through the second pipeline 15, the induced draft fan 16 and the third pipeline 17, part of the heated and evaporated essence is contained in the steam, and the evaporated essence is liquefied and mixed with powder after the temperature of the steam is reduced in the hot-cold high-speed mixer 3, so that the essence components in the steam are recycled, and the waste of raw materials is reduced.
The implementation principle of the production line of the fragrant washing sheet is as follows:
the perfume raw materials are sent into a mixer 1 to be uniformly mixed, the mixed raw materials enter a dehydrator 5 to be dehydrated, then the raw materials are sent into a dryer 2 to be dried by a first auger 6 to obtain perfume particles, hot air is sent into the dryer 2 by an electric heating air generator 14 to improve the drying efficiency, and the perfume particles are conveyed into a hot-cold high-speed mixer 3 through a second auger 7 and a first pipeline 8.
Meanwhile, the induced draft fan 16 sends hot air exhausted by the dryer into the hot and cold high-speed mixer 3, the raw materials of washing active substances are sent into the hot and cold high-speed mixer 3 from the feed hopper 10, the evaporated essence is liquefied and mixed with powder after being cooled in the hot and cold high-speed mixer 3, the hot and cold high-speed mixer 3 evenly mixes the fragrance particles and the raw materials of the washing active substances to obtain finished powder, and the finished powder is conveyed into the tablet press 4 for tabletting through the third auger 11 and the discharge pipe 12 to obtain a finished product of the washing tablet.
The foregoing are all preferred embodiments of the present application, and are not intended to limit the scope of the present application in any way, therefore: all equivalent changes in structure, shape and principle of this application should be covered in the protection scope of this application.
Claims (5)
1. The utility model provides a fragrance laundry piece production line which characterized in that: including blendor (1), desiccator (2), hot cold high-speed mixer (3) and tablet press (4), the discharge end of blendor (1) with the feed end of desiccator (2) is connected, the discharge end of desiccator (2) pass through second auger (7) with hot cold high-speed mixer (3) are connected, be provided with feeder hopper (10) on hot cold high-speed mixer (3), the discharge end of hot cold high-speed mixer (3) pass through third auger (11) with tablet press (4) are connected.
2. A fragrance laundry tablet manufacturing line according to claim 1, characterized in that: be provided with hydroextractor (5) between blendor (1) with desiccator (2), the discharge end of blendor (1) with the feed end of hydroextractor (5) is fixed and the intercommunication, the discharge end of hydroextractor (5) pass through first auger (6) with the feed end of desiccator (2) is fixed and the intercommunication.
3. A fragrance laundry tablet manufacturing line according to claim 1, characterized in that: an electric heating air generating furnace (14) is arranged on the dryer (2), and the air outlet end of the electric heating air generating furnace (14) is fixed and communicated with the dryer (2).
4. A fragrance laundry tablet manufacturing line according to claim 3, characterized in that: the novel hot and cold high-speed mixer is characterized in that an aroma recycling mechanism is arranged between the dryer (2) and the hot and cold high-speed mixer (3), the aroma recycling mechanism comprises a second pipeline (15), an induced draft fan (16) and a third pipeline (17), an air suction end of the induced draft fan (16) is connected with the dryer (2) through the second pipeline (15), and an air outlet end of the induced draft fan (16) is fixed and communicated with the hot and cold high-speed mixer (3) through the third pipeline (17).
5. The fragrance laundry tablet manufacturing line of claim 4, wherein: the cyclone discharger (18) is arranged between the second pipeline (15) and the dryer (2), an air outlet pipe (19) is fixed and communicated between the dryer (2) and the air inlet end of the cyclone discharger (18), the second pipeline (15) is fixed and communicated with the air outlet end of the cyclone discharger (18), and the discharging end of the cyclone discharger (18) is fixed and communicated with the second auger (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321854439.1U CN220328492U (en) | 2023-07-14 | 2023-07-14 | Production line of fragrant washing sheets |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321854439.1U CN220328492U (en) | 2023-07-14 | 2023-07-14 | Production line of fragrant washing sheets |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220328492U true CN220328492U (en) | 2024-01-12 |
Family
ID=89450034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321854439.1U Active CN220328492U (en) | 2023-07-14 | 2023-07-14 | Production line of fragrant washing sheets |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220328492U (en) |
-
2023
- 2023-07-14 CN CN202321854439.1U patent/CN220328492U/en active Active
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