CN216132200U - Two-section dryer for viscous material - Google Patents
Two-section dryer for viscous material Download PDFInfo
- Publication number
- CN216132200U CN216132200U CN202121905729.5U CN202121905729U CN216132200U CN 216132200 U CN216132200 U CN 216132200U CN 202121905729 U CN202121905729 U CN 202121905729U CN 216132200 U CN216132200 U CN 216132200U
- Authority
- CN
- China
- Prior art keywords
- stir
- frying
- drying
- cylinder
- shaft
- 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.)
- Expired - Fee Related
Links
- 239000011345 viscous material Substances 0.000 title claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 99
- 238000007790 scraping Methods 0.000 claims abstract description 43
- 238000007599 discharging Methods 0.000 claims abstract description 30
- 238000004140 cleaning Methods 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims description 52
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 45
- 239000003546 flue gas Substances 0.000 claims description 45
- 238000006243 chemical reaction Methods 0.000 claims description 31
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 17
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 17
- 241001330002 Bambuseae Species 0.000 claims description 17
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 17
- 239000011425 bamboo Substances 0.000 claims description 17
- 230000011218 segmentation Effects 0.000 claims description 2
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000002028 Biomass Substances 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000010924 continuous production Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a two-section type dryer for viscous materials, relates to the technical field of drying equipment, and solves the technical problems that the viscous materials are seriously adhered to walls and are difficult to clean manually in the prior art. The technical characteristics comprise a stir-drying section and a drying section positioned at the downstream of the stir-drying section; the stir-drying section is provided with a stir-drying cylinder, a scraping device and a stir-frying device are arranged in the stir-drying cylinder, and a middle-end moisture-discharging device is arranged between the stir-drying section and the drying section. The drying machine has the beneficial effects of improving the drying efficiency, reducing the heat loss, realizing automatic cleaning and reducing the labor intensity of workers.
Description
Technical Field
The utility model relates to the technical field of drying equipment, in particular to a two-section type dryer for viscous materials.
Background
At present, in industries such as miners, solid waste treatment and feed, a lot of viscous materials exist, the viscous materials have the phenomenon of wall sticking in drying, the problem of automatic wall sticking cleaning cannot be solved by adopting a traditional single-cylinder drying machine, only the regular shutdown is carried out for manual cleaning, the normal production of enterprises is influenced, and meanwhile, the manual cleaning cost is also high. In addition, the single-cylinder dryer adopts a mode of burning natural gas and directly feeding the natural gas, so that the heat loss is large, the drying cost is high, and the single-cylinder dryer cannot be produced in cold areas in the north in winter. The single-cylinder dryer is longer than 20 meters, the moisture discharging device of the dryer can only be arranged at the tail end of the dryer, moisture evaporated from the front end can only be discharged from the tail end, and the drying effect and the drying efficiency of materials are greatly influenced.
SUMMERY OF THE UTILITY MODEL
The utility model provides a two-section dryer for viscous materials, aiming at solving the technical problems that the viscous materials are seriously adhered to walls and the manual cleaning difficulty is high in the prior art.
In order to solve the technical problems, the technical scheme of the utility model is as follows:
two segmentation drying-machines of viscidity material includes:
a parching section and a drying section downstream of the parching section;
the stir-drying section is provided with a stir-drying cylinder, a scraping device and a stir-frying device are arranged in the stir-drying cylinder, and a middle-end moisture-discharging device is arranged between the stir-drying section and the drying section.
Further, the parching section comprises:
the square box body is placed on the external frame, and the wall of the square box body is provided with a burner connecting port;
the stir-frying cylinder is positioned inside the square box body, a scraping device and a stir-frying device are arranged inside the stir-frying cylinder, and a discharge end of the stir-frying cylinder is provided with a square material leaking hole and a moisture connecting channel;
the drying machine fan cover is sleeved at the feed end of the frying cylinder;
an auger-type feeder at a feed end of the fry drying drum.
Further, the middle-end moisture removing device comprises:
the high-temperature flue gas conversion box and the moisture conversion box are arranged on an external frame and sleeved outside the frying cylinder and the drying cylinder, the moisture conversion box is communicated with the moisture connecting channel, the moisture conversion box is provided with a middle-end moisture discharging port, and the wall of the high-temperature flue gas conversion box is provided with a plurality of high-temperature flue gas connecting channels;
the high-temperature flue gas inlet pipe, the one end of high-temperature flue gas inlet pipe is in stir-fry dry section of thick bamboo and the cavity between the square box, and the other end is in the high-temperature flue gas transfer box, and high-temperature flue gas enters into in the section of thick bamboo of drying through a plurality of high-temperature flue gas connecting channel.
Further, the scraping device comprises: the scraping shaft and the scraping plates are arranged on the periphery of the scraping shaft, one end of the scraping shaft is connected with an external motor, and the scraping plates are attached to the inner wall of the frying cylinder;
the stir-frying device comprises a stir-frying shaft and a stir-frying plate arranged on the circumferential side of the stir-frying shaft, one end of the stir-frying shaft is connected with an external motor, the stir-frying shaft is positioned below the inner wall of the stir-frying cylinder, the scraping shaft is positioned above the inner wall of the stir-frying cylinder, and the axial lines of the stir-frying shaft and the scraping shaft are parallel to the axial line of the stir-frying cylinder.
Further, the drying section includes:
the drying cylinder is sleeved at the discharge end of the frying cylinder;
the L-shaped lifting plate is fixedly arranged on the inner wall of the drying cylinder;
the material guide plate is arranged on the inner wall of the drying cylinder and is positioned at the discharge end of the frying cylinder;
the discharging device is sleeved at the discharging end of the drying cylinder and placed on the external frame, a discharging port is formed in the bottom of the discharging device, and a tail-end moisture discharging port is formed in the top of the discharging device.
Furthermore, the bottom of the square box body is provided with a dust cleaning port.
Further, this disclosure still includes the device of breaing up, the device of breaing up includes: one end of the scattering shaft is connected with an external motor, and the scattering shaft is positioned below the auger-type feeder;
the scattering blades are fixedly arranged at the other end of the scattering shaft and are positioned at a discharge port below the auger-type feeder.
Furthermore, a wind shield is arranged at the discharge end of the frying cylinder.
The utility model has the following beneficial effects:
according to the two-section dryer for the viscous material, the scraping device and the stir-frying device are arranged, so that automatic cleaning is realized, and the technical problems that the viscous material is seriously adhered to the wall and the manual cleaning difficulty is large in the prior art are solved; the frying section and the drying section are integrated, the heat loss is small, the drying cost is low, and the continuous production can be realized in cold areas in the north in winter.
Drawings
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
Fig. 1 is a schematic structural view of a two-stage dryer for viscous materials according to the present invention.
The reference numerals in the figures denote:
1. an auger-type feeder; 2. a scraping shaft; 3. a dryer hood; 4. turning over the stir-frying shaft; 5. rolling a ring; 6. a square box body; 7. a burner connector; 8. cleaning the ash hole; 9. frying in a dry cylinder; 10. a scraping plate; 11. a high-temperature flue gas inlet pipe; 12. a high-temperature flue gas conversion box; 13. a moisture transfer box; 14. a middle moisture outlet; 15. a material guide plate; 16. a square material leaking hole; 17. a drive gear ring; 18. a drying drum; 19. a tail end moisture discharge port; 20. a discharge device; 21. a discharge port; 22. the high-temperature flue gas is connected with the channel; 23. a moisture connecting passage; 24. a drive gear; 25. a riding wheel; 26. an L-shaped material raising plate; 27. a wind deflector; 28. turning over the frying plate; 29. breaking up the shaft.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1, a two-stage dryer for viscous materials includes:
a parching section and a drying section downstream of the parching section;
the stir-drying section is provided with a stir-drying cylinder 9, a scraping device and a stir-frying device are arranged in the stir-drying cylinder 9, and a middle-end moisture discharging device is arranged between the stir-drying section and the drying section.
The working principle is as follows: the materials enter the frying cylinder 9, the materials are continuously fried through the self rotation of a frying device at the lower end of the frying cylinder 9, the materials are fully contacted with the wall of the frying cylinder 9, the temperature of the wall of the frying cylinder 9 is high under the heating of high-temperature flue gas of a burner or a hot blast stove, the materials can be rapidly heated, meanwhile, the moisture in the materials is evaporated out and is discharged outwards from a middle-end moisture discharge port, and the drying effect of a drying section is prevented from being influenced by the moisture entering the drying section; the scraping device is driven by the motor to rotate independently, so that the material adhered to the cylinder wall is cleaned; through the combination of the scraping device and the stir-frying device, automatic cleaning and automatic stir-frying are realized, and the technical problems that viscous materials are seriously adhered to walls and the manual cleaning difficulty is high in the prior art are solved; meanwhile, the frying section and the drying section are integrated, the heat loss is small, the drying cost is low, and the continuous production can be carried out in winter in northern cold regions.
In some embodiments, the sauting section comprises:
the square box body 6 is placed on the external frame, and the wall of the square box body 6 is provided with a burner connecting port 7;
the stir-frying cylinder 9 is positioned inside the square box body 6, a scraping device and a stir-frying device are arranged inside the stir-frying cylinder 9, and a discharge end of the stir-frying cylinder 9 is provided with a square material leakage hole 16 and a moisture connecting channel 23;
the dryer fan housing 3 is sleeved at the feed end of the parching cylinder 9, and the dryer fan housing 3 is sleeved at the feed end of the parching cylinder 9;
an auger type feeder 1, wherein the auger type feeder 1 is arranged at the feeding end of the frying cylinder 9.
In some embodiments, the middle-end tide discharge device comprises:
the high-temperature flue gas conversion box 12 and the moisture conversion box 13 are adjacent to the high-temperature flue gas conversion box 12, the high-temperature flue gas conversion box 12 and the moisture conversion box 13 are placed on an external frame and are sleeved outside the parching cylinder 9 and the drying cylinder 18, the moisture conversion box 13 is communicated with the plurality of moisture connecting channels 23, the moisture conversion box 13 is provided with a middle-end moisture discharging port 14, and the wall of the high-temperature flue gas conversion box 12 is provided with a plurality of high-temperature flue gas connecting channels 22;
and one end of the high-temperature flue gas inlet pipe 11 is positioned in a cavity between the parching cylinder 9 and the square box body 6, the other end of the high-temperature flue gas inlet pipe 11 is positioned in the high-temperature flue gas conversion box 12, and high-temperature flue gas enters the drying cylinder 18 through a plurality of high-temperature flue gas connecting channels 22.
In some embodiments, the scraping device comprises: the frying device comprises a scraping shaft 2 and scraping plates 10 arranged on the circumferential side of the scraping shaft 2, wherein one end of the scraping shaft 2 is connected with an external motor, and the scraping plates 10 are attached to the inner wall of a frying cylinder 9;
the stir-frying device comprises a stir-frying shaft 4 and a stir-frying plate 28 arranged on the circumferential side of the stir-frying shaft 4, one end of the stir-frying shaft 4 is connected with an external motor, the stir-frying shaft 4 is positioned below the inner wall of the stir-frying cylinder 9, the material scraping shaft 2 is positioned above the inner wall of the stir-frying cylinder 9, and the axial lines of the stir-frying shaft 4 and the material scraping shaft 2 are parallel to the axial line of the stir-frying cylinder 9.
In some embodiments, the drying section comprises:
the drying cylinder 18 is sleeved at the discharge end of the frying cylinder 9, and the drying cylinder 18 is sleeved at the discharge end of the frying cylinder 9;
the L-shaped material raising plate 26 is fixedly arranged on the inner wall of the drying cylinder 18;
the material guide plate 15 is arranged on the inner wall of the drying cylinder 18 and is positioned at the discharge end of the parching cylinder 9;
the discharging device 20 is sleeved on the discharging end of the drying cylinder 18 and placed on the outer frame, the bottom of the discharging device 20 is provided with a discharging hole 21, and the top of the discharging device 20 is provided with a tail-end moisture discharging hole 19.
In some embodiments, the bottom of the square box 6 has a dust removal port 8.
In some embodiments, the present disclosure further comprises a breaking device comprising: a breaking shaft 29, wherein one end of the breaking shaft 29 is connected with an external motor, and the breaking shaft 29 is positioned below the auger type feeder 1;
and the scattering blades are fixedly arranged at the other end of the scattering shaft 29 and are positioned at a discharge port below the auger type feeder 1.
In some embodiments, the discharge end of the fry drying cylinder 9 is provided with a wind shield 27.
In some embodiments, the discharge end of the parching cylinder 9 is provided with a wind screen 27, a plurality of guide wheels are installed on the circumference side of the wind screen 27, the guide wheels are in sliding fit with guide rings on the parching cylinder 9, the material scraping shaft 2 and the parching shaft 4 are in running fit with the wind screen 27, when the parching cylinder 9 rotates, the wind screen 27 can rotate relative to the parching cylinder 9 through the rotation of the guide wheels, namely the relative positions of the material scraping shaft 2 and the parching shaft 4 can be kept unchanged, and the independent work of the material scraping shaft 2 and the parching shaft 4 is ensured; a wind guard 27 is provided so that moisture can enter the moisture transfer box 13 only through the moisture connection passage 23.
Specifically, the materials enter the frying cylinder 9 through the auger type feeding device 1, the materials are scattered by the high-speed scattering device arranged at the lower side and fall down when falling, the external motor drives the scattering shaft 29 to rotate at high speed, further driving the scattering blades to rotate at high speed, so as to realize the purpose of scattering materials, the materials fall to the bottom of the frying cylinder 9, the lower end of the frying cylinder 9 is provided with a stir-frying device, the stir-frying device is composed of a stir-frying shaft 4 and a stir-frying plate 28 with an inclination angle, the independent low-speed rotation can be realized through an external motor, the frying device rotates to continuously fry the materials, the materials are fully contacted with the wall of the frying cylinder 9, the high-temperature flue gas of the burner or the hot blast stove heats the frying cylinder 9 through the burner connecting port 7 of the square box body 6, the temperature is high, the material in the frying cylinder 9 can be quickly heated, and the moisture evaporated from the material is discharged out of the region from the middle end discharging port 14; because this disclosure has certain inclination in the actual installation, the material moves to the tail end (the discharge end) of the dry section of thick bamboo 9 of frying under the effect of gravity and the stir-fry board 28 that has the inclination, and drop into the drying section of thick bamboo 18 from square hourglass material hole 16, the diameter of drying section of thick bamboo 18 is greater than the diameter of the dry section of thick bamboo 9 of frying, the dry section of thick bamboo 9 of frying is embedded into the drying section of thick bamboo 18, connect into an organic whole through the support column between the two, drive gear 24 through external motor and rotate, and then drive gear 24 drives the drive ring gear 17 who fixes in the drying section of thick bamboo 18 outside and rotates, the circumference side of the dry section of thick bamboo 9 of frying and drying section of thick bamboo 18 all is equipped with rolls circle 5 and riding wheel 25, and then realized the dry section of thick bamboo 9 of frying and drying section of thick bamboo 18 synchronous revolution. The stir-fry dry section is equipped with scraper, and scraper comprises scraping axle 2 and scraping plate 10, and is rotatory alone under the drive of outside motor, and the purpose is exactly will glue and clear up the material on the wall of stir-fry dry section of thick bamboo 9 section of thick bamboo.
The square box body 6 is a heat preservation box body arranged outside the frying cylinder 9, the biomass burner or the hot blast stove is connected with the square box body 6 through a burner connector 7 arranged on the biomass burner, high-temperature flame generated by the biomass burner directly heats the frying cylinder 9, and moisture evaporated in the frying cylinder 9 is led to the moisture conversion box 13 through the moisture connecting channel 23 and then is absorbed and discharged by the middle-end moisture-discharging induced draft fan through the middle-end moisture-discharging port 14. The tail end of the drying cylinder 9 is provided with a wind shield 27, moisture can only enter the moisture conversion box 13 through the moisture connecting channel 23 through the square material leakage hole 16, because the connecting channel 23 is provided with a movable baffle plate near the end of the drying cylinder, the movable baffle plate is arranged on the inner wall of the drying cylinder through a shaft pin, when the drying cylinder is arranged above, the movable baffle plate closes the direction of the connecting channel 23 entering the drying cylinder, when the movable baffle plate is arranged at the bottom end, the movable baffle plate is in an open state, and the material coming out from the rectangular material leakage hole 16 is not influenced to enter the drying cylinder. The outside cold air is isolated by the fan cover 3 of the dryer arranged at the front end of the parching cylinder 9 and can not enter the parching cylinder 9, negative pressure is formed in the parching cylinder 9 under the action of the middle-end moisture exhaust fan, and the drying effect is better under the negative pressure environment; the square box body 6 and the high-temperature flue gas conversion box 12 are connected through the high-temperature flue gas pipe 11, the high-temperature flue gas enters the high-temperature flue gas conversion box 12 through the high-temperature flue gas pipe 11 and then enters the drying cylinder 18 through the high-temperature flue gas connecting passages 22, the dryer fan cover 3, the square box body 6, the high-temperature flue gas conversion box 12, the moisture conversion box 13 and the discharging device 20 are sleeved outside the parching cylinder 9 and the drying cylinder 18 and are not rotated, only the parching cylinder 9 and the drying cylinder 18 are rotated, and the parching device, the scraping device and the scattering device are independently rotated and independently moved, so that mutual interference is avoided to the maximum extent, the materials are ensured to move towards the required direction, and the materials are prevented from being stuck to the wall; meanwhile, the materials can be dried to the maximum extent;
the materials fall into the drying cylinder 18 through the square material leakage holes 16, the materials move under the action of the guide plate 15 with the inclination angle, the materials are thrown off at high altitude under the action of the L-shaped lifting plate 26 with the inclination angle, in the process, the materials can be fully contacted with high-temperature smoke and dried, the generated moisture is discharged under the action of a moisture discharge fan connected with the tail end moisture discharge port 19, and the materials are discharged from the discharge port 21.
The bottom of the square box body 6 is provided with a dust removing opening 8, the dust removing opening 8 is arranged, so that workers can conveniently and timely clean dust in the square box body 6, and uniform heat supply of the square box body 6 to the frying cylinder 9 is guaranteed.
To sum up, the frying and drying sections of the present disclosure are integrated, the frying section is provided with a frying device and a scraping device, the middle of the two sections is provided with a middle moisture outlet 14 and a high temperature flue gas pipe 11 for passing the high temperature flue gas into the drying cylinder. The dried high-temperature flue gas directly enters the drying cylinder 18 through the high-temperature flue gas conversion box 12 to dry the materials entering the drying cylinder 18, and a large amount of moisture evaporated in the frying section is discharged in advance through the moisture conversion box 13 in front of the drying cylinder 18, so that the moisture is prevented from entering the drying cylinder 18, and the drying efficiency is improved; the high-temperature flame is directly sprayed to the wall of the parching cylinder 9 through the burner connector 7 to rapidly heat up, so that the drying efficiency is high, the heat loss is small, the drying cost is low, and the production is carried out in the northern winter; the biomass granular fuel is adopted as a heat source, so that the fuel cost is low, and the environmental protection requirement is met; the flame of the biomass burner is directly sprayed on the wall of the parching cylinder 9, the wall of the parching cylinder 9 is heated, and then the high-temperature flue gas is directly introduced into the drying cylinder 18 at the rear end, so that the heat efficiency is high; the stir-frying section is provided with a stir-frying device and a scraping device, materials adhered to the wall of the drying drum are automatically cleaned, a large amount of moisture evaporated by the stir-frying section is discharged before entering the drying drum 18, the moisture is prevented from entering the drying drum 18, and the drying effect of the drying drum 18 is ensured.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications therefrom are within the scope of the utility model.
Claims (8)
1. The utility model provides a two segmentation drying-machines of viscidity material which characterized in that includes:
a parching section and a drying section downstream of the parching section;
the stir-drying section is provided with a stir-drying cylinder (9), the stir-drying cylinder (9) is internally provided with a scraping device and a stir-frying device, and a middle-end moisture discharging device is arranged between the stir-drying section and the drying section.
2. The two-stage dryer for viscous materials of claim 1 wherein said fry-dry stage comprises:
the square box body (6) is placed on the external frame, and the wall of the square box body (6) is provided with a burner connecting port (7);
the frying cylinder (9) is positioned inside the square box body (6), and a discharge end of the frying cylinder (9) is provided with a square material leakage hole (16) and at least one moisture connecting channel (23);
the dryer fan cover (3), the dryer fan cover (3) is sleeved at the feed end of the frying cylinder (9);
an auger type feeder (1), wherein the auger type feeder (1) is positioned at the feeding end of the frying cylinder (9).
3. The two-stage dryer for viscous materials of claim 2, wherein the middle moisture removing device comprises:
the high-temperature flue gas conversion box (12) and the moisture conversion box (13) adjacent to the high-temperature flue gas conversion box (12), the high-temperature flue gas conversion box (12) and the moisture conversion box (13) are placed on an external frame and sleeved on the outer side of the frying cylinder (9), the moisture conversion box (13) is communicated with the moisture connecting channel (23), the moisture conversion box (13) is provided with a middle-end moisture discharging port (14), and the wall of the high-temperature flue gas conversion box (12) is provided with a plurality of high-temperature flue gas connecting channels (22);
the high-temperature flue gas inlet pipe (11), the one end of high-temperature flue gas inlet pipe (11) is in stir-fry dry section of thick bamboo (9) and the cavity between square box (6), and the other end is in high-temperature flue gas transfer box (12), and high-temperature flue gas is through a plurality of high-temperature flue gas connecting channel (22) enters into in the stoving section of thick bamboo (18).
4. The two-stage dryer for viscous materials of claim 1, wherein the scraping means comprises: the frying device comprises a scraping shaft (2) and scraping plates (10) arranged on the circumferential side of the scraping shaft (2), wherein one end of the scraping shaft (2) is connected with an external motor, and the scraping plates (10) are attached to the inner wall of a frying cylinder (9);
the stir-frying device comprises a stir-frying shaft (4) and a stir-frying plate (28) arranged on the circumferential side of the stir-frying shaft (4), one end of the stir-frying shaft (4) is connected with an external motor, the stir-frying shaft (4) is positioned below the inner wall of the stir-frying cylinder (9), the scraping shaft (2) is positioned above the inner wall of the stir-frying cylinder (9), and the axial lines of the stir-frying shaft (4) and the scraping shaft (2) are parallel to the axial line of the stir-frying cylinder (9).
5. The two-stage dryer for viscous materials of claim 2, wherein the drying stage comprises:
the drying cylinder (18), the drying cylinder (18) is sleeved at the discharge end of the frying cylinder (9);
the L-shaped material raising plate (26), the L-shaped material raising plate (26) is fixedly arranged on the inner wall of the drying cylinder (18);
the material guide plate (15), the material guide plate (15) is arranged on the inner wall of the drying cylinder (18) and is positioned at the discharge end of the frying cylinder (9);
the discharging device (20) is sleeved on the discharging end of the drying drum (18) and placed on the outer frame, a discharging hole (21) is formed in the bottom of the discharging device (20), and a tail-end moisture discharging hole (19) is formed in the top of the discharging device (20).
6. Two-stage dryer for viscous materials, according to claim 2, characterized in that the bottom of the square box (6) has a dust-cleaning opening (8).
7. The two-stage dryer for viscous materials of claim 2 further comprising a breaker, said breaker comprising: a breaking shaft (29), wherein one end of the breaking shaft (29) is connected with an external motor, and the breaking shaft (29) is positioned below the auger type feeder (1);
the loosening blade is fixedly arranged at the other end of the loosening shaft (29) and is positioned at a discharge port below the auger type feeder (1).
8. Two-stage dryer for viscous materials according to claim 2, characterized in that the discharge end of the fry-dry drum (9) is provided with a wind deflector (27).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121905729.5U CN216132200U (en) | 2021-08-15 | 2021-08-15 | Two-section dryer for viscous material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121905729.5U CN216132200U (en) | 2021-08-15 | 2021-08-15 | Two-section dryer for viscous material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216132200U true CN216132200U (en) | 2022-03-25 |
Family
ID=80769987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121905729.5U Expired - Fee Related CN216132200U (en) | 2021-08-15 | 2021-08-15 | Two-section dryer for viscous material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216132200U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115077221A (en) * | 2022-06-10 | 2022-09-20 | 樊文华 | Ore raw materials safety drying equipment that ore processing was used |
-
2021
- 2021-08-15 CN CN202121905729.5U patent/CN216132200U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115077221A (en) * | 2022-06-10 | 2022-09-20 | 樊文华 | Ore raw materials safety drying equipment that ore processing was used |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104791767B (en) | Biomass particle burner and use method thereof | |
| CN102703121A (en) | Biomass gas generation system | |
| CN204593362U (en) | A kind of biomass particle burning machine | |
| CN106678778B (en) | A kind of efficient cyclone environment-protection boiler | |
| CN216132200U (en) | Two-section dryer for viscous material | |
| CN115704650A (en) | Two-section dryer for viscous material | |
| CN112066361A (en) | Wet dust-removing energy-saving coal-fired boiler | |
| CN212058178U (en) | Drum type three-section dryer suitable for straw crushed aggregates and fungus bag waste material boxes | |
| CN202430176U (en) | Biomass gas generating system | |
| CN104720080B (en) | A kind of new-type nut drying machine | |
| KR101223068B1 (en) | A incinerate stove | |
| CN208108065U (en) | A kind of environment-friendly high-efficiency water circulating biological matter particle burning machine | |
| CN205138112U (en) | Just drying equipment is raiseeed to rotation ecology | |
| CN204599282U (en) | A kind of new-type nut drying machine | |
| CN207828093U (en) | A kind of mud drying device | |
| CN207555584U (en) | A kind of high efficient combustion device of solid fuel | |
| CN216204874U (en) | Box cylinder negative pressure indirect dryer | |
| CN215893091U (en) | Drying equipment is used in fluorite particle processing | |
| CN217423260U (en) | Abundant useless pyrolysis treatment device admittedly burns | |
| CN214948977U (en) | Environment-friendly energy-saving biomass fuel boiler | |
| CN215808604U (en) | Pretreatment device of combustion system | |
| CN215757160U (en) | Fallen leaf pyrolysis box | |
| CN113758184A (en) | Box cylinder negative pressure indirect dryer | |
| CN221035759U (en) | Garbage incinerator with flue gas treatment system | |
| CN220892555U (en) | Short flame type energy-saving hot-blast stove |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220325 |