CN213327042U - Efficient fluorine and hardness removing device for water inlet of evaporator - Google Patents
Efficient fluorine and hardness removing device for water inlet of evaporator Download PDFInfo
- Publication number
- CN213327042U CN213327042U CN202021507345.3U CN202021507345U CN213327042U CN 213327042 U CN213327042 U CN 213327042U CN 202021507345 U CN202021507345 U CN 202021507345U CN 213327042 U CN213327042 U CN 213327042U
- Authority
- CN
- China
- Prior art keywords
- tank
- defluorination
- hardness removal
- hardness
- removal reaction
- 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.)
- Active
Links
Images
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
The utility model discloses a high-efficiency defluorination and hardness removal device for water inlet of an evaporator, which comprises a defluorination and hardness removal reaction tank, a defluorination and hardness removal dosing tank and a hardness removal dosing tank which are communicated with the defluorination and hardness removal reaction tank and are positioned above the defluorination and hardness removal reaction tank, a PH regulating tank which is adjacent to the same wall of the defluorination and hardness removal reaction tank, an acidic liquid medicine tank and an alkaline liquid medicine tank which are communicated with the PH regulating tank and are positioned above the PH regulating tank, and a sedimentation tank which is adjacent to the same wall of the defluorination and hardness removal reaction tank and the PH regulating tank respectively; the defluorination and hardness removal reaction tank is provided with a first water inlet, the defluorination and hardness removal reaction tank is communicated with the top of the PH regulating tank, the PH regulating tank is communicated with the top of the sedimentation tank, and the alkaline liquid medicine tank is communicated with the defluorination and hardness removal reaction tank. The utility model discloses a defluorination removes hard and merges and goes on, and effective overall arrangement space occupies.
Description
Technical Field
The utility model belongs to the technical field of sewage treatment, especially, relate to a be used for evaporimeter to intake high-efficient defluorination and remove hard device.
Background
The traditional treatment process of the fluorine-containing hard wastewater has the following disadvantages: membrane treatment processes (e.g., reverse osmosis) are generally used, and high concentration of hardness ions (calcium ions) in water is highly likely to cause scaling of the membrane surface and clogging of the membrane pores. Wastewater treatment plants typically involve more equipment, resulting in larger floor space for the spatial arrangement.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the technical problem and providing a high-efficient defluorination removes hard device for evaporimeter is intake to realize that the defluorination removes hard and merges and go on, effective overall arrangement space occupies. In order to achieve the above purpose, the utility model discloses technical scheme as follows:
the efficient defluorination and hardness removal device for the water inlet of the evaporator comprises a defluorination and hardness removal reaction tank, a defluorination and hardness removal dosing tank and a hardness removal dosing tank which are communicated with and positioned above the defluorination and hardness removal reaction tank, a PH regulating tank which is adjacent to the same wall as the defluorination and hardness removal reaction tank, an acidic liquid medicine tank and an alkaline liquid medicine tank which are communicated with and positioned above the PH regulating tank, and sedimentation tanks which are adjacent to the same wall as the defluorination and hardness removal reaction tank and the PH regulating tank respectively; the defluorination and hardness removal reaction tank is provided with a first water inlet, the defluorination and hardness removal reaction tank is communicated with the top of the PH regulating tank, the PH regulating tank is communicated with the top of the sedimentation tank, and the alkaline liquid medicine tank is communicated with the defluorination and hardness removal reaction tank.
Specifically, the top of defluorination and hardness removal reaction tank is provided with a first water inlet, and the bottom of the defluorination and hardness removal reaction tank is provided with a first sewage discharge port.
Specifically, the alkaline liquid medicine in the alkaline liquid medicine tank is added into a defluorination and hardness removal reaction tank through a pump, and after the sewage in the defluorination and hardness removal reaction tank is adjusted to be alkaline, the PH value is 8-9.
Specifically, the defluorination and hardness removal liquid medicine in the defluorination and hardness removal dispensing pool and the hardness removal dispensing pool is added into the defluorination and hardness removal reaction pool through a pump.
Specifically, the liquid medicine in the acidic liquid medicine tank is added into a pH adjusting tank through a pump, and the pH of the sewage is 6-7.
Specifically, be equipped with the second water inlet of butt joint PH equalizing basin in the sedimentation tank, sewage discharges into the sedimentation tank in the PH equalizing basin and carries out flocculation reaction.
Specifically, a water outlet for discharging supernatant is formed in the top of one side of the sedimentation tank, and a second sewage draining outlet for discharging precipitated impurities is formed in the bottom of the adjacent side of the sedimentation tank.
Compared with the prior art, the utility model discloses a beneficial effect for evaporimeter high-efficient defluorination removes hard device of intaking mainly embodies:
the space occupation is saved by reasonably arranging the position relations of the defluorination and hardness removal reaction tank, the PH regulating tank and the sedimentation tank; the agent for removing fluorine and hardness is arranged above the reaction tank for removing fluorine and hardness, so that the agent is convenient to configure and store, and the fluorine removal and the hardness removal are combined and carried out simultaneously, thereby reasonably simplifying the working procedure and saving the cost; the whole process is simplified, the structure is simple, and the water outlet effect is good.
Drawings
Fig. 1 is a schematic top view of an embodiment of the present invention;
the figures in the drawings represent:
1 defluorination removes hard reaction tank, 11 defluorination dispensing pool, 12 remove hard dispensing pool, 2PH equalizing basin, 21 acid liquid medicine pond, 22 alkaline liquid medicine pond, 3 sedimentation tank, 4 first water inlet, 41 second water inlet, 5 delivery ports, 51 second drain.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely below, and it should be understood that the described embodiments are only some embodiments of the present invention, and not all embodiments.
Example (b):
referring to fig. 1, the present embodiment is an efficient defluorination and hardness removal device for evaporator water inlet, which includes a defluorination and hardness removal reaction tank 1, a defluorination and chemical dosing tank 11 and a hardness removal and chemical dosing tank 12 communicating the defluorination and hardness removal reaction tank 1 to be located above the defluorination and hardness removal reaction tank, a PH adjusting tank 2 adjacent to the same wall of the defluorination and hardness removal reaction tank 1, an acidic chemical liquid tank 21 and an alkaline chemical liquid tank 22 communicating the PH adjusting tank 2 to be located above the defluorination and hardness removal reaction tank, and a sedimentation tank 3 adjacent to the same wall of the defluorination and hardness removal reaction tank 1 and the PH adjusting tank 2, respectively; the defluorination and hardness removal reaction tank 1 is provided with a first water inlet 4, the defluorination and hardness removal reaction tank 1 is communicated with the top of a PH adjusting tank 2, the PH adjusting tank 2 is communicated with the top of a sedimentation tank 3, and an alkaline liquid medicine tank 22 is communicated with the defluorination and hardness removal reaction tank 1.
The top of the defluorination and hardness removal reaction tank 1 is provided with a first water inlet 4, and the bottom thereof is provided with a first sewage discharge port (not marked in the figure).
Alkaline liquid medicine in the alkaline liquid medicine pool 22 is added into the defluorination and hardness removal reaction pool 1 through a pump, after sewage in the defluorination and hardness removal reaction pool 1 is adjusted to be alkaline, the PH value is 8-9, and defluorination and hardness removal liquid medicine in the defluorination and medicine preparation pool 11 and the hardness removal and medicine preparation pool 12 are added into the defluorination and hardness removal reaction pool 1 through a pump.
After the reaction in the defluorination and hardness removal reaction tank 1 is finished, sewage is discharged into a PH adjusting tank 2, liquid medicine in an acid liquid medicine tank 21 is added into the PH adjusting tank 2 through a pump, and the PH of the sewage is 6-7.
A second water inlet 41 which is butted with the PH adjusting tank 2 is arranged in the sedimentation tank 3, and sewage in the PH adjusting tank 2 is discharged into the sedimentation tank 3 for flocculation reaction.
The top of one side of the sedimentation tank 3 is provided with a water outlet 5 for discharging supernatant, and the bottom of the adjacent side of the sedimentation tank 2 is provided with a second sewage outlet 51 for discharging precipitated impurities.
The total long distance of the defluorination and hardness removal reaction tank 1 and the PH adjusting tank 2 is correspondingly consistent with the length of the sedimentation tank 3, and the defluorination and hardness removal reaction tank 1, the PH adjusting tank 2 and the sedimentation tank 3 are integrally of a hollow cuboid co-building structure with the same bottom.
A monitor (not shown) for monitoring the pH value is provided in the pH control tank 2.
When the method is applied, the space occupation is saved by reasonably arranging the position relations of the defluorination and hardness removal reaction tank 1, the PH adjusting tank 2 and the sedimentation tank 3; the agent for removing fluorine and hardness is arranged above the reaction tank 1 for removing fluorine and hardness, so that the agent can be conveniently configured and stored, and the fluorine removal and the hardness removal are simultaneously carried out, thereby reasonably simplifying the process and saving the cost; the whole process is simplified, the structure is simple, and the water outlet effect is good.
What has been described above are only some embodiments of the invention. For those skilled in the art, without departing from the inventive concept, several modifications and improvements can be made, which are within the scope of the invention.
Claims (7)
1. A it removes fluorine and removes hard device to be used for evaporimeter to intake high-efficient, its characterized in that: the device comprises a defluorination and hardness removal reaction tank, a defluorination and hardness removal dosing tank and a hardness removal dosing tank which are communicated with and above the defluorination and hardness removal reaction tank, a PH regulating tank which is adjacent to the same wall of the defluorination and hardness removal reaction tank, an acidic liquid medicine tank and an alkaline liquid medicine tank which are communicated with and above the PH regulating tank, and a sedimentation tank which is adjacent to the same wall of the defluorination and hardness removal reaction tank and the PH regulating tank respectively; the defluorination and hardness removal reaction tank is provided with a first water inlet, the defluorination and hardness removal reaction tank is communicated with the top of the PH regulating tank, the PH regulating tank is communicated with the top of the sedimentation tank, and the alkaline liquid medicine tank is communicated with the defluorination and hardness removal reaction tank.
2. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: the top of the defluorination and hardness removal reaction tank is provided with a first water inlet, and the bottom of the defluorination and hardness removal reaction tank is provided with a first sewage discharge port.
3. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: and the alkaline liquid medicine in the alkaline liquid medicine tank is added into the defluorination and hardness removal reaction tank through a pump, and the PH value is 8-9 after the sewage in the defluorination and hardness removal reaction tank is adjusted to be alkaline.
4. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: and the defluorination and hardness removal liquid medicine in the defluorination and hardness removal dispensing pool and the hardness removal dispensing pool is added into the defluorination and hardness removal reaction pool through a pump.
5. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: the liquid medicine in the acidic liquid medicine tank is added into a pH adjusting tank through a pump, and the pH of the sewage is 6-7.
6. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: and a second water inlet which is butted with a PH adjusting tank is arranged in the sedimentation tank, and sewage in the PH adjusting tank is discharged into the sedimentation tank to carry out flocculation reaction.
7. The device for efficiently removing fluorine and hardness from inlet water of the evaporator according to claim 1, wherein: the top of one side of sedimentation tank is equipped with the delivery port that is used for discharging the supernatant, and the bottom of the adjacent side of sedimentation tank is equipped with the second drain that is used for discharging sediment impurity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021507345.3U CN213327042U (en) | 2020-07-27 | 2020-07-27 | Efficient fluorine and hardness removing device for water inlet of evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021507345.3U CN213327042U (en) | 2020-07-27 | 2020-07-27 | Efficient fluorine and hardness removing device for water inlet of evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213327042U true CN213327042U (en) | 2021-06-01 |
Family
ID=76090825
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021507345.3U Active CN213327042U (en) | 2020-07-27 | 2020-07-27 | Efficient fluorine and hardness removing device for water inlet of evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213327042U (en) |
-
2020
- 2020-07-27 CN CN202021507345.3U patent/CN213327042U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201972020U (en) | Water-saving washing machine with double-row water pipelines | |
| CN209809946U (en) | Online cleaning system for filtering membrane | |
| CN210286897U (en) | Continuous alternating MBBR sewage treatment device | |
| CN213327042U (en) | Efficient fluorine and hardness removing device for water inlet of evaporator | |
| CN206705858U (en) | A kind of sewage-treatment plant based on gas-water separation film | |
| CN205313292U (en) | Middle -size and small -size energy -conserving cooling circulating water treatment system | |
| CN211226644U (en) | Sewage treatment plant for environmental protection | |
| CN213388072U (en) | Sewage treatment device with good sewage treatment and purification performance | |
| CN202415328U (en) | Dyeing and finishing sewage treatment system used for textile process | |
| CN213060598U (en) | Municipal sludge heavy metal treatment system | |
| CN210528714U (en) | MBR membrane sewage treatment plant | |
| CN211198892U (en) | Full-automatic industrial circulating water electrochemical treatment device | |
| CN209797660U (en) | Emulsion wastewater treatment device | |
| CN209797724U (en) | Sewage treatment all-in-one machine | |
| CN207685348U (en) | A kind of PCB etching liquids device for filtering impurities | |
| CN215161989U (en) | Bury formula integration sewage treatment plant | |
| CN213603863U (en) | Novel recirculating aquaculture system | |
| CN201620065U (en) | Automatic deiron and demanganese water supply equipment | |
| CN220779206U (en) | Filter element self-cleaning filtering device and water purifying and drinking machine | |
| CN220364441U (en) | Oxidation precipitation device for removing thallium from sintering and pellet desulfurization wastewater | |
| CN218280932U (en) | Anti-blocking vacuum filter tank | |
| CN213112902U (en) | Drinking water purifier | |
| CN219279693U (en) | Centralized micro-power ultrafiltration water purification equipment | |
| CN213112635U (en) | Efficient water-saving reverse osmosis water purification equipment | |
| CN217972884U (en) | Novel reverse osmosis water purification machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |