CN204471589U - A kind of kaolin is condensed into sizing device - Google Patents
A kind of kaolin is condensed into sizing device Download PDFInfo
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- CN204471589U CN204471589U CN201520005379.5U CN201520005379U CN204471589U CN 204471589 U CN204471589 U CN 204471589U CN 201520005379 U CN201520005379 U CN 201520005379U CN 204471589 U CN204471589 U CN 204471589U
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Abstract
A kind of kaolin of the utility model is condensed into sizing device, belongs to technical field of kaolin; The kaolin that a kind of solid content is high, pulping efficiency is high and effective is provided to be condensed into sizing device; A kind of kaolin is condensed into sizing device, kiln basin, delivery pump, filter press, broken cake spiral, finishing beater and mulser connect successively, described delivery pump plunger displacement pump, described finishing beater adopts vertical finishing beater, also has concentrated pulp storage tank between described finishing beater and mulser; The utility model is mainly used in kaolin aspect.
Description
Technical field
A kind of kaolin of the utility model is condensed into sizing device, belongs to technical field of kaolin.
Background technology
In order to ensure that the material after grinding has uniform size distribution in kaolin production process, for subsequent production provides qualified slurry, therefore need by being reconfigured as the slurries that solid content reduces after grinding is delaminated, classified horizontal screw machine under the influence of centrifugal force, the centrifugal force that the particle that in mud, proportion is larger is subject to is also large, rapid sedimentation can fall drum inner wall, be discharged outside body by screw feeder and enter underflow pond; Comparatively granule is then pressed against rotary drum center, discharges body and enters overflow pulp storage tank, more under the influence of centrifugal force the relatively fine particle in slip is separated through disk centrifuge, thus ensure that final material has uniform size distribution by overfall.But need material to have good mobility in the process of sleeping spiral shell classification and disk centrifuge separating slurry, and cause solid content low, need again the heat of at substantial when follow-up workshop section carries out spraying dry, therefore need press filtration to become cake, again with slurry.The height of solid content directly affects the consumption of spray-dired normal operation and output and heat, is therefore necessary to make improvements.
Utility model content
In order to overcome the deficiencies in the prior art, the kaolin that a kind of solid content is high, pulping efficiency is high and effective is provided to be condensed into sizing device.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of kaolin is condensed into sizing device, and kiln basin, delivery pump, filter press, broken cake spiral, finishing beater and mulser connect successively.
Described delivery pump plunger displacement pump.
Described finishing beater adopts vertical finishing beater.
Concentrated pulp storage tank is also had between described finishing beater and mulser.
Described vertical finishing beater comprises frame, axle, conveying worm, big belt pulley, small belt pulley, first motor and the second motor, described frame internal fixtion has bucket, described bucket top is provided with bung, described axle is vertically fixed, and bottom is placed in bucket, and by axle sleeve lock nut fixed hub, the described axle be placed in bucket is fixed with blade, axle between described bucket and frame is connected with flange coupling, described axle top is connected with bearing block, described bearing block is fixed in frame, and the axle of upper end is connected with big belt pulley, described axle top is provided with axle cap, the inside, left side of described bucket is fixed with conveying worm, described conveying worm connects with the first motor, described second motor top is connected with small belt pulley, described small belt pulley is connected by belt with big belt pulley.
Angular contact ball bearing and deep groove ball bearing is also provided with between described bearing block and axle.
Positioning shaft sleeve is provided with between described angular contact ball bearing and deep groove ball bearing.
Also outside framework oil seal is provided with between described angular contact ball bearing and frame.
Described bucket is spill.
Described axle is provided with two.
The beneficial effect that the utility model is compared with prior art had is:
The utility model novel structure, vertical finishing beater selected by finishing beater, and pulping efficiency is high, solid content is high, pulping is effective, is follow-up workshop section spraying dry, saves hear rate energy consumption.
Accompanying drawing explanation
Below by accompanying drawing, detailed description of the invention of the present utility model is described in further detail.
Fig. 1 is connection schematic diagram of the present utility model;
Fig. 2 is the structural representation of the vertical finishing beater of the utility model;
Fig. 3 is the side view of the vertical finishing beater of the utility model.
In figure, 1 is kiln basin, 2 is delivery pump, 3 is filter press, 4 is broken cake spiral, 5 is finishing beater, 6 is mulser, 7 is concentrated pulp storage tank, 8 is frame, 9 is axle, 10 is conveying worm, 11 is big belt pulley, 12 is small belt pulley, 13 is the first motor, 14 is bucket, 15 is bung, 16 is axle sleeve lock nut, 17 is axle sleeve, 18 is blade, 19 is flange coupling, 20 is bearing block, 21 is axle cap, 22 is the second motor, 23 is angular contact ball bearing, 24 is deep groove ball bearing, 25 is positioning shaft sleeve, 26 is outside framework oil seal.
Detailed description of the invention
The utility model will be further described by reference to the accompanying drawings for embodiment below.
As shown in Figure 1 to Figure 3, a kind of kaolin is condensed into sizing device, and kiln basin 1, delivery pump 2, filter press 3, broken cake spiral 4, finishing beater 5 and mulser 6 connect successively.
Described delivery pump 2 plunger displacement pump.
Described finishing beater 5 adopts vertical finishing beater.
Concentrated pulp storage tank 7 is also had between described finishing beater 5 and mulser 6.
Described vertical finishing beater comprises frame 8, axle 9, conveying worm 10, big belt pulley 11, small belt pulley 12, first motor 13 and the second motor 22, described frame 8 internal fixtion has bucket 14, described bucket 14 top is provided with bung 15, described axle 9 is vertically fixed, and bottom is placed in bucket 14, and by axle sleeve lock nut 16 fixed hub 17, the described axle 9 be placed in bucket 14 is fixed with blade 18, axle 9 between described bucket 14 and frame 8 is connected with flange coupling 19, described axle 9 top is connected with bearing block 20, described bearing block 20 is fixed in frame 8, and the axle 9 of upper end is connected with big belt pulley 11, described axle 9 top is provided with axle cap 21, the inside, left side of described bucket 14 is fixed with conveying worm 10, described conveying worm 10 connects with the first motor 13, described second motor 22 top is connected with small belt pulley 12, described small belt pulley 12 is connected by belt with big belt pulley 11.
Angular contact ball bearing 23 and deep groove ball bearing 24 is also provided with between described bearing block 20 and axle 9.
Positioning shaft sleeve 25 is provided with between described angular contact ball bearing 23 and deep groove ball bearing 24.
Outside framework oil seal 26 is also provided with between described angular contact ball bearing 23 and frame 8.
Described bucket 14 is in spill.
Described axle 9 is provided with two.
The height of solid content directly affects the consumption of spray-dired normal operation and output and heat.Solid content mainly regulates by control inflow and cake discharge speed, and when solid content is on the low side, by accelerating cake discharge speed, the water yield with slurry being reduced to pulp grinder regulates, otherwise on the contrary.
Plunger displacement pump two porcelain knob up-down alternative motion under the effect of hydraulic system, when porcelain knob moves upward, inlet valve opens outlet valve and cuts out, and convey materials enters in the pump housing; When porcelain knob moves downward, inlet valve cuts out outlet valve and opens, and convey materials is discharged in the pump housing, completes the conveying of material in the process of continuous back and forth movement.Plunger displacement pump is large discharge pumped (conveying) medium when low pressure, low discharge pumped (conveying) medium during high pressure.During use, unloader DA10 pressure can be adjusted to 4 ~ 6Mpa, overflow valve DB10 is adjusted to 6 ~ 8Mpa, during hydraulic work system, when pressure is no more than 4 ~ 6Mpa, double-united oil pump works simultaneously, flow rate of hydraulic system is large, and the jig frequency of plunger increases, and POF also increases; When pressure is more than 4 ~ 6Mpa, unloader off-load, an oil pump quits work, and gear pump output flow reduces, and the jig frequency of plunger displacement pump two plunger reduces, and the output flow of pump reduces, to reach instructions for use.
Operationally, in-oil cylinder piston promotes pressure strip to filter press, and compressed by the filter plate between pressure strip and thrust plate, filter plate and filter cloth form filter element one by one alternately, i.e. filter chamber.Slurries are under the promotion of plunger displacement pump, and the charging aperture on thrust plate enters in each filter chamber, and the pressure that slip produces by charging plunger displacement pump carries out Separation of Solid and Liquid, and due to the effect of filter cloth, solid is stayed in filter chamber and forms filter cake, filtrate is got rid of from water nozzle.Filter cake in filter chamber manually draws off, and the slurries being configured to certain solid content by entering finishing beater after broken cake spiral crushing supply next workshop section.
The utility model pulping is effective, and solid content is low, reduces costs.
Claims (10)
1. kaolin is condensed into a sizing device, it is characterized in that: kiln basin (1), delivery pump (2), filter press (3), broken cake spiral (4), finishing beater (5) and mulser (6) connect successively.
2. a kind of kaolin according to claim 1 is condensed into sizing device, it is characterized in that: described delivery pump (2) is plunger displacement pump.
3. a kind of kaolin according to claim 1 is condensed into sizing device, it is characterized in that: described finishing beater (5) adopts vertical finishing beater.
4. a kind of kaolin according to claim 1 is condensed into sizing device, it is characterized in that: also have concentrated pulp storage tank (7) between described finishing beater (5) and mulser (6).
5. a kind of kaolin according to claim 3 is condensed into sizing device, it is characterized in that: described vertical finishing beater comprises frame (8), axle (9), conveying worm (10), big belt pulley (11), small belt pulley (12), first motor (13) and the second motor (22), described frame (8) internal fixtion has bucket (14), described bucket (14) top is provided with bung (15), described axle (9) is vertically fixed, and bottom is placed in bucket (14), and by axle sleeve lock nut (16) fixed hub (17), the described axle (9) be placed in bucket (14) is fixed with blade (18), axle (9) between described bucket (14) and frame (8) is connected with flange coupling (19), described axle (9) top is connected with bearing block (20), described bearing block (20) is fixed in frame (8), and the axle of upper end (9) is connected with big belt pulley (11), described axle (9) top is provided with axle cap (21), the inside, left side of described bucket (14) is fixed with conveying worm (10), described conveying worm (10) connects with the first motor (13), described second motor (22) top is connected with small belt pulley (12), described small belt pulley (12) is connected by belt with big belt pulley (11).
6. a kind of kaolin according to claim 5 is condensed into sizing device, it is characterized in that: be also provided with angular contact ball bearing (23) and deep groove ball bearing (24) between described bearing block (20) and axle (9).
7. a kind of kaolin according to claim 6 is condensed into sizing device, it is characterized in that: be provided with positioning shaft sleeve (25) between described angular contact ball bearing (23) and deep groove ball bearing (24).
8. a kind of kaolin according to claim 6 is condensed into sizing device, it is characterized in that: be also provided with outside framework oil seal (26) between described angular contact ball bearing (23) and frame (8).
9. a kind of kaolin according to claim 5 is condensed into sizing device, it is characterized in that: described bucket (14) is in spill.
10. a kind of kaolin according to claim 5 is condensed into sizing device, it is characterized in that: described axle (9) is provided with two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520005379.5U CN204471589U (en) | 2015-01-06 | 2015-01-06 | A kind of kaolin is condensed into sizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520005379.5U CN204471589U (en) | 2015-01-06 | 2015-01-06 | A kind of kaolin is condensed into sizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204471589U true CN204471589U (en) | 2015-07-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520005379.5U Active CN204471589U (en) | 2015-01-06 | 2015-01-06 | A kind of kaolin is condensed into sizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204471589U (en) |
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2015
- 2015-01-06 CN CN201520005379.5U patent/CN204471589U/en active Active
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