CN208292708U - A kind of Ion exchange resin high tower separation system - Google Patents
A kind of Ion exchange resin high tower separation system Download PDFInfo
- Publication number
- CN208292708U CN208292708U CN201820209843.6U CN201820209843U CN208292708U CN 208292708 U CN208292708 U CN 208292708U CN 201820209843 U CN201820209843 U CN 201820209843U CN 208292708 U CN208292708 U CN 208292708U
- Authority
- CN
- China
- Prior art keywords
- resin
- tower
- knockout tower
- flushing pipe
- output channel
- 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
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a kind of Ion exchange resin high tower separation systems, the system comprises separation system and regenerative systems, the separation assembly is connected at the top of the knockout tower (1) of the separation system, the separation assembly includes stirring motor (2), agitating shaft (3) and stirring blade (4), the top of the knockout tower (1) is connected to upper rinsing module, the bottom of the knockout tower (1) is connected to the lower rinsing module, the top of the knockout tower (1) is connected to exhausted resin pipeline (19), exhaust outlet (7) are additionally provided at the top of the knockout tower (1), knockout tower (1) side wall is communicated with negative resin output channel (9) and positive resin output channel (10), the negative resin output channel (9) and positive resin output channel (10) are communicated to regenerative system.Negative resin and positive resin are sufficiently separated by the utility model, and wherein contain a small amount of impurity, regenerate negative resin and positive resin timely and effectively.
Description
Technical field
The utility model relates to a kind of separation system, specially a kind of Ion exchange resin high tower separation system.
Background technique
The effect of condensed water precision processing system is the trace mineral dissolved in removing condensed water, such as: Fe, Cu, SiO2、
Na+, Cl- etc. and a small amount of suspended matter and dissolved solid.These substances may in varied situations with the metal in system
It works and causes premature destruction, or deposition is in systems, causes ineffective systems and mechanical damage.Therefore, to meet
High parameter, requirement of the heavy-duty generator group to boiler water quality, makes condensed water precision processing system really play protection therrmodynamic system,
The effect for increasing economic benefit, to condensed water precision processing system, in addition to the design of apparatus body (especially mixed bed), the choosing of resin
It selects and matches, Steam Condenser Leak amount will be reduced to bottom line, it is often more important that focus on the selection of resin separation regeneration method.
The operational effect of condensed water precision processing system also just depends on the selection of separation regeneration scheme.The condensation that the country is currently running at present
The resin separation regeneration method of crystal's processing system mainly has: ammoniation process, concentrated base floatation, intermediate extracting method, cone separating method,
High tower separation technique etc..Wherein high tower separation technique system was answered in Power System in China condensed water precision processing system since 1993
With a kind of most commonly used scheme.In recent years, domestic to have 160 power plant, the condensed water precision processing system application of 350 units
The system.For high tower separation technique system compared with other systems, design principle is simpler, with only the waterpower principle of stratification
And resin partial size difference different with the specific gravity of positive negative resin separates positive negative resin.High tower separation technique system includes: mixed
Bed unit, by-pass unit, recirculation pump unit, regeneration unit (three towers), flush water pump unit, roots blower unit, soda acid storage
Memory cell, soda acid metering units, valve, pipeline, resin, stored program controlled, instrument, electrical etc..
Summary of the invention
Negative resin and positive resin are sufficiently separated purpose of the utility model is to overcome the above-mentioned shortcomings and provide a kind of, and
And wherein contain a small amount of impurity, so that negative resin and positive resin is timely and effectively obtained regenerated Ion exchange resin high tower segregative line
System.
Purpose of the utility model is realized as follows:
A kind of Ion exchange resin high tower separation system, the system comprises separation system and regenerative system, the separation
System includes knockout tower, separation assembly, exhausted resin pipeline, upper rinsing module and lower rinsing module, the top of the knockout tower
Portion is connected to the separation assembly, and the separation assembly includes stirring motor, agitating shaft and stirring blade, the stirring motor
It is located at the top of the knockout tower, the output shaft of the stirring motor is connected to the agitating shaft, and the agitating shaft extends to institute
It states in knockout tower, the stirring blade is fixed on the agitating shaft, and the top of the knockout tower is connected to upper rinsing module, described
The bottom of knockout tower is connected to the lower rinsing module, and the upper rinsing module includes upper flushing pipe, and the upper flushing pipe connects
It leads in the knockout tower, at circular configuration, the lower rinsing module includes lower flushing pipe for the end of the upper flushing pipe,
The end of the lower flushing pipe also rounded structure, the upper flushing pipe is parallel with the end of lower flushing pipe, and described point
Top from tower is connected to exhausted resin pipeline, is additionally provided with exhaust outlet at the top of the knockout tower, the separation tower side wall is communicated with
The height of negative resin output channel and positive resin output channel, the negative resin output channel is higher than the positive resin output channel
Height, the negative resin output channel and positive resin output channel be communicated to regenerative system, and the regenerative system includes yin
Resin lives again tower and positive resin is lived again tower, the negative resin are lived again in tower filled with alkaline solution, and the positive resin is lived again in tower
Filled with acid solution.
As a preference, being connected to check valve on the upper flushing pipe and lower flushing pipe.
As a preference, the knockout tower tower wall be coated with erosion shield, the erosion shield from inside to outside according to
It is secondary be equipped with macromolecule membrane layer, gel layer one, nickel phosphorus molybdenum disulfide composite coating, gel layer two, aluminium powder layer, epoxy paint layer,
Adhesive layer and polyethylene layer and waterproof layer.
Compared with prior art, the utility model has the beneficial effects that
The utility model is provided with separation system and regenerative system, and wherein separation system includes knockout tower, wherein knockout tower
Including separation assembly.Exhausted resin is transported in knockout tower by upper rinsing module and lower rinsing module, first exhausted resin pipeline,
Then upper rinsing module is passed through air and liquid cleans exhausted resin, in order to guarantee that resin can completely and impurity
Separation, the utility model are added to separation assembly, and separation assembly includes stirring motor and agitating shaft, and stirring motor drives agitating shaft
Sufficiently rotation, can make gas adequately be in contact with exhausted resin, to complete the separation of resin and impurity, contain impurity
For sewage by the water outlet outflow of separation tower bottom, the lower flushing group and upper rinsing module carry out water distribution and gas distribution simultaneously, complete
At the layering of resin, the resin after layering passes through negative resin output channel respectively and positive resin output channel is communicated to regeneration system
System, regenerative system negative resin and positive resin are regenerated.Negative resin and positive resin are sufficiently separated by the utility model, and wherein
Containing a small amount of impurity, regenerate negative resin and positive resin timely and effectively.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model;
Fig. 2 is the structural schematic diagram of the detection components of the utility model;
In figure: 1, knockout tower;2, stirring motor;3, agitating shaft;4, stirring blade;5, upper flushing pipe;6, lower flushing pipe
Road;7, exhaust outlet;8, check valve;9, negative resin output channel;10, positive resin output channel;11, negative resin is lived again tower;12, positive
Resin is lived again tower;13, camera;14, detection hole;15, transparent glass;16, detection framework;17, motorized rails;18, controller;
19, exhausted resin pipeline.
Specific embodiment
A kind of embodiment provided by the utility model referring to FIG. 1-2:
A kind of Ion exchange resin high tower separation system, the system comprises separation system and regenerative system, the separation
System includes knockout tower 1, separation assembly, exhausted resin pipeline 19, upper rinsing module and lower rinsing module, the knockout tower 1
Top be connected to the separation assembly, the separation assembly includes stirring motor 2, agitating shaft 3 and stirring blade 4, described
Stirring motor 2 is located at the top of the knockout tower 1, and the output shaft of the stirring motor 2 is connected to the agitating shaft 3, described to stir
It mixes axis 3 to extend in the knockout tower 1, the stirring blade 4 is fixed on the agitating shaft 3, and the top of the knockout tower 1 connects
Logical upper rinsing module, the bottom of the knockout tower 1 are connected to the lower rinsing module, and the upper rinsing module includes upper flushing pipe
5, the upper flushing pipe 5 is communicated in the knockout tower 1, and the end of the upper flushing pipe 5 is at circular configuration, the undershoot
Washing component includes lower flushing pipe 6, the end of the lower flushing pipe 6 also rounded structure, the upper flushing pipe 5 and undershoot
The end for washing pipeline 6 is parallel, and the top of the knockout tower 1 is connected to exhausted resin pipeline 19, and the top of the knockout tower 1 is also set
There is exhaust outlet 7,1 side wall of knockout tower is communicated with negative resin output channel 9 and positive resin output channel 10, and the negative resin is defeated
The height of pipeline 9 is higher than the height of the positive resin output channel 10, the negative resin output channel 9 and positive resin efferent duct out
Road 10 is communicated to regenerative system, and the regenerative system includes that negative resin lives again tower 11 and positive resin is lived again tower 12, the yin tree
Rouge is lived again, and tower 11 is interior filled with alkaline solution, and the positive resin is lived again, and tower 12 is interior to be filled with acid solution.
In the present embodiment, the other side of the knockout tower be equipped with detection components, the inspection component include camera 13,
Detection hole 14 and detection framework 16, the detection framework 16 are located at the tower outer wall of the knockout tower 1, edge in the detection hole 14
Embedded with transparent glass 15, the detection framework 16 is equipped with motorized rails 17, and the motorized rails 17 are slidably connected a sliding block, institute
It is fixed on the slide block to state camera 13, the length of the detection hole 14 is more than the length of 1 half of knockout tower.
In the present embodiment, a controller 18 is additionally provided on the knockout tower 1, the camera 13 is connected to controller 18
Input terminal, the check valve 8 is connected to the output end of controller 18.
In the present embodiment, check valve 8 is connected on the upper flushing pipe 5 and lower flushing pipe 6.
In the present embodiment, 1 tower wall of knockout tower be coated with erosion shield, the erosion shield from inside to outside according to
It is secondary be equipped with macromolecule membrane layer, gel layer one, nickel phosphorus molybdenum disulfide composite coating, gel layer two, aluminium powder layer, epoxy paint layer,
Adhesive layer and polyethylene layer and waterproof layer, wherein be uniformly provided in the epoxy paint layer epoxy resin, coal tar pitch and
Curing agent
Working principle: the utility model is provided with separation system and regenerative system, and wherein separation system includes knockout tower,
Middle knockout tower includes separation assembly.Upper rinsing module and lower rinsing module, first exhausted resin pipeline 19 convey exhausted resin
Into knockout tower 1, then upper rinsing module is passed through air and liquid cleans exhausted resin, in order to guarantee resin energy
Enough to separate completely with impurity, the utility model is added to separation assembly, and separation assembly includes stirring motor 2 and agitating shaft 3, stirs
Mix motor 2 drive agitating shaft 3 sufficiently rotate, gas can be made adequately to be in contact with exhausted resin, thus complete resin with it is miscellaneous
The separation of matter, the sewage containing impurity are flowed out by the water outlet of 1 bottom of knockout tower, the lower rinsing module and upper rinsing module
Water distribution and gas distribution are carried out simultaneously, completes the layering of resin, the resin after layering passes through negative resin output channel 9 and positive resin respectively
Output channel 10 is communicated to regenerative system, and regenerative system regenerates negative resin and positive resin.The utility model is by negative resin
It is sufficiently separated with positive resin, and wherein contains a small amount of impurity, regenerate negative resin and positive resin timely and effectively.
Although the utility model is described in detail with reference to the foregoing embodiments, come for those skilled in the art
Say, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic into
Row equivalent replacement, within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on should all
It is included within the scope of protection of this utility model.
Claims (3)
1. a kind of Ion exchange resin high tower separation system, it is characterised in that: the system comprises separation system and regenerative system,
The separation system includes knockout tower (1), separation assembly, exhausted resin pipeline (19), upper rinsing module and lower rinsing module,
Be connected to the separation assembly at the top of the knockout tower (1), the separation assembly include stirring motor (2), agitating shaft (3) with
And stirring blade (4), the stirring motor (2) are located at the top of the knockout tower (1), the output shaft of the stirring motor (2)
It is connected to the agitating shaft (3), the agitating shaft (3) extends in the knockout tower (1), and the stirring blade (4) is fixed on
On the agitating shaft (3), the top of the knockout tower (1), which is connected to, goes up rinsing module, described in the bottom connection of the knockout tower (1)
Lower rinsing module, the upper rinsing module include upper flushing pipe (5), and the upper flushing pipe (5) is communicated to the knockout tower
(1) in, at circular configuration, the lower rinsing module includes lower flushing pipe (6), described for the end of the upper flushing pipe (5)
The end of lower flushing pipe (6) also rounded structure, the upper flushing pipe (5) is parallel with the end of lower flushing pipe (6), institute
Top connection exhausted resin pipeline (19) of knockout tower (1) is stated, is additionally provided with exhaust outlet (7) at the top of the knockout tower (1), it is described
Knockout tower (1) side wall is communicated with negative resin output channel (9) and positive resin output channel (10), the negative resin output channel
(9) height is higher than the height of the positive resin output channel (10), the negative resin output channel (9) and positive resin efferent duct
Road (10) is communicated to regenerative system, and the regenerative system includes that negative resin lives again tower (11) and positive resin is lived again tower (12), institute
It states negative resin to live again filled with alkaline solution in tower (11), the positive resin is lived again in tower (12) filled with acid solution.
2. a kind of Ion exchange resin high tower separation system according to claim 1, it is characterised in that: the upper flushing pipe
(5) and on lower flushing pipe (6) it is connected to check valve (8).
3. a kind of Ion exchange resin high tower separation system according to claim 1, it is characterised in that: the knockout tower (1)
Tower wall is coated with erosion shield, and the erosion shield is successively arranged macromolecule membrane layer, gel layer one, nickel phosphorus from inside to outside
Molybdenum disulfide composite coating, gel layer two, aluminium powder layer, epoxy paint layer, adhesive layer and polyethylene layer and waterproof layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820209843.6U CN208292708U (en) | 2018-02-06 | 2018-02-06 | A kind of Ion exchange resin high tower separation system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820209843.6U CN208292708U (en) | 2018-02-06 | 2018-02-06 | A kind of Ion exchange resin high tower separation system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208292708U true CN208292708U (en) | 2018-12-28 |
Family
ID=64697593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820209843.6U Expired - Fee Related CN208292708U (en) | 2018-02-06 | 2018-02-06 | A kind of Ion exchange resin high tower separation system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208292708U (en) |
-
2018
- 2018-02-06 CN CN201820209843.6U patent/CN208292708U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102764583B (en) | Process of dual-circulation single-tower desulfurization systems | |
CN109174752A (en) | A kind of cleaning pole plate of storage battery device | |
CN208292708U (en) | A kind of Ion exchange resin high tower separation system | |
CN109851166B (en) | Internal circulation type anaerobic and denitrification methane-generating reactor and sewage treatment method | |
CN203170211U (en) | Ring-pipe rotational-flow wet-method flue gas desulfurization tower | |
CN202263695U (en) | Constant temperature retaining device | |
CN206219350U (en) | Mixed ion exchanger and water purifier | |
CN203598673U (en) | High-speed flue gas desulfurization, wet-type electric dust removal, and mist removal tower | |
CN104624029A (en) | Device for integrating cooling tower, desulfurizing tower and chimney, and desulfurizing method | |
CN202860398U (en) | Flue gas desulfurization device by magnesium oxide method | |
CN105214839A (en) | A kind of wet type demister | |
CN207628433U (en) | Backwash resin tower is exempted from a kind of resin regeneration | |
CN103691294A (en) | Device and technology for wet-type double-alkali method-based desulphurization and dedusting | |
CN206295680U (en) | A kind of ardealite filter protector | |
CN208082197U (en) | A kind of efficient waste gas filter | |
CN206463975U (en) | Chemical reaction pot waste gas negative pressure recovering device with spraying function | |
CN209475943U (en) | Desulfurizing tower is used in a kind of manufacture of fuel gas | |
CN211644853U (en) | Coal-fired power plant condensate water fine treatment system regeneration waste water zero discharge system | |
CN101734753B (en) | Picogram-level precision processing method of industrial condensed water | |
CN211420081U (en) | Condensate tank capable of removing impurities and separating water | |
CN208229659U (en) | A kind of novel chemical scrubber | |
CN2875569Y (en) | Waste gas purification device | |
CN103611406B (en) | The magnetic separating device of sulfur dioxide in flue gas and method | |
CN104276739B (en) | A kind of reinforcement sludge gravity concentration realize device and method | |
CN205109867U (en) | Wet -type defroster |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181228 Termination date: 20210206 |
|
CF01 | Termination of patent right due to non-payment of annual fee |