CN205360818U - Precipitated white carbon black waste liquid sedimentation device - Google Patents
Precipitated white carbon black waste liquid sedimentation device Download PDFInfo
- Publication number
- CN205360818U CN205360818U CN201620007338.4U CN201620007338U CN205360818U CN 205360818 U CN205360818 U CN 205360818U CN 201620007338 U CN201620007338 U CN 201620007338U CN 205360818 U CN205360818 U CN 205360818U
- Authority
- CN
- China
- Prior art keywords
- pond
- ponds
- grades
- level
- overfall
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a precipitated white carbon black waste liquid sedimentation device, including the rectangle cell body, including one -level pond, second grade pond, tertiary pond, level four pond, pyatyi pond and six grades of ponds in the cell body, the inside baffle that all is equipped with in every pond, the inside filter equipment that all is equipped with in one -level pond and second grade pond is equipped with the overflow mouth on the lateral wall between every two adjacent ponds, is equipped with an iron wire cylinder mould on every overflow mouth position, the inside filter layer that is equipped with of iron wire cylinder mould. The utility model discloses simple structure, the operation of being convenient for, through establishing ties in six ponds, the waste liquid passes through baffle, overflow mouth inflow next stage pond from last one -level pond, and the iron wire cylinder mould that has a multiple -layer filtering layer on the filter equipment in one -level pond and the second grade pond and each overflow mouth position is isolated impurity and solid gradually, has obtained the waste liquid of the defecation at last, has reached fine sedimentation effect.
Description
Technical field
This utility model relates to a kind of settling separation device, particularly relates to a kind of precipitated silica waste liquid settling separation device.
Background technology
White carbon has another name called hydrated SiO 2, because of its have that particle diameter is little, specific surface area is big, a series of good characteristic such as high temperature resistant and stable chemical performance and have very wide application prospect, given play to the effect of its uniqueness in fields such as rubber, plastics, coating and papermaking.Current white carbon conventional production process mainly has vapor phase method and the sedimentation method, the method of the commonly used silicate of precipitated silica (being generally sodium silicate) and mineral acid (generally using sulphuric acid) neutralization-precipitation reaction is produced, after generating hydrated SiO 2 precipitation, according to finished product requirement, through filtering, washing the unnecessary moisture of removing and byproduct of reaction in roller pressure filter or plate pressure filter, obtain white carbon filter cake, obtain finished product then through dry.Waste liquid in production process does not often reach the standard of directly discharge, it is necessary to carry out settlement separate process.
Chinese patent CN20152001510104.9 discloses the settlement separate pond in a kind of carbon white production process, it adopts four pond series connection, sidewall between pond is gradually lowered, clear liquid is made to flow to next stage pond from upper level pond gradually, impurity and solid are gradually disengaged out, it settles than traditional pond that is used alone, and effect is much obvious.But its isolated filtrate does not also reach direct discharge standard sometimes.
Summary of the invention
The purpose of this utility model is to provide a kind of precipitated silica waste liquid settling separation device, and settlement separate effect is notable.
For achieving the above object, the technical solution of the utility model is as follows:
A kind of precipitated silica waste liquid settling separation device, including rectangle cell body, low-level culture pool, two grades of ponds, three grades of ponds, level Four pond, Pyatyi pond and six grades of ponds are included in described cell body, described low-level culture pool and two grades of ponds are set up in parallel, described three grades of ponds and level Four pond are set up in parallel, described Pyatyi pond and six grades of ponds are set up in parallel, described three grades of ponds are also set up in parallel with two grades of ponds, six grades of ponds respectively, described level Four pond is also set up in parallel with low-level culture pool, Pyatyi pond respectively, it is provided with the first defecator inside described low-level culture pool, inside described two grades of ponds, is provided with the second defecator；It is equipped with dividing plate inside the cell body in described low-level culture pool, two grades of ponds, three grades of ponds, level Four pond, Pyatyi pond and six grades of ponds；
Sidewall between described low-level culture pool and two grades of ponds is provided with overfall I, sidewall between described two grades of ponds and three grades of ponds is provided with overfall II, sidewall between described three grades of ponds and level Four pond is provided with overfall III, sidewall between described level Four pond and Pyatyi pond is provided with overfall IV, and the sidewall between described Pyatyi pond and six grades of ponds is provided with overfall V；
The position of described overfall I, overfall II, overfall III, overfall IV and overfall V is equipped with an iron wire cylinder mould, it is provided with filter course inside described iron wire cylinder mould, described filter course includes the cobblestone filter course, the first quartz sand filtration layer, the second quartz sand filtration layer and the 3rd quartz sand filtration layer that from top to bottom stack gradually, and the quartz sand particle size in described first quartz sand filtration layer, the second quartz sand filtration layer and the 3rd quartz sand filtration layer is sequentially reduced；
Described low-level culture pool is provided with inlet, and described six grades of ponds are provided with leakage fluid dram.
Preferably, described first defecator and the second defecator are filter cloth, filter screen or screen plate.
Preferably, the quartz sand particle size in described 3rd quartz sand filtration layer is 1～2mm.
This utility model simple in construction, it is easy to operation, it is together in series by six ponds, waste liquid flows into next stage pond from upper level pond by overfall, defecator in low-level culture pool and two grades of ponds and the iron wire cylinder mould with multiple layers of filters on each overfall position, it is gradually disengaged out by impurity and solid, has finally obtained the waste liquid of clarification, reached good settlement separate effect.
Accompanying drawing explanation
Fig. 1 is top view of the present utility model；
Fig. 2 is the structural representation of low-level culture pool in Fig. 1；
Fig. 3 is the structural representation of iron wire cylinder mould in Fig. 1.
In figure: 1 low-level culture pool；2 two grades of ponds；3 three grades of ponds；4 level Four ponds；5 Pyatyi ponds；6 six grades of ponds；7 first defecators；8 second defecators；9 overfalls I；10 overfalls II；11 overfalls III；12 overfalls IV, 13 overfalls V；14 iron wire cylinder moulds；15 inlets；16 leakage fluid drams；17 cobblestone filter courses；18 first quartz sand filtration layers；19 second quartz sand filtration layers；20 the 3rd quartz sand filtration layers；21 dividing plates.
Detailed description of the invention
Below in conjunction with accompanying drawing and detailed description of the invention, this utility model is described in further detail.
As shown in Figure 1, precipitated silica waste liquid settling separation device of the present utility model, including rectangle cell body, low-level culture pool 1 is included in described cell body, two grades of ponds 2, three grades of ponds 3, level Four pond 4, Pyatyi pond 5 and six grades of ponds 6, described low-level culture pool 1 and two grades of ponds 2 are set up in parallel, described three grades of ponds 3 are set up in parallel with level Four pond 4, described Pyatyi pond 5 and six grades of ponds 6 are set up in parallel, described three grades of ponds 3 also respectively with two grades of ponds 2, six grades of ponds 6 are set up in parallel, described level Four pond 4 also respectively with low-level culture pool 1, Pyatyi pond 5 is set up in parallel, described low-level culture pool 1 is internal is provided with filter cloth 7, described two grades of ponds 2 are internal is provided with filter cloth 8.
It is equipped with dividing plate 21 inside the cell body in described low-level culture pool, two grades of ponds, three grades of ponds, level Four pond, Pyatyi pond and six grades of ponds；Shown in Fig. 2 is the structural representation of low-level culture pool, pending waste liquid enters low-level culture pool 1 from inlet 15, first fraction solids particulate matter is deposited in the cell body of inlet 15 side, the liquid on upper strata then overflows across dividing plate 21 and enters in the cell body away from inlet 15 side, again through the filtration of filter cloth 7, retain partial impurities, entered in two grades of ponds 2 through overfall I 9, due to the effect of dividing plate 21, the liquid overflowing low-level culture pool 1 will not take away the floating thing of solid granular.
Sidewall between described low-level culture pool 1 and two grades of ponds 2 is provided with overfall I 9, sidewall between described two grades of ponds 2 and three grades of ponds 3 is provided with overfall II 10, sidewall between described three grades of ponds 3 and level Four pond 4 is provided with overfall III 11, sidewall between described level Four pond 4 and Pyatyi pond 5 is provided with overfall IV 12, and the sidewall between described Pyatyi pond 5 and six grades of ponds 6 is provided with overfall V 13；
Described overfall I 9, overfall II 10, overfall III 11, the position of overfall IV 12 and overfall V 13 is equipped with an iron wire cylinder mould 14, described iron wire cylinder mould 14 is internal is provided with filter course, as shown in Figure 3, described filter course includes the cobblestone filter course 17 from top to bottom stacked gradually, first quartz sand filtration layer 18, second quartz sand filtration layer 19 and the 3rd quartz sand filtration layer 20, described first quartz sand filtration layer 18, quartz sand particle size in second quartz sand filtration layer 19 and the 3rd quartz sand filtration layer 20 is sequentially reduced, wherein the quartz sand particle size in the 3rd quartz sand filtration layer 20 is 1～2mm.
Described low-level culture pool 1 is provided with inlet 15, and described six grades of ponds 6 are provided with leakage fluid dram 16.
nullThis utility model one producing white carbon black using settling method waste liquid settling separation device work process is as follows: entered in low-level culture pool 1 by inlet 15 by the waste liquid produced in precipitated silica production process，Respectively through dividing plate 21、A part of solid and impurity are leached and sink to the bottom by the effect of filter cloth 7 and overfall I 9 place iron wire cylinder mould 14，Waste liquid is flowed into two grades of ponds 2 from low-level culture pool 1 by overfall I 9，Further by dividing plate 21、A part of solid and impurity are leached and sink to the bottom by the effect of filter cloth 8 and overfall II 10 place iron wire cylinder mould 14，Waste liquid then passes through overfall II 10 and flows into three grades of ponds 3 from two grades of ponds 2，By the effect of dividing plate 21 and overfall III 11 place iron wire cylinder mould 14 a part of solid and impurity leached and sink to the bottom，Waste liquid flows into level Four pond 4 by overfall III 11 from three grades of ponds 3，By the effect of dividing plate 21 and overfall IV 11 place iron wire cylinder mould 14 a part of solid and impurity leached and sink to the bottom，Then waste liquid flows into Pyatyi pond 5 by overfall IV 12 from level Four pond 4，By the effect of dividing plate 21 and overfall IV place iron wire cylinder mould 14 a part of solid and impurity leached and sink to the bottom，Last waste liquid is flowed into six grades of ponds 6 from Pyatyi pond 5 by overfall V 13，Settlement separate further by the dividing plate in six grades of ponds 6，The waste liquid of clarification is obtained finally by leakage fluid dram 16.
Claims (3)
1. a precipitated silica waste liquid settling separation device, including rectangle cell body, it is characterized in that, low-level culture pool (1) is included in described cell body, two grades of ponds (2), three grades of ponds (3), level Four pond (4), Pyatyi pond (5) and six grades of ponds (6), described low-level culture pool (1) and two grades of ponds (2) are set up in parallel, described three grades of ponds (3) and level Four pond (4) are set up in parallel, described Pyatyi pond (5) and six grades of ponds (6) are set up in parallel, described three grades of ponds (3) also respectively with two grades of ponds (2), six grades of ponds (6) are set up in parallel, described level Four pond (4) also respectively with low-level culture pool (1), Pyatyi pond (5) is set up in parallel, described low-level culture pool (1) is internal is provided with the first defecator (7), described two grades of ponds (2) are internal is provided with the second defecator (8)；It is equipped with dividing plate (21) inside the cell body of described low-level culture pool (1), two grades of ponds (2), three grades of ponds (3), level Four pond (4), Pyatyi pond (5) and six grades of ponds (6)；
Sidewall between described low-level culture pool (1) and two grades of ponds (2) is provided with overfall I (9), sidewall between described two grades of ponds (2) and three grades of ponds (3) is provided with overfall II (10), sidewall between described three grades of ponds (3) and level Four pond (4) is provided with overfall III (11), sidewall between described level Four pond (4) and Pyatyi pond (5) is provided with overfall IV (12), and the sidewall between described Pyatyi pond (5) and six grades of ponds (6) is provided with overfall V (13)；
Described overfall I (9), overfall II (10), overfall III (11), the position of overfall IV (12) and overfall V (13) is equipped with an iron wire cylinder mould (14), described iron wire cylinder mould (14) is internal is provided with filter course, described filter course includes the cobblestone filter course (17) from top to bottom stacked gradually, first quartz sand filtration layer (18), second quartz sand filtration layer (19) and the 3rd quartz sand filtration layer (20), described first quartz sand filtration layer (18), quartz sand particle size in second quartz sand filtration layer (19) and the 3rd quartz sand filtration layer (20) is sequentially reduced；
Described low-level culture pool (1) is provided with inlet (15), and described six grades of ponds (6) are provided with leakage fluid dram (16).
2. precipitated silica waste liquid settling separation device according to claim 1, it is characterised in that described first defecator (7) and the second defecator (8) are filter cloth, filter screen or screen plate.
3. precipitated silica waste liquid settling separation device according to claim 1 and 2, it is characterised in that the quartz sand particle size in described 3rd quartz sand filtration layer (20) is 1～2mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620007338.4U CN205360818U (en) | 2016-01-04 | 2016-01-04 | Precipitated white carbon black waste liquid sedimentation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620007338.4U CN205360818U (en) | 2016-01-04 | 2016-01-04 | Precipitated white carbon black waste liquid sedimentation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205360818U true CN205360818U (en) | 2016-07-06 |
Family
ID=56275080
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620007338.4U Expired - Fee Related CN205360818U (en) | 2016-01-04 | 2016-01-04 | Precipitated white carbon black waste liquid sedimentation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205360818U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106396253A (en) * | 2016-08-30 | 2017-02-15 | 中山市海枣椰农业科技有限公司 | Treatment application method and treatment device of water for river irrigation |
| CN108889029A (en) * | 2018-07-07 | 2018-11-27 | 安徽润泓环保科技有限公司 | Sewage integrated treatment equipment |
| CN111203008A (en) * | 2020-01-08 | 2020-05-29 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
-
2016
- 2016-01-04 CN CN201620007338.4U patent/CN205360818U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106396253A (en) * | 2016-08-30 | 2017-02-15 | 中山市海枣椰农业科技有限公司 | Treatment application method and treatment device of water for river irrigation |
| CN108889029A (en) * | 2018-07-07 | 2018-11-27 | 安徽润泓环保科技有限公司 | Sewage integrated treatment equipment |
| CN111203008A (en) * | 2020-01-08 | 2020-05-29 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
| CN111203008B (en) * | 2020-01-08 | 2021-11-19 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205360818U (en) | Precipitated white carbon black waste liquid sedimentation device | |
| CN206063870U (en) | A kind of high-efficiency sedimentation device | |
| CN202876533U (en) | Wastewater treatment system for coal mine equipment | |
| CN105251267B (en) | Cement sewage processing and recycling system | |
| CN102849836A (en) | Sludge water concentration and purification treatment method and integrated treatment device | |
| CN202688121U (en) | Waste muddy water recycling system | |
| CN205100022U (en) | Bicone high concentration scummer | |
| CN206069537U (en) | A kind of sewage purifying and treating device | |
| CN103086446B (en) | Process for super-refining treatment of rejection water of low permeability oilfield and compound drive oilfield | |
| CN108939624A (en) | A kind of continous way sewage purification structure of Ceramic manufacturing | |
| CN206285543U (en) | A kind of subsider in the production for trimethylolpropane | |
| CN203389374U (en) | Dilute sulfuric acid mud tank | |
| CN207886813U (en) | Improve the efficient back flow water pump equipment of plain boiled water utilization rate | |
| CN206762458U (en) | A kind of vertical settling tank of sewage disposal | |
| CN213668299U (en) | Waste water treatment is with deposiing device based on chemical production uses | |
| CN204824175U (en) | Yellow phosphorus filtering pretreatment device and yellow phosphorus clean system who constitutes thereof | |
| CN219848573U (en) | Assembled multistage sedimentation tank of construction | |
| CN205099491U (en) | Device of concentrated separation washing ore pulp of membrane separation | |
| CN202724780U (en) | Gravity valveless filter pool | |
| CN204848509U (en) | Mud water processing system | |
| CN215208965U (en) | Dense medium magnetic coagulation high-efficiency integrated shale gas extraction water purification device | |
| CN207169237U (en) | A kind of aluminum fluoride slurries filtration system | |
| CN102690002B (en) | Solid-liquid separation method for tailing disposal | |
| CN216445131U (en) | Water pollution treatment and separation system | |
| CN201889850U (en) | Novel mud squeezing machine |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 Termination date: 20220104 |