CN221099304U - Raw material dehumidifying equipment for glass production - Google Patents
Raw material dehumidifying equipment for glass production Download PDFInfo
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- CN221099304U CN221099304U CN202322393218.5U CN202322393218U CN221099304U CN 221099304 U CN221099304 U CN 221099304U CN 202322393218 U CN202322393218 U CN 202322393218U CN 221099304 U CN221099304 U CN 221099304U
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- 239000011521 glass Substances 0.000 title claims abstract description 53
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 35
- 239000002994 raw material Substances 0.000 title claims abstract description 30
- 230000007246 mechanism Effects 0.000 claims abstract description 12
- 230000005540 biological transmission Effects 0.000 claims abstract description 7
- 238000007790 scraping Methods 0.000 claims abstract description 7
- 238000007789 sealing Methods 0.000 claims description 9
- 230000002093 peripheral effect Effects 0.000 claims description 6
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052810 boron oxide Inorganic materials 0.000 abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 23
- 238000007599 discharging Methods 0.000 description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 239000003546 flue gas Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 5
- 229910052796 boron Inorganic materials 0.000 description 5
- 238000007791 dehumidification Methods 0.000 description 5
- 239000000428 dust Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000000712 assembly Effects 0.000 description 2
- 238000000429 assembly Methods 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- 239000005388 borosilicate glass Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000010006 flight Effects 0.000 description 2
- 239000006066 glass batch Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910011255 B2O3 Inorganic materials 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000005391 art glass Substances 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- RSCACTKJFSTWPV-UHFFFAOYSA-N disodium;3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane;pentahydrate Chemical compound O.O.O.O.O.[Na+].[Na+].O1B([O-])OB2OB([O-])OB1O2 RSCACTKJFSTWPV-UHFFFAOYSA-N 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- VGTPKLINSHNZRD-UHFFFAOYSA-N oxoborinic acid Chemical compound OB=O VGTPKLINSHNZRD-UHFFFAOYSA-N 0.000 description 1
- 230000005622 photoelectricity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses raw material dehumidifying equipment for glass production, which comprises a cylinder, a supporting component and a driving mechanism, wherein the cylinder is arranged on the cylinder; one end of the cylinder is provided with an air inlet and a feed inlet, the other end of the cylinder is provided with a discharge hole, and the inner wall of the cylinder is provided with a scraping plate; the supporting component is used for supporting the cylinder body and the cylinder body can rotate around the axis of the supporting component; the driving mechanism is in transmission connection with the cylinder body to drive the cylinder body to rotate. The raw material dehumidifying equipment for glass production provided by the utility model can effectively reduce the water content of the batch in the glass production, thereby being beneficial to reducing the discharge of boron oxide in the glass production and reducing the waste of raw materials.
Description
Technical Field
The utility model relates to the technical field of glass production equipment, in particular to raw material dehumidification equipment for glass production.
Background
The boron oxide (B 2O3) has the functions of increasing the low-temperature viscosity and reducing the high-temperature viscosity of glass, and has very high heat absorption coefficient and mass absorption coefficient, and the high-middle-low borosilicate glass can be produced by adding boron element (borax pentahydrate) in glass production, so that the glass has excellent chemical stability, lower heat expansion coefficient and good mechanical property, and has been widely applied to the fields of precision photoelectricity and medical glass tube control bottles.
However, the volatilization of B 2O3 and B 2O3 is easy to cause the volatilization of B 2O3 due to the high temperature in the glass melting furnace in the glass production, so that a large amount of raw materials are consumed, the quality of the glass is reduced, the furnace is greatly corroded, the service life of the furnace is shortened, boron oxide (boron oxide) is discharged into the environment along with flue gas, and boric acid generated by the reaction of boron oxide and water in the air causes acid rain, so that the environment is polluted. Secondly, due to the chemical characteristics of the boron oxide, a great amount of volatilized boron oxide and mixtures thereof are contained in the flue gas discharged by the kiln, and the problems of adhesion, blockage and the like are formed on a flue gas path due to the fact that the boron oxide can exist in solid, liquid and gas at different temperatures, so that the normal operation of flue gas treatment equipment is seriously influenced, and the stability of the kiln pressure is influenced to a certain extent. A large amount of B 2O3 contained in the flue gas can cause the flue gas dew point to be higher, the phenomenon of dew condensation is easy to generate, the conditions of residual adhesion of the inner wall of a flue, bag pasting of a dust collector bag and the like can be caused in the middle section and the tail section of the environment-friendly dust collection system, and finally the standard emission is influenced.
Boride in the glass melting furnace flue gas is derived from the added borax raw material, the content of B 2O3 in the medium-high boron glass batch is more than or equal to 47.50, the melting point of boron oxide is 450 ℃, the boron oxide is easy to volatilize at low temperature, and the conversion of boric acid into boride is a gradual dehydration process along with the temperature rise. Under the high temperature of 1500 ℃ of the glass melting furnace, the volatilization rate of B 2O3 in the glass batch is 8.9-12.78%, so B 2O3 becomes the source of boride in the flue gas of the glass melting furnace.
According to the research, water vapor in (Wenzel J T,Sanders D M.Sodium and boron vaporization from a boric oxide and a borosilicate glass melt【J】.Physics and chemistry of Glass,1982,23(2):47-53.), flue gas is easy to generate metaboric acid with liquid B 2O3, so that volatilization of boron is promoted, the volatilization amount of boron is proportional to the partial pressure of water vapor, so that the higher the water content of the batch is, the higher the partial pressure of water vapor in melting is, and the volatilization amount of B 2O3 is also higher, namely, the reduction of the water content in raw materials is an effective means for reducing the boron oxide content of the flue gas.
According to the important point, the dehumidification equipment provided by the invention pretreats raw materials (a plurality of process factors (J) influencing volatilization of boron oxide when glass such as Qiandaxing is melted; building materials journal, 1998,1 (2); 197-200), and reduces the volatilization amount (50% of the total amount of the existing boron oxide) of the glass melting furnace B 2O3 by reducing the water content of the raw materials, so that the concentration of boride in discharged flue gas is reduced from the source.
Disclosure of utility model
The application aims to solve the technical problems that: the water content of the batch is higher in the current glass production process, so that the utilization rate of raw materials is low, and a glass kiln is easy to erode.
The utility model provides raw material dehumidifying equipment for glass production, which can effectively reduce the water content of batch materials in glass production.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
A raw material dehumidifying apparatus for glass production includes a cylinder, a support assembly, and a driving mechanism. One end of the cylinder is provided with an air inlet and a feed inlet, the other end of the cylinder is provided with a discharge hole, and the inner wall of the cylinder is provided with a scraping plate; the supporting component is used for supporting the cylinder body and the cylinder body can rotate around the axis of the supporting component; the driving mechanism is in transmission connection with the cylinder body to drive the cylinder body to rotate.
In some embodiments, the number of flights is a plurality, the plurality of flights being distributed in an annular array about the axis of the barrel.
In some embodiments, the cross section of the flight is arcuate.
In some embodiments, the axis of the barrel is at an angle to the horizontal such that the end of the barrel with the discharge port is lower than the end of the barrel with the feed port.
In some embodiments, the feed port is located on a sidewall of the barrel.
In some embodiments, the support assembly comprises a first roller, a second roller and a support seat, wherein the first roller, the second roller and the support seat are positioned below the cylinder, the support seat is fixed with the ground, the first roller and the second roller are both rotationally connected with the support seat and are respectively positioned on two sides of the vertical shaft section of the cylinder, and the peripheral wall of the cylinder is tangential to the first roller and the second roller at the same time.
In some embodiments, the drum has a tread on its peripheral wall, and the first roller and the second roller are both tangential to the tread.
In some embodiments, the number of support assemblies is two, wherein one support assembly is used for supporting one end of the cylinder body adjacent to the air inlet, and the other support assembly is used for supporting one end of the cylinder body adjacent to the discharge hole.
In some embodiments, the driving mechanism comprises a gear motor, a gear set and a gear ring, wherein the gear ring is sleeved on the cylinder, the gear motor is fixed on the ground and is in transmission connection with the gear set, and the gear set is meshed with the gear ring.
In some embodiments, the raw material dehumidifying device for glass production further comprises a discharging box and a sealing ring, wherein a cavity is formed in the discharging box, a discharging opening communicated with the cavity is formed in the lower end of the discharging box, the discharging opening is communicated with the cavity, and the sealing ring is arranged between the cylinder and the discharging box to achieve sealing between the cylinder and the discharging box.
Compared with the prior art, the raw material dehumidifying equipment for glass production provided by the utility model can effectively reduce the water content of batch materials in glass production, thereby being beneficial to reducing the discharge of boron oxide in glass production and reducing the waste of raw materials, improving the quality of glass, prolonging the service life of a glass kiln and reducing the equipment and operation cost.
Drawings
In order to more clearly illustrate the embodiments of the utility model or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, it being obvious that the drawings in the following description are only some embodiments of the utility model, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a front view of an embodiment of the present utility model;
FIG. 2 is a right side view of an embodiment of the present utility model;
FIG. 3 is a cross-sectional view taken along line A-A of FIG. 1;
FIG. 4 is a cross-sectional view taken along line B-B in FIG. 1;
FIG. 5 is a schematic view of a prior art glass production process;
FIG. 6 is a schematic view of a glass production process optimized using an embodiment of the present utility model.
The reference numerals are explained as follows:
In the figure: 1. a cylinder; 11. an air inlet; 12. a feed inlet; 13. a discharge port; 14. a scraper; 15. a wheel belt; 2. a support assembly; 21. a first roller; 22. a second roller; 23. a support base; 3. a driving mechanism; 31. a speed reducing motor; 32. a gear set; 33. a gear ring; 4. a seal ring; 5. discharging boxes; 51. a feed opening; 52. an air outlet; 100. mixing equipment; 200. a kiln feeder; 300. a glass kiln; 400. a dehumidifying device.
Detailed Description
Embodiments of the present application are described in further detail below with reference to the accompanying drawings and examples. The following detailed description of the embodiments and the accompanying drawings are provided to illustrate the principles of the application and are not intended to limit the scope of the application, which may be embodied in many different forms and not limited to the specific embodiments disclosed herein, but rather to include all technical solutions falling within the scope of the claims.
These embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the application to those skilled in the art. It should be noted that: the relative arrangement of parts and steps, the composition of materials, numerical expressions and numerical values set forth in these embodiments should be construed as exemplary only and not limiting unless otherwise specifically stated.
In the description of the present application, unless otherwise indicated, the meaning of "plurality of" means greater than or equal to two; the terms "upper," "lower," "left," "right," "inner," "outer," and the like are merely used for convenience in describing the present application and to simplify the description, and do not denote or imply that the devices or elements referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus are not to be construed as limiting the present application. When the absolute position of the object to be described is changed, the relative positional relationship may be changed accordingly.
Furthermore, the use of the terms first, second, and the like in the present application are not used for any order, quantity, or importance, but rather are used for distinguishing between different parts. The "vertical" is not strictly vertical but is within the allowable error range. "parallel" is not strictly parallel but is within the tolerance of the error. The word "comprising" or "comprises" and the like means that elements preceding the word encompass the elements recited after the word, and not exclude the possibility of also encompassing other elements.
It should also be noted that, in the description of the present application, unless explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be directly connected or indirectly connected through an intermediate medium. The specific meaning of the above terms in the present application can be understood as appropriate by those of ordinary skill in the art. When a particular device is described as being located between a first device and a second device, there may or may not be an intervening device between the particular device and either the first device or the second device.
All terms used herein have the same meaning as understood by one of ordinary skill in the art to which the present application pertains, unless specifically defined otherwise. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
Techniques, methods, and apparatus known to one of ordinary skill in the relevant art may not be discussed in detail, but where appropriate, the techniques, methods, and apparatus should be considered part of the specification.
Referring to fig. 1 to 4, the present utility model provides a raw material dehumidifying apparatus 400 for glass production, which includes a cylinder 1, a support assembly 2, and a driving mechanism 3. One end of the cylinder body 1 is provided with an air inlet 11 and a feed inlet 12, the other end of the cylinder body 1 is provided with a discharge hole 13, and the inner wall of the cylinder body 1 is provided with a scraping plate 14; the support component 2 is used for supporting the cylinder 1, and the cylinder 1 can rotate around the axis of the support component; the driving mechanism 3 is in transmission connection with the cylinder 1 to drive the cylinder 1 to rotate.
As shown in fig. 1, the air inlet 11 and the feed inlet 12 are arranged at the left end of the cylinder 1, the discharge outlet 13 is arranged at the right end of the cylinder 1, and the feed inlet 12 is positioned on the side wall of the cylinder 1. In order to facilitate the flow of the high temperature air flow in the cylinder 1, an air inlet 11 is provided on the end face of the left end of the cylinder 1. The discharge gate 13 sets up on the terminal surface of barrel 1 right-hand member, in order that the material after the drying flows from discharge gate 13 constantly, designs the shape of discharge gate 13 into circular, and the diameter of discharge gate 13 equals with the internal diameter of barrel 1 right-hand member.
When the material dryer is used, firstly, a material to be dried is added into the cylinder body 1 from the feed inlet 12, then high-temperature gas is introduced into the cylinder body 1 from the air inlet 11 and drives the cylinder body 1 to rotate by the driving mechanism 3, the material is continuously lifted by the scraping plate 14 in the rotating process of the cylinder body 1, and the fallen material forms a material curtain state, so that the material is fully contacted with high-temperature airflow, and the material is more easily dehydrated and dried. In addition, the material continuously moves rightwards under the action of high-temperature air flow in the falling process, so that the transverse movement of the material is realized, and the material is finally discharged from the discharge hole 13.
As shown in fig. 3 and 4, the number of the squeegees 14 is 12, and 12 squeegees 14 are distributed in an annular array around the axis of the cylinder 1. In some embodiments, the number of the scrapers 14 may be other, the number of the scrapers 14 may be determined according to the inner diameter of the cylinder 1, and in order to make the dehumidifying apparatus have a preferable dehumidifying effect, the number of the scrapers 14 is not limited. As shown in fig. 4, the cross section of the scraper 14 is arc-shaped, and in the clockwise rotation process of the cylinder 1, the arc-shaped scraper 14 can carry the material to a higher position, so that the falling time of the material can be prolonged, and the dehumidification effect can be improved.
In the utility model, a certain included angle is formed between the axis of the cylinder 1 and the horizontal plane, so that one end of the cylinder 1 provided with the discharge hole 13 is lower than one end of the cylinder 1 provided with the feed hole 12, namely, the right end of the cylinder 1 is lower than the left end of the cylinder 1 in fig. 1. The scraping plate 14 fixed on the inner wall of the cylinder body 1 has the same gradient as the cylinder body 1, and the cylinder body 1 accelerates the rightward movement of the material in the rotating process, thereby being beneficial to improving the efficiency of the dehumidification equipment.
As shown in fig. 4, the support assembly 2 comprises a first roller 21, a second roller 22 and a support seat 23 which are positioned below the cylinder 1, the support seat 23 is fixed with the ground, the first roller 21 and the second roller 22 are both rotatably connected with the support seat 23 and are respectively positioned at two sides of the vertical axis section of the cylinder 1, and the peripheral wall of the cylinder 1 is tangential to the first roller 21 and the second roller 22 at the same time. The wheel belt 15 is arranged on the peripheral wall of the cylinder body 1, the first roller 21 and the second roller 22 are tangential to the wheel belt 15, the arranged wheel belt 15 can prevent the cylinder body 1 from being worn, the service life of lifting equipment is prolonged, and the wheel belt 15 is easy to replace when worn seriously, so that the maintenance cost is reduced. As shown in fig. 1, the number of the support assemblies 2 is two, wherein one support assembly 2 is used for supporting one end of the cylinder 1 adjacent to the air inlet 11, and the other support assembly 2 is used for supporting one end of the cylinder 1 adjacent to the discharge hole 13.
In the utility model, the driving mechanism 3 comprises a gear motor 31, a gear set 32 and a gear ring 33, wherein the gear ring 33 is sleeved on the cylinder body 1, the gear motor 31 is fixed on the ground and is in transmission connection with the gear set 32, and the gear set 32 is meshed with the gear ring 33.
In the utility model, the raw material dehumidifying equipment for glass production further comprises a discharging box 5 and a sealing ring 4, wherein a cavity is formed in the discharging box 5, a discharging opening 51 communicated with the cavity is formed in the lower end of the discharging box 5, a discharging opening 13 is communicated with the cavity, the sealing ring 4 is arranged between the cylinder 1 and the discharging box 5 to realize sealing between the cylinder 1 and the discharging box 5, and the arranged sealing ring 4 can prevent materials from leaking from a gap between the cylinder 1 and the discharging box 5. In order to enable the high-temperature gas to smoothly flow in the cylinder 1, an air outlet 52 is provided on the right end surface of the blanking box 5, and the air outlet 52 is located opposite to the air inlet 11.
Fig. 5 is a schematic view of a conventional glass production process, and fig. 6 is a schematic view of a glass production process optimized by the aforementioned dehumidifying apparatus 400. As shown in fig. 6, the dehumidifying apparatus 400 of the present utility model is added between the mixing apparatus 100 and the kiln charging apparatus, after the mixing of the existing mixing apparatus 100 is finished, the material is conveyed to the feed inlet 12 of the dehumidifying apparatus 400 by a conveyor, the dehumidifying apparatus 400 operates in a continuous mode, after the material enters the cylinder 1 to reach a certain weight, the dehumidifying apparatus 400 starts drying and dehumidifying the material, after a period of time, the material moves to the discharge inlet 51 under the rotation conduction of the cylinder 1, the dried material is fed into the kiln charger 200, and finally enters the glass kiln 300.
After the dehumidification equipment provided by the utility model is utilized to optimize the existing glass production process, the following beneficial effects can be achieved:
1. The boron oxide discharge is reduced, and the discharge is ensured to reach the standard;
2. The volatilization of B 2O3 in the glass kiln is effectively reduced, the product quality is improved, and the waste of raw materials is reduced;
3. The erosion to the glass kiln is reduced, the service life of the glass kiln is prolonged, and the equipment and operation cost is reduced;
4. Protecting equipment, pipelines and dust collection systems, and prolonging the service life and the integrity rate of the equipment;
5. The labor cost is reduced, and personal injury and occupational hazard possibly occurring in the process of cleaning the flue due to frequent replacement of the dust collector cloth bag are avoided.
Thus, various embodiments of the present application have been described in detail. In order to avoid obscuring the concepts of the application, some details known in the art have not been described. How to implement the solutions disclosed herein will be fully apparent to those skilled in the art from the above description.
While certain specific embodiments of the application have been described in detail by way of example, it will be appreciated by those skilled in the art that the above examples are for illustration only and are not intended to limit the scope of the application. It will be understood by those skilled in the art that the foregoing embodiments may be modified and equivalents substituted for elements thereof without departing from the scope and spirit of the application. In particular, the technical features mentioned in the respective embodiments may be combined in any manner as long as there is no structural conflict.
Claims (10)
1. A raw material dehumidifying apparatus for glass production, comprising:
The device comprises a barrel body (1), wherein an air inlet (11) and a feed inlet (12) are formed in one end of the barrel body (1), a discharge hole (13) is formed in the other end of the barrel body (1), and a scraping plate (14) is arranged on the inner wall of the barrel body (1);
the support assembly (2) is used for supporting the cylinder (1) and the cylinder (1) can rotate around the axis of the support assembly (2);
the driving mechanism (3) is in transmission connection with the cylinder body (1) to drive the cylinder body (1) to rotate.
2. The raw material dehumidifying apparatus for glass production according to claim 1, wherein: the number of the scrapers (14) is a plurality, and the plurality of the scrapers (14) are distributed in an annular array around the axis of the cylinder (1).
3. The raw material dehumidifying apparatus for glass production according to claim 2, wherein: the cross section of the scraping plate (14) is arc-shaped.
4. The raw material dehumidifying apparatus for glass production according to claim 1, wherein: the axis of the cylinder body (1) has a certain included angle with the horizontal plane, so that one end of the cylinder body (1) provided with the discharge hole (13) is lower than one end of the cylinder body (1) provided with the feed inlet (12).
5. The raw material dehumidifying apparatus for glass production according to claim 1, wherein: the feed inlet (12) is positioned on the side wall of the cylinder (1).
6. The raw material dehumidifying apparatus for glass production according to claim 1, wherein: the support assembly (2) comprises a first roller (21), a second roller (22) and a support seat (23) which are arranged below the cylinder body (1), the support seat (23) is fixed with the ground, the first roller (21) and the second roller (22) are both rotationally connected with the support seat (23) and are respectively arranged on two sides of the vertical shaft section of the cylinder body (1), and the peripheral wall of the cylinder body (1) is simultaneously tangent with the first roller (21) and the second roller (22).
7. The raw material dehumidifying apparatus for glass production according to claim 6, wherein: the outer peripheral wall of the cylinder body (1) is provided with a belt (15), and the first roller (21) and the second roller (22) are tangential to the belt (15).
8. The raw material dehumidifying apparatus for glass production according to claim 7, wherein: the number of the supporting components (2) is two, one supporting component (2) is used for supporting one end, close to the air inlet (11), of the cylinder body (1), and the other supporting component (2) is used for supporting one end, close to the discharge hole (13), of the cylinder body (1).
9. The raw material dehumidifying apparatus for glass production according to claim 1, wherein: the driving mechanism (3) comprises a gear motor (31), a gear set (32) and a gear ring (33), wherein the gear ring (33) is sleeved on the cylinder body (1), the gear motor (31) is fixed on the ground and is in transmission connection with the gear set (32), and the gear set (32) is meshed with the gear ring (33).
10. The raw material dehumidifying apparatus for glass production according to any one of claims 1 to 9, wherein: still include unloading case (5) and sealing washer (4), the inside of unloading case (5) is equipped with the cavity, the lower extreme of unloading case (5) be equipped with feed opening (51) of cavity intercommunication, discharge gate (13) with the cavity intercommunication, sealing washer (4) are established barrel (1) with between unloading case (5) in order to realize barrel (1) with seal between the unloading case (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322393218.5U CN221099304U (en) | 2023-09-04 | 2023-09-04 | Raw material dehumidifying equipment for glass production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322393218.5U CN221099304U (en) | 2023-09-04 | 2023-09-04 | Raw material dehumidifying equipment for glass production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221099304U true CN221099304U (en) | 2024-06-07 |
Family
ID=91320032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322393218.5U Active CN221099304U (en) | 2023-09-04 | 2023-09-04 | Raw material dehumidifying equipment for glass production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221099304U (en) |
-
2023
- 2023-09-04 CN CN202322393218.5U patent/CN221099304U/en active Active
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