CN216557953U - Drying process system of stickness material - Google Patents
Drying process system of stickness material Download PDFInfo
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- CN216557953U CN216557953U CN202123316365.XU CN202123316365U CN216557953U CN 216557953 U CN216557953 U CN 216557953U CN 202123316365 U CN202123316365 U CN 202123316365U CN 216557953 U CN216557953 U CN 216557953U
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Abstract
The utility model relates to a drying treatment system for viscous materials, which comprises a feeder, a flash evaporation drying device, a cyclone separator, a bag-type dust collector and an induced draft fan which are arranged in sequence, the lower part of the flash drying device is provided with an air inlet, a feed inlet is arranged above the air inlet, the upper part of the flash drying device is provided with a discharge outlet, the air inlet of the flash drying device is connected with a hot blast stove, the feed inlet of the flash drying device is connected with the outlet of the feeding device, the inlet of the feeding device is connected with the outlet of the feeder, the outlet of the feeding device is connected with a distributor, the distributor is arranged in the flash drying device and comprises a feeding channel with an opening at one end, the open end of the feeding channel is connected with the outlet of the feeding device, the feeding channel is a tubular channel, and a plurality of discharging holes are formed in the feeding channel. The utility model improves the drying effect, is not easy to block the air inlet at the bottom, improves the working efficiency and reduces the failure rate.
Description
Technical Field
The utility model relates to the technical field of material drying, in particular to a drying treatment system for viscous materials.
Background
The flash evaporation dryer is a novel continuous drying device integrating drying, crushing and screening, and is particularly suitable for drying cake-shaped, paste-shaped and slurry-shaped materials. The existing flash dryer often has the problems that the material is blocked inside and is not easy to clean, the service life is short, the heat exchange effect is poor, and the like.
Especially flash dryer's feed inlet, when handling the great material of moisture height, stickness, the stickness material is fallen by a feed inlet monoblock, and weight is big, and falling speed is fast, is difficult for stirring the bits of broken glass, and the hot-blast mouth that blocks up the bottom part after the whereabouts is hot-blast can not blown up whole material, causes the air-blower air inlet not smooth, and the internal temperature of desiccator is not high, and the intake stack temperature continuously rises, leads to shutting down the trouble, reduces work efficiency.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects and provide a drying treatment system for viscous materials, which is suitable for drying the viscous materials.
The purpose of the utility model is realized as follows:
a drying treatment system for viscous materials comprises a feeder, a flash drying device, a cyclone separator, a bag-type dust collector and an induced draft fan which are sequentially arranged, wherein an air inlet is formed in the lower portion of the flash drying device, a feed inlet is formed above the air inlet, a discharge port is formed in the upper portion of the flash drying device, the air inlet of the flash drying device is connected with a hot blast stove, the feed inlet of the flash drying device is connected with the outlet of the feed device, the inlet of the feed device is connected with the outlet of the feeder, the discharge port of the flash drying device is connected with the upper portion of the cyclone separator, a discharge port is formed in the bottom of the cyclone separator, the cyclone separator is connected with the bag-type dust collector through a pipeline, and the bag-type dust collector is connected with the induced draft fan through a pipeline; the feeding device is a spiral feeder, an outlet of the spiral feeder is connected with a distributor, the distributor is arranged in the flash evaporation drying device and comprises a feeding channel with an open end, the open end of the feeding channel is connected with the outlet of the feeding device, the feeding channel is a tubular channel, and a plurality of discharge holes are formed in the feeding channel.
Furthermore, a plurality of discharging holes are respectively arranged on two side walls of the feeding channel.
Further, the discharge holes are uniformly distributed.
Furthermore, the distance between two adjacent discharge holes is from large to small, and the distance from the open end to the closed end of the feeding channel is from sparse to dense.
Further, a discharge hole is formed in the bottom of the bag-type dust collector, and a spiral discharging machine is arranged at the discharge hole.
Compared with the prior art, the utility model has the beneficial effects that:
according to the flash evaporation drying device, the distributor is arranged in the flash evaporation drying device and connected with the feeding device, the feeding device extrudes materials into the feeding channel of the distributor through the screw, and then the strip-shaped materials are extruded through the discharge hole, so that the flash evaporation drying device is easy to break and light in weight, hot air at the lower part can be blown up conveniently, and part of the materials can be dried by the hot air in the dropping process, the drying effect is improved, the air inlet at the bottom is not easy to block, the working efficiency is improved, and the failure rate is reduced.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic structural view of a distributor according to embodiment 1 of the present invention.
Fig. 3 is a schematic structural view of a distributor according to embodiment 2 of the present invention.
Fig. 4 is a schematic structural view of a distributor according to embodiment 3 of the present invention.
Wherein:
feeder 1, hot-blast furnace 2, feed arrangement 3, flash drying device 4, distributing device 5, feedstock channel 5.1, discharge opening 5.2, cyclone 6, sack cleaner 7, draught fan 8.
Detailed Description
For a better understanding of the technical aspects of the present invention, reference will now be made in detail to the accompanying drawings. It should be understood that the following specific examples are not intended to limit the embodiments of the present invention, but are merely exemplary embodiments of the present invention. It should be noted that the description of the positional relationship of the components, such as the component a is located above the component B, is based on the description of the relative positions of the components in the drawings, and is not intended to limit the actual positional relationship of the components.
Example 1:
referring to fig. 1-2, fig. 1 is a schematic diagram of a viscous material drying system. As shown in the figure, the drying treatment system for viscous materials comprises a feeder 1, a flash evaporation drying device 4, a cyclone separator 6, a bag-type dust collector 7 and an induced draft fan 8 which are sequentially arranged, the lower part of the flash evaporation drying device 4 is provided with an air inlet, a feed inlet is arranged above the air inlet, the upper part of the flash drying device 4 is provided with a discharge hole, the air inlet of the flash drying device 4 is connected with the hot blast stove 2, the feed inlet of the flash evaporation drying device 4 is connected with the outlet of the feeding device 3, the inlet of the feeding device 3 is connected with the outlet of the feeder 1, the discharge hole of the flash evaporation drying device 4 is connected with the upper part of the cyclone separator 6, the bottom of the cyclone separator 6 is provided with a discharge hole, the cyclone separator 6 is connected with a bag-type dust collector 7 through a pipeline, and the bag-type dust collector 7 is connected with an induced draft fan 8 through a pipeline.
The feeding device 3 is a spiral feeder, an outlet of the spiral feeder is connected with a distributor 5, the distributor 5 is arranged in a flash drying device 4, the distributor 5 comprises a feeding channel 5.1 with an open end, the open end of the feeding channel 5.1 is connected with an outlet of the feeding device 3, and a plurality of discharge holes 5.2 are arranged on the feeding channel 5.1.
The feeding channel 5.1 is a tubular channel, a row of discharging holes 5.2 are respectively arranged on two side walls of the feeding channel, and the discharging holes 5.2 are uniformly distributed.
The bottom of the bag-type dust collector 7 is provided with a discharge hole, and a spiral discharging machine is arranged at the discharge hole.
Example 2:
referring to fig. 1 and 3, fig. 3 is a schematic view showing the structure of the distributor of the present embodiment 2. As shown in the drawings, the drying processing system for viscous materials in this embodiment 2 is different from that in embodiment 1 in that the discharging holes 5.2 on the feeding channel 5.1 are not uniformly arranged, and the distance between two adjacent discharging holes 5.2 is from large to small, and from the open end to the closed end of the feeding channel 5.1, the discharging holes are from sparse to dense.
Because the extruded pressure of the open end of the feed channel 5.1 is larger than that of the closed end, the closed end is additionally provided with the discharge holes 5.2, so that the discharge is facilitated, and the blockage is not easy to cause.
Example 3:
referring to fig. 1 and 4, fig. 4 is a schematic structural view of the distributor of the present embodiment 2. As shown in the drawings, the drying processing system for viscous materials in this embodiment 2 is different from that in embodiment 1 in that two rows of discharge holes 5.2 are respectively formed on two side walls of the feeding channel 5.1.
The above is only a specific application example of the present invention, and the protection scope of the present invention is not limited in any way. All the technical solutions formed by equivalent transformation or equivalent replacement fall within the protection scope of the present invention.
Claims (5)
1. A drying processing system of stickness material which characterized in that: it comprises a feeder (1), a flash drying device (4), a cyclone separator (6), a bag-type dust collector (7) and a draught fan (8) which are arranged in sequence, the lower part of the flash evaporation drying device (4) is provided with an air inlet, a feed inlet is arranged above the air inlet, a discharge hole is arranged at the upper part of the flash evaporation drying device (4), an air inlet of the flash evaporation drying device (4) is connected with a hot blast stove (2), the feed inlet of the flash evaporation drying device (4) is connected with the outlet of the feeding device (3), the inlet of the feeding device (3) is connected with the outlet of the feeder (1), the discharge hole of the flash evaporation drying device (4) is connected with the upper part of the cyclone separator (6), the bottom of the cyclone separator (6) is provided with a discharge opening, the cyclone separator (6) is connected with a bag-type dust collector (7) through a pipeline, the bag-type dust collector (7) is connected with an induced draft fan (8) through a pipeline; feed arrangement (3) are screw feeder, a distributing device (5) of its exit linkage, distributing device (5) set up in flash drying device (4), distributing device (5) include one end open-ended feedstock channel (5.1), the export of feed arrangement (3) is connected to the open end of feedstock channel (5.1), feedstock channel (5.1) are the tubulose passageway, are equipped with a plurality of discharge openings (5.2) on feedstock channel (5.1).
2. A viscous material drying system according to claim 1, wherein: and a plurality of discharging holes (5.2) are respectively arranged on two side walls of the feeding channel (5.1).
3. A viscous material drying system according to claim 1, wherein: the discharge holes (5.2) are uniformly distributed.
4. A viscous material drying system according to claim 1, wherein: the distance between two adjacent discharge holes (5.2) is from large to small, and the distance from the open end to the closed end of the feed channel (5.1) is from sparse to dense.
5. A viscous material drying system according to claim 1, wherein: the bottom of the bag-type dust collector (7) is provided with a discharge hole, and a spiral discharging machine is arranged at the discharge hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123316365.XU CN216557953U (en) | 2021-12-28 | 2021-12-28 | Drying process system of stickness material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123316365.XU CN216557953U (en) | 2021-12-28 | 2021-12-28 | Drying process system of stickness material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216557953U true CN216557953U (en) | 2022-05-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123316365.XU Active CN216557953U (en) | 2021-12-28 | 2021-12-28 | Drying process system of stickness material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216557953U (en) |
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2021
- 2021-12-28 CN CN202123316365.XU patent/CN216557953U/en active Active
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