CN212006462U - Drying stirrer for producing benzenediol - Google Patents
Drying stirrer for producing benzenediol Download PDFInfo
- Publication number
- CN212006462U CN212006462U CN202020523760.1U CN202020523760U CN212006462U CN 212006462 U CN212006462 U CN 212006462U CN 202020523760 U CN202020523760 U CN 202020523760U CN 212006462 U CN212006462 U CN 212006462U
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- CN
- China
- Prior art keywords
- connecting rod
- shell
- motor
- support frame
- drying
- 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
- 238000001035 drying Methods 0.000 title claims abstract description 28
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 title abstract description 11
- 238000003756 stirring Methods 0.000 claims abstract description 43
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000000741 silica gel Substances 0.000 claims abstract description 19
- 229910002027 silica gel Inorganic materials 0.000 claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 claims description 31
- 239000002274 desiccant Substances 0.000 claims description 14
- 229910003460 diamond Inorganic materials 0.000 claims 1
- 239000010432 diamond Substances 0.000 claims 1
- 230000008859 change Effects 0.000 abstract description 2
- 238000003466 welding Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 14
- 238000007789 sealing Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 150000005208 1,4-dihydroxybenzenes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Silicon Compounds (AREA)
Abstract
The utility model discloses a drying stirrer is used in benzenediol production, including support frame, first motor, second motor, silica gel drier and overlap joint piece, the right side fixed mounting of support frame has the baffle, and the inboard movable mounting of baffle has a brace table, the fixed axle that is provided with in side of support frame top, and the outside fixed mounting who links the axle has the bearing to the fixed shell that is provided with in outside of bearing, the top bolt fastening of shell has first motor, and the fixed connecting rod that is provided with in below of first motor to the surface welding of connecting rod is connected with the stirring leaf, outside fixed mounting in the middle of the connecting rod has the disc, and the left and right sides of disc is all fixed and is provided with the stirring rod. This drying agitator is used in benzenediol production conveniently adjusts the stirring mode, vertically and transversely stir simultaneously and turn, can change inside silica gel drier and clear up the device is inside through wholly dismantling the device simultaneously.
Description
Technical Field
The utility model relates to a hydroquinone production technical field specifically is a drying agitator is used in hydroquinone production.
Background
The hydroquinone is a white crystalline chemical organic matter, has wide application, can be used for manufacturing medicines, can also be used for producing dyes, electroplating materials and the like, is one of important raw materials in chemical industry, and needs to use a drying stirrer to dry the hydroquinone during the production of the hydroquinone.
Some drying stirrers for hydroquinone production on the market today:
(1) the existing drying device usually performs drying in the production process of hydroquinone, and after the production is finished, the produced hydroquinone is inconvenient to perform secondary drying work due to different air humidity in different areas;
(2) the existing drying equipment usually turns over the materials inside the device through heating and rotation to dry when drying, so that the drying effect is poor, and meanwhile, the inside of the device is not convenient to clean.
Therefore, we have proposed a drying agitator for hydroquinone production in order to solve the problems set forth above.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a drying stirrer is used in benzenediol production to some benzenediol drying device on the existing market that solve above-mentioned background art and provide is not convenient for clear up inside, the relatively poor problem of drying effect moreover.
In order to achieve the above object, the utility model provides a following technical scheme: a drying stirrer for producing benzenediol comprises a support frame, a first motor, a second motor, a silica gel drying agent and a lapping block, wherein a baffle is fixedly arranged on the right side of the support frame, a support table is movably arranged on the inner side of the baffle, a connecting shaft is fixedly arranged on the side face above the support frame, a bearing is fixedly arranged on the outer side of the connecting shaft, a shell is fixedly arranged on the outer side of the bearing, the first motor is fixed on the top of the shell through a bolt, a connecting rod is fixedly arranged below the first motor, a stirring blade is connected to the surface of the connecting rod in a welding manner, a disc is fixedly arranged on the outer side of the middle of the connecting rod, stirring rods are fixedly arranged on the left side and the right side of the disc, net boxes are fixedly arranged on the left side and the right side of the inner part of the shell through bolts, a sealing groove is formed in the middle of each net box, and the front end fixedly connected with connecting rod of second motor, the outside laminating of connecting rod is provided with the outer liner, and is fixed connection between outer liner and the shell, the inside packing of net box is provided with the silica gel drier, the surface welded connection of shell has the overlap joint piece.
Preferably, the support frame is L-shaped in appearance, the baffles are symmetrically fixed on the front side and the rear side of the support frame, and the outer surfaces of the baffles and the outer surface of the support table are mutually attached.
Preferably, the shell forms a detachable structure with an adjacent shell through a bolt and an overlapping block, the upper part and the lower part of the shell are both internally hollow hemispheroids, and the middle part of the shell is an internally hollow cylinder.
Preferably, the lengths of the stirring blades from the upper side and the lower side of the connecting rod to the middle of the connecting rod are increased progressively, the stirring blades are distributed on the surface of the connecting rod at equal intervals, and the stirring rods are symmetrically distributed on the left side and the right side of the connecting rod.
Preferably, the disc runs through in the inside of net box through the seal groove, and the net box is the surrounding type structure in the inside of shell, the upper and lower both ends of stirring rod are the arc.
Preferably, the connecting rod runs through in the inside of outer bush, and the outer wall of connecting rod and the inner wall of outer bush laminate mutually to the shape of connecting rod longitudinal section is the rhombus, the second motor passes through to constitute detachable construction between connecting rod and outer bush and the shell.
Compared with the prior art, the beneficial effects of the utility model are that: this hydroquinone production is with dry agitator:
(1) the device is provided with a stirring and turning mechanism capable of rotating longitudinally and transversely simultaneously, the first motor drives the stirring blades to stir the input materials, the stirring rod stirs the drying agent inside while stirring the materials, and the disc is matched with the rubber pad on the outer wall of the sealing groove to seal the net box, so that the materials and the drying agent can be mixed, and the drying and stirring effects of the device on the materials are improved;
(2) also can come to demolish the second motor through the telescopic link of device below to only transversely mix, promoted the variety that the device used, can come to dismantle the device is whole through the overlap joint piece in addition, because the silica gel drier meets water can grow, consequently can determine whether change the drier through observing the inside degree of hugging closely of drier, conveniently clear up inside simultaneously, promoted the result of use of device.
Drawings
FIG. 1 is a schematic front sectional view of the present invention;
FIG. 2 is a schematic view of the structure at A in FIG. 1 according to the present invention;
FIG. 3 is a schematic front view of the present invention;
FIG. 4 is a schematic view of a sectional view of the support frame of the present invention;
FIG. 5 is a schematic view of the connection structure of the disc and the stirring rod of the present invention;
FIG. 6 is a schematic cross-sectional view of the net box of the present invention;
fig. 7 is a schematic side sectional view of the outer liner of the present invention.
In the figure: 1. a support frame; 2. a baffle plate; 3. a support table; 4. a connecting shaft; 5. a bearing; 6. a housing; 7. a first motor; 8. a connecting rod; 9. stirring blades; 10. a disc; 11. a stirring rod; 12. a net box; 13. sealing the groove; 14. an inner tank; 15. a second motor; 16. a connecting rod; 17. an outer liner; 18. a silica gel desiccant; 19. and a lapping block.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-7, the present invention provides a technical solution: a drying stirrer for producing benzenediol comprises a support frame 1, a baffle 2, a support table 3, a connecting shaft 4, a bearing 5, a shell 6, a first motor 7, a connecting rod 8, a stirring blade 9, a disc 10, a stirring rod 11, a net box 12, a sealing groove 13, an inner groove 14, a second motor 15, a connecting rod 16, an outer bushing 17, a silica gel drying agent 18 and a lap joint block 19, wherein the baffle 2 is fixedly arranged on the right side of the support frame 1, the support table 3 is movably arranged on the inner side of the baffle 2, the connecting shaft 4 is fixedly arranged on the side surface above the support frame 1, the bearing 5 is fixedly arranged on the outer side of the connecting shaft 4, the shell 6 is fixedly arranged on the outer side of the bearing 5, the first motor 7 is fixed on the top of the shell 6 through a bolt, the connecting rod 8 is fixedly arranged below the first motor 7, the stirring blade 9 is welded on the surface of the connecting rod 8, and the left and right sides of the disc 10 are all fixedly provided with stirring rods 11, the left and right sides inside the shell 6 are all bolted with net boxes 12, the middle of each net box 12 is provided with a sealing groove 13, an inner groove 14 is arranged above the supporting table 3, the inner part of the inner groove 14 is bolted with a second motor 15, the front end of the second motor 15 is fixedly connected with a connecting rod 16, the outer side of the connecting rod 16 is provided with an outer lining 17 in a laminating manner, the outer lining 17 is fixedly connected with the shell 6, the inside of the net box 12 is filled with a silica gel drying agent 18, and the surface of the shell 6 is welded with a lapping block 19.
The appearance of support frame 1 is "L" type, and both sides around support frame 1 are fixed to baffle 2 symmetry, and the surface of baffle 2 and the surface of brace table 3 laminate mutually, can decide whether to use second motor 15 through the telescopic link between support frame 1 and the brace table 3 to the mode of adjusting device stirring.
The shell 6 forms detachable structure with adjacent shell 6 through bolt and overlap joint piece 19 between, and the upper and lower two parts of shell 6 are inside hollow hemispheroid to the intermediate portion of shell 6 is inside hollow cylinder, comes to clear up the device inside and changes inside silica gel drier 18 through dismantling shell 6.
Stirring leaf 9 increases progressively from the upper and lower both sides of connecting rod 8 to the middle length of connecting rod 8, and stirring leaf 9 is at the equidistant distribution in the surface of connecting rod 8, and stirring rod 11 is the symmetrical form distribution in the left and right sides of connecting rod 8, and stirring leaf 9 can also stir silica gel drier 18 through stirring rod 11 when stirring the material to absorb water and dry the material better.
The disc 10 runs through the inside of net box 12 through sealing the groove 13, and net box 12 is the surrounding type structure in the inside of shell 6, stirs the upper and lower both ends of pole 11 and is the arc for stir pole 11 and be located the net box 12 inside centre all the time when rotating, guaranteed the drying and the effect of absorbing water of device.
Connecting rod 16 runs through in the inside of outer liner 17, and the outer wall of connecting rod 16 and the inner wall of outer liner 17 laminate mutually, and the shape of connecting rod 16 longitudinal section is the rhombus, and second motor 15 passes through to constitute detachable construction between connecting rod 16 and outer liner 17 and the shell 6, and the position through adjusting second motor 15 makes the device only turn the material through inside stirring leaf 9, conveniently adjusts the user mode of device, has promoted the result of use of device.
The working principle is as follows: when the drying stirrer for producing the benzenediol is used, as shown in fig. 1-4, when the device is used, the position of the supporting table 3 on the inner side of the baffle 2 can be adjusted by adjusting the telescopic rod between the supporting frame 1 and the supporting table 3, the telescopic rod is extended to enable the supporting table 3 to move rightwards (as shown in fig. 4), the connecting rod 16 at the front end of the second motor 15 is separated from the inner part of the outer bushing 17, so that when the device is used, the connecting rod 8 and the stirring blade 9 are driven by the first motor 7 to turn over materials in the outer shell 6, the telescopic rod can be adjusted to the state in fig. 1, the whole shell 6 can rotate longitudinally, the turning effect of the materials in the device is improved, the materials are fully contacted with the silica gel drying agent 18 in the mesh box 12, water absorption and drying work are carried out through the silica gel drying agent 18, it is required that the meshes of the mesh box 12 are smaller than the size, the silica gel drying agent 18 is prevented from leaking out of the meshes of the net box 12, and as the benzenediol is in a granular shape with a small volume, when the device is actually produced and manufactured, the size of the meshes of the net box 12 needs to be adjusted to be larger than the volume of the benzenediol and smaller than the size of the silica gel drying agent 18, so that the silica gel drying agent 18 can be prevented from leaking out of the net box 12 while the materials are fully contacted with the silica gel drying agent 18;
as shown in fig. 1-3 and 5-7, when the connecting rod 8 rotates, the stirring rods 11 at the left and right sides of the disk 10 in the middle of the connecting rod 8 can turn over the silica gel desiccant 18 in the net box 12, so as to further improve the water absorption effect of the silica gel desiccant 18 on the materials, as can be seen from fig. 1 and 6, the sealing gaskets at the upper and lower sides of the sealing groove 13 are matched with the disk 10, the silica gel drying agent 18 can not leak from the middle of the net box 12, the shells 6 at the left side and the right side are finally disassembled through the lapping blocks 19 and the bolts, the net box 12 is disassembled through the bolts after the disassembly is finished to clean the inside of the shell 6 and replace the silica gel drying agent 18, for the next use, this is the working process of the whole device and the details not described in this specification are well known to those skilled in the art.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (6)
1. The utility model provides a hydroquinone production is with dry agitator, includes support frame (1), first motor (7), second motor (15), silica gel drier (18) and overlap joint piece (19), its characterized in that: the right side of the support frame (1) is fixedly provided with a baffle (2), the inner side of the baffle (2) is movably provided with a support table (3), the side surface above the support frame (1) is fixedly provided with a connecting shaft (4), the outer side of the connecting shaft (4) is fixedly provided with a bearing (5), the outer side of the bearing (5) is fixedly provided with a shell (6), the top of the shell (6) is fixed with a first motor (7) through a bolt, the lower part of the first motor (7) is fixedly provided with a connecting rod (8), the surface of the connecting rod (8) is welded and connected with a stirring blade (9), the outer side of the middle of the connecting rod (8) is fixedly provided with a disc (10), the left side and the right side of the disc (10) are both fixedly provided with stirring rods (11), the left side and the right side of the inner part of the shell (6) are both fixed with net boxes (12), an inner groove (14) is formed in the upper portion of the supporting table (3), a second motor (15) is fixed to the inner portion of the inner groove (14) through bolts, a connecting rod (16) is fixedly connected to the front end of the second motor (15), an outer lining (17) is attached to the outer side of the connecting rod (16), the outer lining (17) and the shell (6) are fixedly connected, a silica gel drying agent (18) is filled in the net box (12), and a lapping block (19) is welded to the surface of the shell (6).
2. The drying agitator for producing hydroquinone as set forth in claim 1, wherein: the appearance of support frame (1) is "L" type, both sides around support frame (1) are fixed to baffle (2) symmetry, and the surface of baffle (2) and the surface of brace table (3) are laminated mutually.
3. The drying agitator for producing hydroquinone as set forth in claim 1, wherein: the shell (6) forms a detachable structure with the adjacent shell (6) through bolts and the overlapping blocks (19), the upper part and the lower part of the shell (6) are both internally hollow hemispheroids, and the middle part of the shell (6) is an internally hollow cylinder.
4. The drying agitator for producing hydroquinone as set forth in claim 1, wherein: the length of the stirring blades (9) from the upper side and the lower side of the connecting rod (8) to the middle of the connecting rod (8) is increased progressively, the stirring blades (9) are distributed on the surface of the connecting rod (8) at equal intervals, and the stirring rods (11) are symmetrically distributed on the left side and the right side of the connecting rod (8).
5. The drying agitator for producing hydroquinone as set forth in claim 1, wherein: the disc (10) penetrates through the inside of the net box (12) through the seal groove (13), the net box (12) is of a surrounding structure in the shell (6), and the upper end and the lower end of the stirring rod (11) are both arc-shaped.
6. The drying agitator for producing hydroquinone as set forth in claim 1, wherein: the connecting rod (16) penetrates through the inner part of the outer bushing (17), the outer wall of the connecting rod (16) is attached to the inner wall of the outer bushing (17), the longitudinal section of the connecting rod (16) is in a diamond shape, and the second motor (15) forms a detachable structure with the shell (6) through the connecting rod (16) and the outer bushing (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020523760.1U CN212006462U (en) | 2020-04-11 | 2020-04-11 | Drying stirrer for producing benzenediol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020523760.1U CN212006462U (en) | 2020-04-11 | 2020-04-11 | Drying stirrer for producing benzenediol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212006462U true CN212006462U (en) | 2020-11-24 |
Family
ID=73413548
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020523760.1U Expired - Fee Related CN212006462U (en) | 2020-04-11 | 2020-04-11 | Drying stirrer for producing benzenediol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212006462U (en) |
-
2020
- 2020-04-11 CN CN202020523760.1U patent/CN212006462U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20201124 |