CN201620035U - Raw brine deferrization device - Google Patents
Raw brine deferrization device Download PDFInfo
- Publication number
- CN201620035U CN201620035U CN2010200027567U CN201020002756U CN201620035U CN 201620035 U CN201620035 U CN 201620035U CN 2010200027567 U CN2010200027567 U CN 2010200027567U CN 201020002756 U CN201020002756 U CN 201020002756U CN 201620035 U CN201620035 U CN 201620035U
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- CN
- China
- Prior art keywords
- brine
- halogen
- storage
- bucket
- deferrization
- 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
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Abstract
The utility model relates to a raw brine deferrization device, which is used for removing ferrous iron contained in brine under a halite mine and is mainly formed by a brine storage barrel (1), a deflection reaction tank (2), a raw brine inlet (7), an aeration reactor (3), a flow equalizer (4), a Doll pipe (5), a flow equalizing weir (8), a mud drain pipe network (6) and a mud drain port (9). The device can combine chemical reaction, aeration accelerated reaction, settling and sedimentation and clean brine storage together, has the advantages of simple structure, convenient operation and reliable and practical process, is mainly used for raw brine deferrization and can also be popularized in fields such as wastewater treatment and the like.
Description
Affiliated technical field
The utility model relates to a kind of former halogen deironing apparatus.
Background technology
Generally all contain a certain amount of Fe2+ in the bittern of salt mine down-hole, this part Fe2+ enters and not only consumes Potassium Iodate in the salt making system and cause iodine loss, and influences the finished product salt whiteness, must add NaoH and carry out reaction treatment, and chemical equation is as follows:
Method according to routine need be provided with former halogen iron removal step, and technology mainly adopts chemical reaction, clarification, separation.Process unit mainly contains: one, deironing reaction container 2 covers, and your reacting-settler or stirring reaction bucket are led in main selection; Two, settling tank 2 covers are mainly selected inclined plate settler; Three, two covers of halogen transmitting pump.Not only investment is big, and must configuration special messenger operation.Simultaneously, the production cycle is longer, and the production process heat-energy losses is serious, salt manufacturing cost height.
Summary of the invention
In order to shorten the production cycle, reduce heat-energy losses, reduce the salt manufacturing cost, the utility model has designed a kind of simple in structure, easy to operate former halogen deironing apparatus.
The technical scheme that its technical problem that solves the utility model adopts is: this device is in storage halogen bucket top one side one baffling reactive tank to be set, the baffling reactive tank is provided with former halogen inlet, storage halogen bucket top center is provided with the taper aeration reactor, aeration reactor is outward a current equalizer, lead your pipe upper end and connect current equalizer, the lower end passes to storage halogen bucket bottom, and storage halogen bucket upper edge is provided with the current-sharing weir, and the bottom is provided with spoil disposal pipe network and mud discharging mouth.
The beneficial effects of the utility model are: chemical reaction, aeration accelerated reaction, heavy clear sedimentation, clear halogen stored and combined, and simple in structure, easy to operate, can realize automatic control, need not be equipped with the special messenger.Install concentratedly relatively, floor space is little, and reduced investment, technology are reliable and practical.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is a structural representation of the present utility model.
Among the figure: 1. storage halogen bucket, 2. baffling reactive tank, 3. aeration reactor, 4. current equalizer is 5. led your pipe, 6. spoil disposal pipe network, 7. former halogen inlet, 8. current-sharing weir, 9. mud discharging mouth.
Embodiment
Below in conjunction with accompanying drawing, use of the present utility model is elaborated: this device is in storage halogen bucket (1) top one side one baffling reactive tank (2) to be set, the baffling reactive tank is provided with former halogen inlet (7), ferrous iron in quantitative adding of NaoH solution and the former halogen is reacted, reaction generates insoluble ironic hydroxide, reacted bittern is on the taper aeration reactor (3) that flow to storage halogen bucket top center, quicken to flow into the current equalizer (4) that aeration reactor is provided with outward behind the aerated reaction, evenly the inflow center is led your pipe (5) and is directed at the further reaction of storage bucket bottom, heavy clear sedimentation, clear halogen rises on the storage halogen bucket, along evenly flowing into current-sharing weir (8), standby by brine pipeline input halogen pond.The settled insoluble ironic hydroxide in bottom (iron halogen mud) is discharged storage halogen bucket by the spoil disposal pipe network (6) that is arranged on the bottom by mud discharging mouth (9), and press filtration is handled.
This device is mainly used in former halogen deironing, also can be generalized to fields such as wastewater treatment.
Claims (1)
1. former halogen deironing apparatus, it is characterized in that: this device is in storage halogen bucket (1) top one side one baffling reactive tank (2) to be set, the baffling reactive tank is provided with former halogen inlet (7), storage halogen bucket top center is provided with taper aeration reactor (3), aeration reactor is outward current equalizer (4), leads your pipe (5) upper end and connects current equalizer, and the lower end passes to storage halogen bucket bottom, storage halogen bucket upper edge is provided with current-sharing weir (8), and the bottom is provided with spoil disposal pipe network (6) and mud discharging mouth (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200027567U CN201620035U (en) | 2010-01-12 | 2010-01-12 | Raw brine deferrization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200027567U CN201620035U (en) | 2010-01-12 | 2010-01-12 | Raw brine deferrization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201620035U true CN201620035U (en) | 2010-11-03 |
Family
ID=43023491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010200027567U Expired - Fee Related CN201620035U (en) | 2010-01-12 | 2010-01-12 | Raw brine deferrization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201620035U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030495A (en) * | 2014-07-03 | 2014-09-10 | 中蓝连海设计研究院 | Recycling treatment method for sylvinite ore brine containing soluble ferrite |
| CN104496093A (en) * | 2014-11-04 | 2015-04-08 | 江苏大学 | Method for performing purification treatment on titanium white wastewater by utilizing salt slurry |
-
2010
- 2010-01-12 CN CN2010200027567U patent/CN201620035U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030495A (en) * | 2014-07-03 | 2014-09-10 | 中蓝连海设计研究院 | Recycling treatment method for sylvinite ore brine containing soluble ferrite |
| CN104496093A (en) * | 2014-11-04 | 2015-04-08 | 江苏大学 | Method for performing purification treatment on titanium white wastewater by utilizing salt slurry |
| CN104496093B (en) * | 2014-11-04 | 2017-01-25 | 江苏大学 | Method for performing purification treatment on titanium white wastewater by utilizing salt slurry |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101103 Termination date: 20110112 |