CN220317506U - Coarse filtration device for industrial production of magnesium fluosilicate - Google Patents
Coarse filtration device for industrial production of magnesium fluosilicate Download PDFInfo
- Publication number
- CN220317506U CN220317506U CN202321664937.XU CN202321664937U CN220317506U CN 220317506 U CN220317506 U CN 220317506U CN 202321664937 U CN202321664937 U CN 202321664937U CN 220317506 U CN220317506 U CN 220317506U
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- Prior art keywords
- pipe
- storehouse
- filtration
- bin
- industrial production
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- 238000001914 filtration Methods 0.000 title claims abstract description 60
- 238000009776 industrial production Methods 0.000 title claims abstract description 17
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 16
- 239000011777 magnesium Substances 0.000 title claims abstract description 16
- 238000004062 sedimentation Methods 0.000 claims abstract description 29
- 239000010865 sewage Substances 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 239000003814 drug Substances 0.000 claims abstract description 10
- 238000011084 recovery Methods 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 7
- 238000000151 deposition Methods 0.000 claims 4
- 239000013049 sediment Substances 0.000 abstract description 12
- 229940104869 fluorosilicate Drugs 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 235000019738 Limestone Nutrition 0.000 abstract description 5
- 239000006028 limestone Substances 0.000 abstract description 5
- 239000006228 supernatant Substances 0.000 abstract description 4
- 239000003795 chemical substances by application Substances 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000001556 precipitation Methods 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 239000002244 precipitate Substances 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 235000013547 stew Nutrition 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- -1 magnesium fluorosilicate Chemical compound 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a coarse filtration device for industrial production of magnesium fluosilicate, which belongs to the field of fluorosilicate production equipment, wherein the left side and the right side of a sedimentation bin of the coarse filtration device for industrial production of magnesium fluosilicate are provided with filtration bins, sewage after sedimentation treatment in the sedimentation bin enters the filtration bins for filtration, so that the filtration effect can be effectively ensured, sewage enters the filtration bins from a sewage inlet pipe, a treatment agent such as limestone is added from a medicine inlet pipe, the sewage reacts and is precipitated in the sedimentation bin, the sewage stands and is precipitated in the sedimentation bin, sediment is recovered from a discharge hole and a discharge pipe by sedimentation layering, and supernatant enters the filtration bin from a liquid outlet pipe for filtration again, so that the filtration effect can be effectively ensured.
Description
Technical Field
The utility model belongs to the field of fluorosilicate production equipment, and particularly relates to a coarse filtration device for industrial production of magnesium fluorosilicate.
Background
When the intermittent method is used for producing the fluorosilicate, the fluorosilicate is required to be added into salt solution according to a certain proportion, the salt solution is added into the fluorosilicate, the fluorosilicate is generated by reaction, the feeding speed and curing time are controlled, fluorosilicate crystals with proper crystallinity are obtained, and then the fluorosilicate crystals are centrifugally separated and dried to obtain fluorosilicate products, and the dried tail gas is discharged after reaching the standard through a bag-type dust collector;
the dilute acid after centrifugal separation is sent to a sewage treatment station to be neutralized, flocculated and settled by lime, the discharged dilute acid is discharged after water treatment reaches the standard, silicic acid is contained in the discharged dilute acid, sedimentation is removed when the discharged dilute acid is sent to the sewage treatment station in the later stage, a sedimentation tank is adopted as coarse filtration equipment of dilute acid and acid in the sewage treatment station, the practical treatment equipment in the prior art has simple structure, the sedimentation tank is generally utilized to carry out simple sedimentation, limestone is added in the sedimentation tank in a sedimentation mode, residual dilute acid and silicic acid in the sewage are flocculated and settled after being neutralized by lime, and then filtration and separation can be carried out, but the sedimentation process needs time, and only sedimentation operation effect is limited.
Disclosure of Invention
In order to overcome the problems in the prior art, the utility model discloses a coarse filtration device for industrial production of magnesium fluosilicate, wherein the left side and the right side of a sedimentation bin of the coarse filtration device for industrial production of magnesium fluosilicate are provided with filtration bins, sewage after sedimentation treatment in the sedimentation bin enters the filtration bins for filtration, so that the filtration effect can be effectively ensured, sewage enters the filtration bins from a sewage inlet pipe, a treatment agent such as limestone is added from a medicine inlet pipe, the sewage reacts and precipitates in the sedimentation bin, the sewage stands and precipitates in the sedimentation bin, precipitates are recovered from a discharge hole and a discharge pipe by sedimentation layering, and supernatant enters the filtration bin from a liquid outlet pipe for filtration again, so that the filtration effect can be effectively ensured.
In order to achieve the above purpose, the utility model is realized by the following technical scheme:
the utility model provides a coarse filtration device for industrial production magnesium fluosilicate includes sediment storehouse, discharge gate, discharging pipe, sewage advance pipe, feed pipe, window, drain pipe, filtration storehouse, bottom recovery pipe, clear water advance pipe, side recovery pipe, the discharge gate sets up in sediment storehouse bottom, and the discharging pipe is connected with the discharge gate, and the sewage advances the pipe setting at sediment storehouse top, advances the medicine pipe setting at sediment storehouse top, and the window setting is in sediment storehouse openly, and the drain pipe setting is in sediment storehouse side, and filtration storehouse passes through drain pipe and filtration storehouse intercommunication, and bottom recovery pipe setting is in filtration storehouse bottom, and clear water advances the pipe setting at filtration storehouse top, and side recovery pipe sets up in filtration storehouse side, filtration storehouse inside is provided with the net storehouse.
The discharge hole is of an inverted cone structure.
The liquid outlet pipes are arranged at two, and the two liquid outlet pipes are positioned at the left side and the right side of the sedimentation bin.
The two liquid outlet pipes are communicated with the filter bins, and the two filter bins have the same structure.
The shape of the net bin is consistent with that of the filtering bin, the top surface of the net bin is connected with the top surface of the filtering bin, and the clean water inlet pipe, the liquid outlet pipe and the side recovery pipe are communicated with the net bin.
The bottom recovery pipes are positioned on the outer side of the net bin, and at least three bottom recovery pipes are arranged.
The utility model has the beneficial effects that: the utility model provides a filter house is provided with to industrial production magnesium fluosilicate with coarse filtration device's sediment storehouse left and right sides, sewage after sedimentation in sediment storehouse subsides the processing enters into the filter house and filters, can effectively guarantee the filter effect, sewage enters into the filter house from sewage feed pipe, add such treatment medicament of lime stone from the feed pipe, sewage reaction precipitation in sediment storehouse, sewage stews in sediment storehouse and deposits the layering and just retrieves the precipitate from discharge gate and discharging pipe, the supernatant enters into the filter house from the drain pipe and filters once more, can effectively guarantee the filter effect.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
fig. 2 is a schematic structural view of the filter cartridge.
In the figure, a 1-sedimentation bin, a 2-discharge port, a 3-discharge pipe, a 4-sewage inlet pipe, a 5-medicine inlet pipe, a 6-window, a 7-liquid outlet pipe, an 8-filtering bin, a 9-bottom recovery pipe, a 10-clear water inlet pipe, a 11-side recovery pipe and a 12-net bin are arranged.
Detailed Description
In order to make the above objects, technical schemes and beneficial effects clearer and more clear, the present utility model is specifically described below with reference to the accompanying drawings.
As shown in figures 1-2, the rough filtering device for industrial production of magnesium fluosilicate comprises a precipitation bin 1, a discharge hole 2, a discharge pipe 3, a sewage inlet pipe 4, a medicine inlet pipe 5, a window 6, a liquid outlet pipe 7, a filtering bin 8, a bottom recycling pipe 9, a clear water inlet pipe 10 and a side recycling pipe 11, wherein the discharge hole 2 is arranged at the bottom of the precipitation bin 1, the discharge pipe 3 is connected with the discharge hole 2, the discharge hole 2 is of a reverse taper structure, a pump body and a control valve are arranged on the discharge pipe 3, the sewage inlet pipe 4 is arranged at the top of the precipitation bin 1, the medicine inlet pipe 5 is arranged at the top of the precipitation bin 1, the window 6 is arranged at the front of the precipitation bin 1, the liquid outlet pipe 7 is arranged at the side of the precipitation bin 1, the filtering bin 8 is communicated with the filtering bin 8 through the liquid outlet pipe 7, the bottom recovery pipe 9 sets up in filtering storehouse 8 bottom, and clear water advances pipe 10 setting at filtering storehouse 8 top, and side recovery pipe 11 sets up in filtering storehouse 8 side, filtering storehouse 8 inside is provided with net storehouse 12, drain pipe 7 is provided with two, and two drain pipes 7 are located the left and right sides that deposits storehouse 1, and two drain pipe 7 department all communicates there is filtering storehouse 8, and the structure of two filtering storehouse 8 is the same, the shape of net storehouse 12 is unanimous with the shape of filtering storehouse 8, and the top surface of net storehouse 12 is connected with the top surface of filtering storehouse 8, and clear water advances pipe 10, drain pipe 7, side recovery pipe 11 and net storehouse 12 intercommunication, bottom recovery pipe 9 is located net storehouse 12 outside, and bottom recovery pipe 9 is provided with at least three.
The utility model provides a filter equipment, including sedimentation bin 1, filter bin 8, filter effect can effectively be guaranteed to the waste water after sedimentation in sedimentation bin 1, waste water enters into filter bin 8 from waste water inlet pipe 4, add such treatment medicament of lime stone from feed tube 5, waste water reaction precipitation in sedimentation bin 1, waste water stews in sedimentation bin 1 and deposits, the sediment layering just retrieves the precipitate from discharge gate 2 and discharging pipe 3, discharge gate 2 is the back taper structure, be provided with pump body and control valve on the discharging pipe 3, can retrieve the solid at the bottom of filter bin 8, the supernatant in filter bin 8 enters into filter bin 8 from liquid outlet pipe 7 and filters once more, the upper layer liquid of requesting enters into net storehouse 12 from liquid outlet pipe 7, net storehouse 12's shape is unanimous with filter bin 8, net storehouse 12's top surface and filter bin 8 top surface are connected, net 9, net diameter is in net 12 is retrieved from bottom 9, net diameter is in net 12 is retrieved to net 12, net diameter is 9, net diameter is retrieved from bottom 9 to net diameter is retrieved to net 12, net diameter is in net diameter is retrieved from bottom 9 to bottom of filter bin 12, the bottom is retrieved from the bottom of filter bin 9.
Finally, it is noted that the above-mentioned preferred embodiments are only intended to illustrate rather than limit the utility model, and that, although the utility model has been described in detail by means of the above-mentioned preferred embodiments, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the scope of the utility model as defined by the appended claims.
Claims (6)
1. The industrial production is coarse filtration device for magnesium fluosilicate, its characterized in that, coarse filtration device for industrial production magnesium fluosilicate is including depositing storehouse, discharge gate, discharging pipe, sewage advance the pipe, advance the medicine pipe, window, drain pipe, filtration storehouse, bottom recovery pipe, clear water advance the pipe, side recovery pipe, the discharge gate sets up in depositing the storehouse bottom, and the discharging pipe is connected with the discharge gate, and sewage advances the pipe setting and deposits the storehouse top, advances the medicine pipe setting and deposits the storehouse top, and the window setting is in depositing the storehouse openly, and the drain pipe setting is in depositing the storehouse side, and the filtration storehouse passes through drain pipe and filtration storehouse intercommunication, and the bottom recovery pipe setting is in filtration storehouse bottom, and clear water advances the pipe setting at filtration storehouse top, side recovery pipe setting is in filtration storehouse side, the inside net storehouse that is provided with of filtration storehouse.
2. The straining device for industrial production of magnesium fluosilicate according to claim 1, wherein: the discharge hole is of an inverted cone structure.
3. The straining device for industrial production of magnesium fluosilicate according to claim 1, wherein: the liquid outlet pipes are arranged at two, and the two liquid outlet pipes are positioned at the left side and the right side of the sedimentation bin.
4. A straining device for industrial production of magnesium fluosilicate according to claim 3, characterized in that: the two liquid outlet pipes are communicated with the filter bins, and the two filter bins have the same structure.
5. The straining device for industrial production of magnesium fluosilicate according to claim 1, wherein: the shape of the net bin is consistent with that of the filtering bin, the top surface of the net bin is connected with the top surface of the filtering bin, and the clean water inlet pipe, the liquid outlet pipe and the side recovery pipe are communicated with the net bin.
6. The straining device for industrial production of magnesium fluosilicate according to claim 1, wherein: the bottom recovery pipes are positioned on the outer side of the net bin, and at least three bottom recovery pipes are arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321664937.XU CN220317506U (en) | 2023-06-28 | 2023-06-28 | Coarse filtration device for industrial production of magnesium fluosilicate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321664937.XU CN220317506U (en) | 2023-06-28 | 2023-06-28 | Coarse filtration device for industrial production of magnesium fluosilicate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220317506U true CN220317506U (en) | 2024-01-09 |
Family
ID=89420224
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321664937.XU Active CN220317506U (en) | 2023-06-28 | 2023-06-28 | Coarse filtration device for industrial production of magnesium fluosilicate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220317506U (en) |
-
2023
- 2023-06-28 CN CN202321664937.XU patent/CN220317506U/en active Active
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