CN201896078U - Magnetic resin adsorption reaction recovery device - Google Patents
Magnetic resin adsorption reaction recovery device Download PDFInfo
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- CN201896078U CN201896078U CN2010206223284U CN201020622328U CN201896078U CN 201896078 U CN201896078 U CN 201896078U CN 2010206223284 U CN2010206223284 U CN 2010206223284U CN 201020622328 U CN201020622328 U CN 201020622328U CN 201896078 U CN201896078 U CN 201896078U
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- magnetic
- magnetic resin
- cylindrical reactor
- absorption reaction
- resin
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Abstract
The utility model relates to the field of wastewater treatment, in particular to a magnetic resin adsorption reaction recovery device. The magnetic resin adsorption reaction recovery device comprises a columnar reactor and magnetic separation equipment, wherein the upper part of the columnar reactor is a cylinder and the lower part of the columnar reactor is a conoid, 1 to 5 layers of mixer blades are arranged in the columnar reactor, and the magnetic separation equipment is arranged at the upper part of the columnar reactor. The magnetic resin adsorption reaction recovery device has the characteristics of large treating water amount, stable and reliable equipment operation, low energy consumption and lower cost.
Description
Technical field
The utility model relates to field of waste water treatment, relates in particular to magnetic resin absorption reaction retrieving arrangement.
Background technology
Ion exchange method be a kind of remove by means of the ion on the ion-exchanger and the ion in the water carry out permutoid reaction anhydrate in the method for harmful ion.
Advantages such as adopt ion exchange method, have the clearance height, can concentrate the recovery useful matter, equipment is simpler, and operation control is easy mainly are to be used for water softening and decolouring.But the shortcoming that the present common ion exchange resin of using exists some to be difficult to overcome, for example unstable in acid or alkaline media, exchange capacity descends in the working process.And if when containing a certain amount of suspended solids or muddy heavy-gravity slurry in the pending solution, ordinary resin separates with solid-liquid between solution, admittedly and consolidate-separate the very difficulty that just becomes between ordinary resin and the suspended solids.
The research of magnetic resin has a lot of open source literatures at present since the seventies in last century, and for example 91100655.9 Chinese patents disclose a kind of method for preparing magnetism macroporous adsorbed ion exchange resin; 03130423.0 disclose a kind of ferromegnetism urea-formaldehyde resin microballoon medium and preparation method thereof again.At the research of the adsorption unit of magnetic resin publication number being arranged is CN101708876A, and it discloses a kind of hydraulic jet magnetic resin adsorptive reactor, uses the jet pipe water inlet, and agitator mixes, and triphase separator carries out separating of resin and water.The jet water inlet that this equipment uses can strengthen the broken and wearing and tearing of resin in mixing, and triphase separator can't be with single trickle resin separating treatment from water simultaneously, and the number of dropouts of resin also can be bigger.
The utility model content
In view of there is above-mentioned weak point in prior art, the utility model provides a kind of treatment scheme short, and it is big to handle the water yield, and stable equipment operation is reliable, and energy consumption is low, the magnetic resin absorption reaction retrieving arrangement that expense is low.For achieving the above object, a kind of magnetic resin absorption reaction retrieving arrangement that the utility model provides, this device comprises cylindrical reactor and magnetic separating apparatus two portions, cylindrical reactor top is divided into right cylinder, the cylindrical reactor bottom is divided into cone, 1-5 layer agitating vane is set in the cylindrical reactor, the agitating vane that haves three layers in the preferred cylindrical reactor, magnetic separating apparatus is on cylindrical reactor top.Magnetic separating apparatus is by magnetic drum, dreg scraping stripe and unload slag chute and form.Unloading slag chute one end is connected with the magnetic resin regenerating unit.The cylindrical reactor bottom is provided with 1-5 water-in, and preferred cylindrical reactor bottom is provided with 3 water-ins.
Effect of the present utility model is achieved in that and adds magnetic resin in cylindrical reactor, waste water enters from the cylindrical reactor bottom, under the effect of agitating vane, waste water fully contacts with magnetic resin, magnetic resin after the generation absorption reaction moves with current direction cylindrical reactor middle and upper part, when arriving the cylindrical reactor top, pass through magnetic separation technique, magnetic resin is adsorbed on the magnetic separator surface, and along with the rotation of magnetic separator is taken magnetic resin out of the water surface, by slag unloading device magnetic resin is unloaded, be transported to and enter once more in the cylindrical reactor after the magnetic resin regenerating unit is regenerated, circulation reacts.Water outlet is to flow out to water outlet from the magnetic separating apparatus bottom through turning over mill weir, and whole process flow is short, the magnetic resin recycle.
The utlity model has following advantage:
Compared with prior art, advantage of the present invention is: simple to operate, the entire treatment flow process is short; The processing water yield is big; Mechanical part is less, stable and reliable operation, and energy consumption is low; Compact equipment, the integrated degree height, floor space is little; Separation efficiency is fast at a high speed, can greatly reduce the loss of resin; Only need to add magnetic resin in the use of this equipment, need not to add other medicaments, running cost is low.The utility model equipment can be widely used in the Treatment of Coking Effluent of each iron and steel and coal chemical enterprise and the transformation of reuse facility.
Description of drawings
Fig. 1 is the structural representation of magnetic resin absorption reaction retrieving arrangement;
Among the above figure, the 1 fingering mouth of a river wherein; 2 refer to agitating vane; 3 refer to cylindrical reactor; 4 refer to magnetic separating apparatus; 5 refer to magnetic drum; 6 refer to dreg scraping stripe; 7 refer to unload slag chute; 8 refer to turn over mill weir; 9 point out the mouth of a river; 10 refer to the magnetic resin regenerating unit; 11 refer to the magnetic resin inlet after the regeneration.
Embodiment
Below in conjunction with accompanying drawing structure of the present utility model and working process are described.
Embodiment
As shown in Figure 1, the magnetic resin absorption reaction retrieving arrangement that present embodiment provides, comprise cylindrical reactor 3 and magnetic separating apparatus 4 two portions, cylindrical reactor 3 tops are divided into right cylinder, cylindrical reactor 3 bottoms are divided into cone, 3 layers of agitating vane are set in the cylindrical reactor, and magnetic separating apparatus 4 is on cylindrical reactor 3 tops.Magnetic separating apparatus 4 is by magnetic drum 5, dreg scraping stripe 6 and unload slag chute 7 and form.Unloading slag chute 7 one ends is connected with magnetic resin regenerating unit 10.Cylindrical reactor 3 bottoms are provided with 3 water-ins 1.
Adopt above equipment, the coking chemical waste water of certain enterprise is made advanced treatment, adopt same water sample, carried out 4 tests altogether.
Add the magnetic resin of 5%-50% volume in cylindrical reactor 3, magnetic resin particle diameter 50um-250um, proportion are 1.02.Coking chemical waste water enters from the water-in 1 of cylindrical reactor 3 bottoms, under the effect of agitating vane 2, coking chemical waste water fully contacts with magnetic resin, magnetic resin after the generation absorption reaction moves with current direction cylindrical reactor 3 middle and upper parts, when moving to cylindrical reactor 3 tops, magnetic resin is adsorbed on its surface by magnetic drum 5, and along with the rotation of magnetic drum 5 is taken out of the water surface, after dreg scraping stripe 6 is discharged to the magnetic resin on magnetic drum 5 surfaces in the slag chute 7, this magnetic resin is transported to magnetic resin regenerating unit 10 and regenerates, and the magnetic resin of process manipulation of regeneration is circulated back to the cylindrical reactor 3 from magnetic resin inlet 11.Water outlet is to flow out to water outlet 9 from magnetic drum 5 bottoms through turning over mill weir 8.
Test-results is as shown in the table:
Magnetic resin absorption reaction retrieving arrangement Treatment of Wastewater in Coking test-results
Has good effect by above-mentioned test-results explanation the utility model Treatment of Wastewater in Coking.
Claims (6)
1. magnetic resin absorption reaction retrieving arrangement, it is characterized in that: this device comprises cylindrical reactor (3) and magnetic separating apparatus (4) two portions, cylindrical reactor (3) top is divided into right cylinder, cylindrical reactor (3) bottom is divided into cone, 1-5 layer agitating vane (2) is set in the cylindrical reactor (3), and magnetic separating apparatus (4) is on cylindrical reactor (3) top.
2. magnetic resin absorption reaction retrieving arrangement as claimed in claim 1 is characterized in that: agitating vane (2) haves three layers in the cylindrical reactor (3).
3. magnetic resin absorption reaction retrieving arrangement as claimed in claim 2 is characterized in that: magnetic separating apparatus (4) is by magnetic drum (5), dreg scraping stripe (6) and unload slag chute (7) and form.
4. magnetic resin absorption reaction retrieving arrangement as claimed in claim 3 is characterized in that: unload slag chute (7) one ends and be connected with magnetic resin regenerating unit (10).
5. magnetic resin absorption reaction retrieving arrangement as claimed in claim 1 or 2 is characterized in that: cylindrical reactor (3) bottom is provided with 1-5 water-in (1).
6. magnetic resin absorption reaction retrieving arrangement as claimed in claim 5 is characterized in that: cylindrical reactor (3) bottom is provided with 3 water-ins (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206223284U CN201896078U (en) | 2010-11-24 | 2010-11-24 | Magnetic resin adsorption reaction recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206223284U CN201896078U (en) | 2010-11-24 | 2010-11-24 | Magnetic resin adsorption reaction recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201896078U true CN201896078U (en) | 2011-07-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206223284U Expired - Lifetime CN201896078U (en) | 2010-11-24 | 2010-11-24 | Magnetic resin adsorption reaction recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201896078U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106277186A (en) * | 2016-09-12 | 2017-01-04 | 南京大学 | A kind of magnetic resin waste water treatment reactor and using method thereof |
| CN111874993A (en) * | 2020-08-04 | 2020-11-03 | 江苏永冠给排水设备有限公司 | Continuous water treatment device and process |
-
2010
- 2010-11-24 CN CN2010206223284U patent/CN201896078U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106277186A (en) * | 2016-09-12 | 2017-01-04 | 南京大学 | A kind of magnetic resin waste water treatment reactor and using method thereof |
| CN106277186B (en) * | 2016-09-12 | 2019-11-08 | 南京大学 | A kind of magnetic resin waste water treatment reactor and its application method |
| CN111874993A (en) * | 2020-08-04 | 2020-11-03 | 江苏永冠给排水设备有限公司 | Continuous water treatment device and process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 610045 Wuhou District, Sichuan Province, Wu Xing Road, No. 3, No. Patentee after: Ring energy Polytron Technologies Inc Address before: 610045 Wuhou District, Sichuan Province, Wu Xing Road, No. 3, No. Patentee before: Sichuan Demo-scimee Science and Technology Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 610045 No. 3, Wu Xing Road, Chengdu, Sichuan, Wuhou District Patentee after: CSCEC Huanneng Technology Co., Ltd Address before: 610045 No. 3, Wu Xing Road, Chengdu, Sichuan, Wuhou District Patentee before: Ring energy Polytron Technologies Inc |
|
| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110713 |
|
| CX01 | Expiry of patent term |