CN204401353U - A kind of sediment pot of HC Cleaner - Google Patents
A kind of sediment pot of HC Cleaner Download PDFInfo
- Publication number
- CN204401353U CN204401353U CN201420861850.6U CN201420861850U CN204401353U CN 204401353 U CN204401353 U CN 204401353U CN 201420861850 U CN201420861850 U CN 201420861850U CN 204401353 U CN204401353 U CN 204401353U
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- Prior art keywords
- tank body
- blocking
- communicated
- middle tank
- slurry
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Links
- 239000013049 sediment Substances 0.000 title claims abstract description 24
- 239000002002 slurry Substances 0.000 claims abstract description 26
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000002893 slag Substances 0.000 abstract description 15
- 239000000835 fiber Substances 0.000 abstract description 13
- 239000012535 impurity Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 238000000746 purification Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 208000004141 microcephaly Diseases 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a kind of sediment pot of HC Cleaner, comprise tank body, described tank body is by upper tank body, middle tank body and lower tank composition, the lower end of upper tank body is communicated with the upper end of middle tank body, the lower end of middle tank body is communicated with the upper end of lower tank, described upper tank body is eccentric reducer, described middle tank body is straight tube, described lower tank is straight tube, Concentric Reducers or eccentric reducer, the inclined outside faces of described upper tank body is provided with turbulent flow transmitting tube, the vertical lateral surface of described middle tank body is provided with the anti-blocking slurry be communicated with middle tank interior and eluriates water pipe and anti-blocking balancing pipeline, described anti-blocking balancing pipeline is arranged on the below that water pipe eluriated by anti-blocking slurry.The utility model can be avoided accumulated slag and reduce fiber loss, ensures the running rate of equipment, increases the whole service life of equipment.
Description
Technical field
The utility model belongs to slurry purification equipment technical field, particularly relates to a kind of sediment pot of HC Cleaner.
Background technology
HC Cleaner is used to remove the various heavy seeds such as the larger metal of proportion in paper pulp, sand at higher concentrations, to obtain a kind of ideal equipment of high-quality slurry, is also the necessary equipment of waste paper pulp-making purification.HC Cleaner utilize fiber different from impurity proportion come removing impurities.Slurry enters High Rotation Speed after scummer with certain pressure by charging threeway tangent line, and due to the difference of centrifugal force, heavy seeds is thrown toward wall, under gravity, gradually runs to the cone end, enters sediment pot.Fiber is less due to centrifugal force, runs gradually to center low-pressure area, and after arriving bottom, vortex rises, and is finally discharged by good slurry mouth.The cone of HC Cleaner has certain taper, and cone is longer, and slurry radius of turn in cone reduces gradually, avoids slurry stream to reduce at rotary course medium velocity, ensures that centrifugal force is strengthened, thus improve the purification efficiency of paper stock.Equilibrium water, bottom pressure, slightly larger than slurry pressure, makes fiber not enter sediment pot, only has the heavy seeds such as sand grains, metallic particles, blob of viscose, plastics to sink in tank, decrease fiber loss.
Existing HC Cleaner sediment pot is made as and is divided into straight tube form and Concentric Reducers form two kinds, straight tube form there will not be slag inclusion, but caliber is too little, the volume little storage time is short, slide valve switch shortens too frequent service life, proximity switch is fragile, and the too large valve aperture of caliber needs corresponding increase, and input cost is too large.Though Concentric Reducers form can increase sediment pot volume, but slag easily forms accumulated slag at barrel place, reducing position after overlong time, long-time will cause sediment pot entirety blocking, and rotate decline slag blanket do not obtain effective fluid turbulent interference, and make a large amount of acceptable fiber run off strengthen.
Utility model content
The utility model, in order to solve the problems of the prior art, provides a kind of sediment pot of HC Cleaner, can avoid accumulated slag and reduce fiber loss, ensureing the running rate of equipment, increasing the whole service life of equipment.
For solving the problems of the technologies described above, the utility model adopts following technical scheme: a kind of sediment pot of HC Cleaner, comprise tank body, described tank body is by upper tank body, middle tank body and lower tank composition, the lower end of upper tank body is communicated with the upper end of middle tank body, the lower end of middle tank body is communicated with the upper end of lower tank, described upper tank body is eccentric reducer, described middle tank body is straight tube, described lower tank is straight tube, Concentric Reducers or eccentric reducer, the inclined outside faces of described upper tank body is provided with turbulent flow transmitting tube, the vertical lateral surface of described middle tank body is provided with the anti-blocking slurry be communicated with middle tank interior and eluriates water pipe and anti-blocking balancing pipeline, described anti-blocking balancing pipeline is arranged on the below that water pipe eluriated by anti-blocking slurry.
Described turbulent flow transmitting tube is vertical with the inclined outside faces of described upper tank body.
The upper end of described upper tank body is provided with upper flange, and the lower end of lower tank is provided with lower flange.
Described anti-blocking balancing pipeline is provided with two, and two anti-blocking balancing pipelines are symmetricly set on middle tank body.
Described middle tank body is provided with mirror device.
The beneficial effects of the utility model: in the utility model, tank body is made up of upper tank body, middle tank body and lower tank, the lower end of upper tank body is communicated with the upper end of middle tank body, the lower end of middle tank body is communicated with the upper end of lower tank, middle tank body is straight tube, described lower tank is straight tube, Concentric Reducers or eccentric reducer, this structural design is convenient to directly transform existing equipment, reduces the direct input cost of equipment; Anti-blocking slurry is eluriated water pipe and is ensured that equipment is when normally running, and rinses well slurry and is fully separated with impurity, and prevents impurity from blocking sediment pot; Turbulent flow transmitting tube injects current makes water form turbulent flow at the obliquity place of eccentric reducer, is beneficial to being separated of slurry and impurity; Anti-blocking balancing pipeline ensures the hydraulic pressure in sediment pot bottom, makes slurry act on float downward in equilibrium water to the top of sediment pot, prevents stock losses; Upper tank body is eccentric reducer, increases the actual volume of tank body, effectively reduces valve switch number of times, extends the life-span of valve, increases the whole service life of equipment; The cooperation of water pipe eluriated by the eccentric reducer of upper tank body, turbulent flow transmitting tube and anti-blocking slurry, makes to there will not be accumulated slag phenomenon in sediment pot, avoids accumulated slag and reduces fiber loss, ensureing the running rate of equipment; Mirror device can clearly be seen that position and the screenings separation case of heavy slag, controls the pressure of deslagging time and the anti-blocking equilibrium water of adjustment, ensures utilization ratio and the equipment fiber loss rate of slide valve valve; Anti-blocking balancing pipeline is provided with two, and two anti-blocking balancing pipelines are symmetricly set on middle tank body, ensure that the stable of the middle tank body lower part hydraulic pressure of sediment pot; The upper end of upper tank body is provided with upper flange, and upper flange is for installing feed pipe, and the lower end of lower tank is provided with lower flange, and lower flange is for installing heavy slag pipe.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment one;
Fig. 2 is the structural representation of the utility model embodiment two.
Detailed description of the invention
Embodiment one: as shown in Figure 1, the sediment pot of a kind of HC Cleaner of the present utility model, comprise tank body, described tank body is by upper tank body 3, middle tank body 9 and lower tank 8 form, the lower end of upper tank body 3 is communicated with the upper end of middle tank body 9, the lower end of middle tank body 9 is communicated with the upper end of lower tank 8, described upper tank body 3 is eccentric reducer, described middle tank body 9 is straight tube, described lower tank 8 is Concentric Reducers, the dead in line of the described axis of upper tank body 3 major part and the axis of middle tank body 9 and lower tank 8, the inclined outside faces of described upper tank body 3 is provided with turbulent flow transmitting tube 2, described turbulent flow transmitting tube 2 is vertical with the inclined outside faces of the eccentric reducer of upper tank body 3, the vertical lateral surface of described middle tank body 9 is provided with the anti-blocking slurry be communicated with middle tank body 9 inside and eluriates water pipe 4 and anti-blocking balancing pipeline 6, anti-blocking balancing pipeline 6 is arranged on the bottom of middle tank body 9, the top that water pipe 4 is arranged on middle tank body 9 eluriated by anti-blocking slurry, anti-blocking balancing pipeline 6 is provided with two, two anti-blocking balancing pipelines 6 are symmetricly set on middle tank body 9, the axis place of tank body in the water inlet direction sensing of water pipe 4 and anti-blocking balancing pipeline 6 eluriated by anti-blocking slurry.The upper end of described upper tank body 3 is provided with upper flange 1, and upper flange 1 is for installing feed pipe, and the lower end of lower tank 8 is provided with lower flange 7, and lower flange 7 is for installing heavy slag pipe.Described middle tank body 9 is also provided with mirror device 5, can clearly be seen that position and the screenings separation case of heavy slag, control the pressure of deslagging time and the anti-blocking equilibrium water of adjustment.
Embodiment two: as a kind of technical scheme comparatively optimized, the difference of this embodiment and embodiment one is, described lower tank 8 is eccentric reducer, the dead in line of the described axis of upper tank body 3 major part and the axis of middle tank body 9 and lower tank 8 major part, the axis of described upper tank body 3 microcephaly and the dead in line of lower tank 8 microcephaly, lower tank 8 adopts eccentric reducer, increase the actual volume of tank body, rotate the slag blanket declined and can obtain the interference of effective fluid turbulent, avoid a large amount of acceptable fiber is run off, and not easily occur accumulated slag phenomenon in sediment pot.
The utility model operationally, slurry enters High Rotation Speed after scummer with certain pressure by charging threeway tangent line, due to the difference of centrifugal force, heavy seeds is thrown toward wall, under gravity, gradually run to the cone end, slurry containing a large amount of heavy seeds and a small amount of fiber enters the upper tank body 3 of sediment pot, the turbulent flow transmitting tube 2 that the inclined outside faces of upper tank body 3 is arranged injects current in tank body, slurry forms turbulent flow at the obliquity place of upper tank body 3 under the effect of current, due to the difference of centrifugal force, heavy seeds is thrown toward vessel edge, under gravity, gradually run to tank base, anti-blocking slurry is eluriated water pipe 4 and inject current in tank body, and the Fiber wash on heavy seeds is clean and be fully separated with heavy seeds, anti-blocking balancing pipeline 6 injects current in tank body, and the hydraulic pressure arranging anti-blocking balancing pipeline 6 is greater than the hydraulic pressure of turbulent flow transmitting tube 2 and anti-blocking slurry elutriation water pipe 4, make the fiber in heavy seeds at the flow action float downward of anti-blocking balancing pipeline 6 to the top of tank body, prevent stock losses, heavy seeds falls to lower tank 8 under gravity always, discharges from heavy slag pipe.
Above embodiment is the unrestricted the technical solution of the utility model in order to explanation only, although be described in detail the utility model with reference to above-described embodiment, those of ordinary skill in the art is to be understood that: still can modify to the utility model or equivalent replacement, and not departing from any modification or partial replacement of spirit and scope of the present utility model, it all should be encompassed in the middle of right of the present utility model.
Claims (5)
1. the sediment pot of a HC Cleaner, comprise tank body, it is characterized in that: described tank body is by upper tank body, middle tank body and lower tank composition, the lower end of upper tank body is communicated with the upper end of middle tank body, the lower end of middle tank body is communicated with the upper end of lower tank, described upper tank body is eccentric reducer, described middle tank body is straight tube, described lower tank is straight tube, Concentric Reducers or eccentric reducer, the inclined outside faces of described upper tank body is provided with turbulent flow transmitting tube, the vertical lateral surface of described middle tank body is provided with the anti-blocking slurry be communicated with middle tank interior and eluriates water pipe and anti-blocking balancing pipeline, described anti-blocking balancing pipeline is arranged on the below that water pipe eluriated by anti-blocking slurry.
2. the sediment pot of HC Cleaner according to claim 1, is characterized in that: described turbulent flow transmitting tube is vertical with the inclined outside faces of described upper tank body.
3. the sediment pot of HC Cleaner according to claim 1 and 2, is characterized in that: the upper end of described upper tank body is provided with upper flange, and the lower end of lower tank is provided with lower flange.
4. the sediment pot of HC Cleaner according to claim 3, is characterized in that: described anti-blocking balancing pipeline is provided with two, and two anti-blocking balancing pipelines are symmetricly set on middle tank body.
5. the sediment pot of HC Cleaner according to claim 4, is characterized in that: described middle tank body is provided with mirror device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861850.6U CN204401353U (en) | 2014-12-31 | 2014-12-31 | A kind of sediment pot of HC Cleaner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861850.6U CN204401353U (en) | 2014-12-31 | 2014-12-31 | A kind of sediment pot of HC Cleaner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204401353U true CN204401353U (en) | 2015-06-17 |
Family
ID=53425229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420861850.6U Expired - Fee Related CN204401353U (en) | 2014-12-31 | 2014-12-31 | A kind of sediment pot of HC Cleaner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204401353U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109706554A (en) * | 2018-12-29 | 2019-05-03 | 江苏宝德新材料有限公司 | A kind of preparation method of high temperature resistant staple fiber |
-
2014
- 2014-12-31 CN CN201420861850.6U patent/CN204401353U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109706554A (en) * | 2018-12-29 | 2019-05-03 | 江苏宝德新材料有限公司 | A kind of preparation method of high temperature resistant staple fiber |
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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: 20150617 |