CN202683100U - Continuous mixer combining spilling method and driving-reversing supply method - Google Patents
Continuous mixer combining spilling method and driving-reversing supply method Download PDFInfo
- Publication number
- CN202683100U CN202683100U CN 201220354966 CN201220354966U CN202683100U CN 202683100 U CN202683100 U CN 202683100U CN 201220354966 CN201220354966 CN 201220354966 CN 201220354966 U CN201220354966 U CN 201220354966U CN 202683100 U CN202683100 U CN 202683100U
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- main shaft
- cylindrical shell
- supply method
- advance
- agitator
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Abstract
The utility model discloses a continuous mixer combining a spilling method and a driving-reversing supply method. An output shaft of a driving unit is connected to a main shaft through a coupler; stirrers are arranged on the main shaft; a feed inlet, a discharge port and a cleaning port are formed on a cylinder; the inside of the cylinder is provided with a flow baffle; the stirrer is a coulter which is fixed inside a fixing groove in the main shaft; two sets of the stirrers are distributed in the axial and radial directions of the main shaft vertically and adjacently; each set of stirrers are parallelly distributed at two sides of the main shaft uniformly; the ends of the coulters are in swallow-tail shape; and the end faces of the coulters have certain radian. A forwarding face and a receding face are formed on each coulter; the flow baffle has a semi-circular structure and is arranged on one side of the discharge port in the cylinder; the flow baffle has an adjustable telescopic structure, can adjust the angle according to the material nature and material direction; and by adoption of a design of a coulter structure and a flow baffle structure, the continuous mixer combines the driving-reversing supply method and the spilling method, and is high in mixing efficiency, high in stability and wide in application.
Description
Technical field
The utility model relates to a kind of mixer, relates in particular to a kind of out-of-stream method and advance and retreat supply method mating type continuous mixing machine, belongs to the hybrid technology field.
Background technology
Domestic continuous mixer commonly used is long stroke type to be mixed, do not demonstrate fully the diffusion ratio of mixed material, in the mixer of long stroke type, usually select pusher agitator, it follows the material elder generation discharging that is introduced into mixer, can't join mixed with the material of hysteresis certain hour, the range of scatter that has determined thus material is smaller, the material of some points can't spread alternately with large-scale material, its diffusion ratio is very little, so such as the relatively more awkward degree of this class water content of mud, unlike mud, also unlike loosening the soil, there is not mobile and agglomerating material and powder ground ginseng mixed, make it that powder is more difficult to be diffused among the mud uniformly, the material of any when often causing sampling, powder content is high especially, and certain any material does not contain powder material substantially, in addition the continuous mixer of long stroke then, its amount of fill can't be kept weighing apparatus, different mixed materials can present different amount of fill, has larger difficulty on the again lectotype selection size, if its amount of fill is too high, just there is not unnecessary stirring space, can't mix uniformly, the too low effective diffusion that can't guarantee again material of amount of fill, and do not form the action effect of high yield.
Summary of the invention
In order to solve problems of the prior art and deficiency, the utility model provides a kind of out-of-stream method and advance and retreat supply method mating type continuous mixing machine, realize that out-of-stream method is combined hybrid mode with the supply method of advancing and retreat, mixing efficiency is high, good stability, surpass and automatically overflow after 50%-60% is fully loaded with, the Treatment of Sludge that can be used for the sewage treatment plant in city, conversion mud is fertilizer, the dirt ash that can be used for after thermal power plant and steel mill burn solidifies processing, also can be used for processing non-sintering and lay bricks, build the production of easily building plate, substitute fired brick and waste reclamation.
The purpose of this utility model realizes by the following technical solutions
Out-of-stream method and advance and retreat supply method mating type continuous mixing machine, comprise the driving group on the structure, support, cylindrical shell, main shaft, the mixer support, agitator, charging aperture, discharging opening and flow-stopping plate, the driving group is arranged on the support, whole device is fixed on the mixer support, driving group output shaft is connected to main shaft by shaft coupling, be provided with protective cover on the shaft coupling, the main shaft two ends are provided with bearing block and seal member, be provided with agitator on the main shaft, the cylindrical shell upper end is provided with charging aperture, and the lower end is provided with discharging opening, be provided with flow-stopping plate in the cylindrical shell, the cylindrical shell side is provided with the clean-up port.
Described driving group is made of main stirrer-driven machine, reductor.
Described main shaft, its two ends are placed in the bearing on the spindle bearing holder, and main shaft and cylindrical shell junction be provided with seal member, are provided with the colter holddown groove on it.
Described cylindrical shell, its both sides are provided with wallboard, and cylindrical shell is fixed on the wallboard, is provided with the rotary-cut fly cutter on the cylindrical shell medial surface, during work, external rotary-cut fly cutter motor.
Described agitator adopts colter, is fixed in the holddown groove on the main shaft, and agitator has two groups, two groups of adjacent Vertical Uniforms of agitator be distributed in main shaft axially and radially, every group of parallel main shaft both sides that are uniformly distributed in.
Described colter, end are swallow-tail form, and end face has certain radian, are formed with on the colter into face and move back face, can realize shearing fast the shunting material, realize that advancing less of material move back more, and advance and retreat equate, fewly advance to move back more.
Described flow-stopping plate is semicircular structure, and its bottom surface and side contact with cylindrical shell, be arranged at discharging opening one side in the cylindrical shell, be adjustable telescopic formula structure, consisted of by two baffle plates that baffle plate one is placed in the baffle plate two, two baffle plates are fixed by the flange spiral, baffle plate one can carry out the adjustment of angle according to the character of material and the direction of material, and it highly reaches 50%～60% of cylindrical shell height, in case material is higher than the flow-stopping plate height, can automatically overflow, ensureing in the cylinder has 50%～60% inserts.
The utility model adopts the design of colter structure and flow-stopping plate structure, has realized respectively advance and retreat supply method and the out-of-stream method hybrid mode of material.
The utility model adopts adjustable flow-stopping plate, hinder the interlude of material first in first out, make and keep balanced fill level in the cylindrical shell, flow-stopping plate has guaranteed to have in the equipment amount of fill of 50%-60%, mix minute structure of the similar colter of streamed rather than unidirectional pusher form, guaranteed that certain any material can carry out diffusion with material in the whole cylinder, the stirring blade of plough coulter type is sheared the shunting material fast, axially and radially acting on simultaneously material, can mix fast the material on the gang plough cutter track, the discharging of out-of-stream method mud continuous mixer is to follow the mode of automatically overflowing after fully loaded above 50%-60%, the material basic guarantee of inner barrel such as the mixed effect of batch mixer, cooperate the tube structure form, effectively realized lignin-sludge and the powder of continuous uniform, powder and powder, the mixing of powder liquid feeding.
Description of drawings
Fig. 1 is the utility model one example structure schematic diagram
Fig. 2 is the utility model colter rotation status schematic diagram
Fig. 3 is the utility model colter structural representation
Fig. 4 is another angle structural representation of Fig. 3
Among the figure: 1-driving group, 2-shaft coupling, 3-protective cover, 4-bearing block, 5-seal member, 6-charging aperture, the 7-cylindrical shell, 8-agitator, 9-clean-up port, 10-main shaft, 11, the 15-wallboard, 12-discharging opening, the 13-support, 14-mixer support, the 16-flow-stopping plate, 81-advances face, and 82-moves back face, the 83-arc.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further described
Such as Fig. 1, embodiment illustrated in fig. 2, out-of-stream method and advance and retreat supply method mating type continuous mixing machine, comprise the driving group on the structure, support, cylindrical shell, main shaft, the mixer support, agitator, charging aperture, discharging opening and flow-stopping plate, the driving group is arranged on the support, whole device is fixed on the mixer support, driving group output shaft is connected to main shaft by shaft coupling, is provided with protective cover on the shaft coupling, is provided with protective cover on the shaft coupling, the main shaft two ends are provided with bearing block and seal member, be provided with agitator on the main shaft, the cylindrical shell upper end is provided with charging aperture, and the lower end is provided with discharging opening, be provided with flow-stopping plate in the cylindrical shell, the cylindrical shell side is provided with the clean-up port.
Further, described driving group is made of main stirrer-driven machine, reductor.
Further, described main shaft, its two ends are placed in the bearing on the spindle bearing holder, and main shaft and cylindrical shell junction be provided with seal member, are provided with the colter holddown groove on it.
Further, described cylindrical shell, its both sides are provided with wallboard, and cylindrical shell is fixed on the wallboard, is provided with the rotary-cut fly cutter on the cylindrical shell medial surface, during work, external rotary-cut fly cutter motor.
Described agitator adopts colter, is fixed in the holddown groove on the main shaft, and agitator has two groups, two groups of adjacent Vertical Uniforms of agitator be distributed in main shaft axially and radially, every group of parallel main shaft both sides that are uniformly distributed in.
Further, see Fig. 3, embodiment illustrated in fig. 4, described colter, the end is swallow-tail form, end face is arc, and certain radian is arranged, and is formed with into face on the colter and moves back face, selectively excellent, the face of moving back is arcwall face, can realize shearing fast the shunting material, and advancing less of material of realization moves back more, advance and retreat equate, lack to advance to move back more.
Described flow-stopping plate is semicircular structure, and bottom surface and both sides contact with cylindrical shell, be arranged at discharging opening one side in the cylindrical shell, be adjustable telescopic formula structure, consisted of by two baffle plates that baffle plate one is placed in the baffle plate two, two baffle plates are fixed by the flange spiral, baffle plate one can carry out the adjustment of angle according to the character of material and the direction of material, and it highly reaches 50%～60% of cylindrical shell height, in case material is higher than the flow-stopping plate height, can automatically overflow, ensureing in the cylinder has 50%～60% inserts.
The utility model adopts the design of colter structure and flow-stopping plate structure, has realized respectively advance and retreat supply method and the out-of-stream method hybrid mode of material.
The utility model adopts adjustable flow-stopping plate, hinder the interlude of material first in first out, make and keep balanced fill level in the cylindrical shell, flow-stopping plate has guaranteed to have in the equipment amount of fill of 50%-60%, mix minute structure of the similar colter of streamed rather than unidirectional pusher form, guaranteed that certain any material can carry out diffusion with material in the whole cylinder, the stirring blade of plough coulter type is sheared the shunting material fast, axially and radially acting on simultaneously material, can mix fast the material on the gang plough cutter track, the discharging of out-of-stream method mud continuous mixer is to follow the mode of automatically overflowing after fully loaded above 50%-60%, the material basic guarantee of inner barrel such as the mixed effect of batch mixer, cooperate the tube structure form, effectively realized lignin-sludge and the powder of continuous uniform, powder and powder, the mixing of powder liquid feeding.
Claims (6)
1. out-of-stream method and advance and retreat supply method mating type continuous mixing machine, comprise the driving group on the structure, support, cylindrical shell, main shaft, the mixer support, agitator, charging aperture, discharging opening, the driving group is arranged on the support, whole device is fixed on the mixer support, driving group output shaft is connected to main shaft by shaft coupling, be provided with protective cover on the shaft coupling, the main shaft two ends are provided with bearing block and seal member, are provided with agitator on the main shaft, the cylindrical shell upper end is provided with charging aperture, the lower end is provided with discharging opening, and the cylindrical shell side is provided with the clean-up port, it is characterized in that, also comprise flow-stopping plate on the structure, be provided with flow-stopping plate in the cylindrical shell.
2. out-of-stream method according to claim 1 and advance and retreat supply method mating type continuous mixing machine, it is characterized in that, described main shaft, its two ends are placed in the bearing on the spindle bearing holder, and main shaft and cylindrical shell junction are provided with seal member, are provided with the colter holddown groove on it.
3. out-of-stream method according to claim 1 and advance and retreat supply method mating type continuous mixing machine is characterized in that described cylindrical shell, its both sides are provided with wallboard, cylindrical shell is fixed on the wallboard, is provided with the rotary-cut fly cutter on the cylindrical shell medial surface, the external rotary-cut fly cutter of rotary-cut fly cutter motor.
4. out-of-stream method according to claim 1 and advance and retreat supply method mating type continuous mixing machine, it is characterized in that, described agitator, adopt colter, be fixed in the holddown groove on the main shaft, agitator has two groups, two groups of adjacent Vertical Uniforms of agitator be distributed in main shaft axially and radially, every group of parallel main shaft both sides that are uniformly distributed in.
According to claim 1 with 4 described out-of-stream methods and advance and retreat supply method mating type continuous mixing machine, it is characterized in that, described colter, the end is swallow-tail form, end face has certain radian, is formed with into face on the colter and moves back face.
6. out-of-stream method according to claim 1 and advance and retreat supply method mating type continuous mixing machine, it is characterized in that, described flow-stopping plate is semicircular structure, and its bottom surface and side contact with cylindrical shell, be arranged at discharging opening one side in the cylindrical shell, be adjustable telescopic formula structure, consisted of by two baffle plates that baffle plate one is placed in the baffle plate two, two baffle plates are fixed by the flange spiral, and it highly reaches 50%～60% of cylindrical shell height.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220354966 CN202683100U (en) | 2012-07-20 | 2012-07-20 | Continuous mixer combining spilling method and driving-reversing supply method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220354966 CN202683100U (en) | 2012-07-20 | 2012-07-20 | Continuous mixer combining spilling method and driving-reversing supply method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202683100U true CN202683100U (en) | 2013-01-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220354966 Expired - Fee Related CN202683100U (en) | 2012-07-20 | 2012-07-20 | Continuous mixer combining spilling method and driving-reversing supply method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202683100U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104997144A (en) * | 2015-08-26 | 2015-10-28 | 通威股份有限公司 | Production technology of oreochromis mossambicus granulated feed |
| CN108114626A (en) * | 2018-01-08 | 2018-06-05 | 重庆大学 | A kind of batch mixer for improving sinter granulation consistency |
| CN111892464A (en) * | 2020-08-14 | 2020-11-06 | 北京京煤化工有限公司 | Continuous production line and continuous production method for emulsified ammonium nitrate fuel oil explosive |
-
2012
- 2012-07-20 CN CN 201220354966 patent/CN202683100U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104997144A (en) * | 2015-08-26 | 2015-10-28 | 通威股份有限公司 | Production technology of oreochromis mossambicus granulated feed |
| CN108114626A (en) * | 2018-01-08 | 2018-06-05 | 重庆大学 | A kind of batch mixer for improving sinter granulation consistency |
| CN108114626B (en) * | 2018-01-08 | 2021-02-02 | 重庆大学 | Mixer for improving granulating uniformity of sinter |
| CN111892464A (en) * | 2020-08-14 | 2020-11-06 | 北京京煤化工有限公司 | Continuous production line and continuous production method for emulsified ammonium nitrate fuel oil explosive |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130123 Termination date: 20210720 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |