CN207051292U - For separating the experimental rig of anion and cation exchange resin - Google Patents
For separating the experimental rig of anion and cation exchange resin Download PDFInfo
- Publication number
- CN207051292U CN207051292U CN201720781369.XU CN201720781369U CN207051292U CN 207051292 U CN207051292 U CN 207051292U CN 201720781369 U CN201720781369 U CN 201720781369U CN 207051292 U CN207051292 U CN 207051292U
- Authority
- CN
- China
- Prior art keywords
- exchange resin
- resin
- cation exchange
- anion
- experimental rig
- 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
It the utility model is related to water-treatment technology field, it is more particularly to a kind of for separating the moon, the experimental rig of cationic ion-exchange resin, including splitter, the splitter includes being used to accommodate layering the moon, the receiving portion of cationic ion-exchange resin and for conveying the moon, the delivery section of cationic ion-exchange resin, the delivery section connects with the bottom of described accommodation section, the end of the delivery section is provided with resin flow export, the delivery section is sequentially provided with batterfly clack core and cock along resin stream outgoing direction, the batterfly clack core is connected with swing arm, for driving the batterfly clack core to rotate by rotating the swing arm, the transfer passage of the delivery section is set to be in closed or unimpeded state.The utility model can greatly save the time of anion and cation exchange resin layering, and reduce resin usage amount, wastage, and brand-new operating method is provided for the work of laboratory anion and cation exchange resin layered weighting.
Description
Technical field
Water-treatment technology field is the utility model is related to, more particularly to it is a kind of for separating anion and cation exchange resin
Experimental rig.
Background technology
Ion exchange resin is that power industry water treatment system uses one of important materials extensive, that investment is big.Ion is handed over
The quality for changing resin property directly affects demineralization plant water outlet quality and the economy of operation, influences the safety fortune of heat power equipment
OK.Therefore, in order to safe and efficient production must monitor operation resin performance.Yin, yang resin needs elder generation in the mixed bed of censorship laboratory
It could separately be detected respectively according to corresponding standard, and not have effective laboratory resin separator at present and carry out in fact
Operation is tested, causes the detection of resin in mixed bed to need substantial amounts of resin sample, operation difficulty is big, and precision is low, directly affects follow-up
The detection of resin property.Therefore, need a kind of device suitable for the separation of laboratory anion and cation exchange resin badly, improve mixed bed
The precision and efficiency of resin property detection.
Utility model content
Handed in order to solve the above technical problems, the purpose of this utility model is to provide a kind of laboratory anions and canons that are applied to
The device of resin separation is changed, saves the time of anion and cation exchange resin layering, and reduces resin usage amount, wastage, is improved
The efficiency and precision of mixed-bed resin performance detection.
The utility model provides a kind of experimental rig for being used to separate anion and cation exchange resin, including splitter, point
Include being used to accommodate from post being layered the receiving portion of anion and cation exchange resin and for conveying the defeated of anion and cation exchange resin
Portion is sent, delivery section connects with the bottom of receiving portion, and the end of delivery section is provided with resin flow export, and delivery section is along resin stream outgoing direction
Batterfly clack core and cock are sequentially provided with, batterfly clack core is connected with swing arm, for driving the batterfly clack by rotating swing arm
Core rotates, and the transfer passage of delivery section is in closed or unimpeded state.
Further, cock is glass cock, and the transfer passage for making delivery section by rotation is in closed or unimpeded
State.
Further, the agitator for being used for stirring anion and cation exchange resin is provided with receiving portion.
Further, agitator is double-layered stirrer.
Further, the periphery wall of batterfly clack core is provided with sealing ring.
Further, the device also includes support, and splitter is fixedly connected with the support.
Further, support is connected with clip, the outer wall clamping of clip and receiving portion.
Further, the device also includes resin jigger, and resin jigger is located at the lower section of resin flow export.
Further, splitter is lucite splitter.
By such scheme, by this device, the time of anion and cation exchange resin layering can be greatlyd save, and reduce
Resin usage amount, wastage, brand-new operating method is provided for the work of laboratory anion and cation exchange resin layered weighting.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and being practiced according to the content of specification, with preferred embodiment of the present utility model and coordinate accompanying drawing detailed below
Describe in detail bright as after.
Brief description of the drawings
Fig. 1 is the structural representation that the utility model is used to separate the embodiment of experimental rig one of anion and cation exchange resin
Figure；
Fig. 2 is that the structure for another embodiment of experimental rig that the utility model is used to separate anion and cation exchange resin is shown
It is intended to；
Fig. 3 is that the structure for the experimental rig batterfly clack core that the utility model is used to separate anion and cation exchange resin is shown
It is intended to.
Label in figure：
1- lucite splitters；2- batterfly clack cores；3- sealing rings；4- cocks；5- resin flow exports；6- resins measure
Cup；7- supports；8- clips；9- agitators；21- swing arms.
Embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is used to illustrate the utility model, but is not limited to the scope of the utility model.
Join and shown in Fig. 1 to Fig. 3, present embodiments provide a kind of experimental rig for being used to separate anion and cation exchange resin,
Including lucite splitter 1, batterfly clack core 2, sealing ring 3, cock 4, resin flow export 5, resin jigger 6 with a scale,
Support 7, belt washer clip 8, double-deck dasher 9, lucite splitter 1 are the experimental provision main body (as shown in Figure 2),
Lower end installation batterfly clack core 2 at the reducing of lucite splitter 1, batterfly clack core 2 is connected with swing arm 21 (as shown in Figure 3),
By swing arm 21 butterfly flap core 2 can be driven to rotate, by rotating swing arm 21 batterfly clack core 2 can be driven to rotate, played
The function of resin is intercepted and discharges, it is simple to operate, and resin flow can be precisely controlled, sealing ring 3 is installed on batterfly clack sand
The surrounding of core 2, can play a part of sealing, ensure its rotation to being sealed at 180 ° between lucite splitter 1, resin can not flow
Under spill, cock 4 is located at the lower end of batterfly clack core 2, and the circulation of current and resin, cock 4 are can control by rotary glass cock 4
It can extract and be cleaned, and smear vaseline and keep lubrication, the bottom of lucite splitter 1 is resin flow export 5, with a scale
Resin jigger 6 is placed in 5 positive lower end of resin flow export, and for measuring the amount of resin isolated, support 7 is used to fix lucite
Splitter 1, belt washer clip 8 are installed on support 7, convenient and safe for fixing lucite splitter 1, can be achieved stable
Operation, double-deck dasher 9 are placed in lucite splitter 1, and agitation anions and canons exchange tree before being layered for resin
Fat, by double-deck dasher 9 resin layering before fully agitation resin, can make its all float get up after according to resin ratio
It is layered again.
The present embodiment by the way that batterfly clack core 2 and cock 4 are combined into composition integrated apparatus, install by batterfly clack core 2
Upper, cock 4 is arranged on down, and anion and cation exchange resin is according to different specific weight natural layering, sun in machine glass splitter 1
Ion ratio is great in lower floor, and anion proportion is small on upper strata, closes batterfly clack core 2 at the same time and cock 4 stirs resin simultaneously
Fully layering；Discharge water the repeated multiple times effect being layered completely with reaching when closing batterfly clack core 2 and opening cock 4；Same
When opening batterfly clack core 2 and cock 4, resin enters in resin jigger 6 with a scale with current.Can be significantly by the device
The time of anion and cation exchange resin layering is saved, and reduces resin usage amount, wastage, is exchanged for laboratory anions and canons
The work of resin layered weighting provides brand-new operating method.
In the present embodiment, the process of anion and cation exchange resin is separated using the device to be included：First, by organic glass
Glass splitter 1 is fixed on the support 7 of belt washer clip 8, and resin jigger 6 with a scale is placed in 5 positive lower end of resin flow export, and
Close batterfly clack core 2 and cock 4.Then, hybrid resin and pure water are poured into, makes pure water that resin be completely covered, inserts double-deck oar
Formula agitator 9 fully stirs resin, and it is about 100% to make its backwash expansion degree, pulls out double-deck dasher 9, anions and canons
Exchanger resin is smaller on upper strata in lower floor, negative resin proportion than great according to its proportion difference natural layering, positive resin.Keep butterfly
Valve core 2 is closed and opens cock 4, pure water outflow, so repeatedly this step with reach cleaning resin and ensure it is cloudy,
The purpose that cationic ion-exchange resin is fully layered.Finally, while batterfly clack core 2 and cock 4 are opened cause following positive resin
Flowed into pure water in resin jigger 6 with a scale, separately take resin jigger 6 with a scale to contain the negative resin then flowed out.Pass through
Above-mentioned separation process, scrapped according to DL/T 673-2015 thermal power plant water process with 001X7 storng-acid cation exchange resins
Standard, DL/T 807-2002 thermal power plant water process 201X7 strong-base anion-exchange resins Rejection standard and DL/T
519-2014 power plants water process spent ion exchange resin acceptance criteria, after being separated to mixed-bed resin, it can carry out respective
Performance detection, reach the purpose of the precision and efficiency that improve mixed-bed resin performance detection.
The experimental rig that the utility model is used to separate anion and cation exchange resin has the following technical effect that：
1st, the utility model is simple, convenient, safe, and laboratory separation anion and cation exchange resin can be achieved.
2nd, the utility model controls resin by the batterfly clack core with swing arm, and core is fabricated into butterfly flap, leads to
Swing arm control folding is crossed, it is simple in construction, it is easy to operate.
3rd, the utility model alternately coordinates the separation of control resin using batterfly clack core and cock, realizes resin layering
Carried out while with separating.
Described above is only preferred embodiment of the present utility model, is not limited to the utility model, it is noted that
For those skilled in the art, on the premise of the utility model technical principle is not departed from, can also do
Go out some improvement and modification, these improvement and modification also should be regarded as the scope of protection of the utility model.
Claims (9)
- A kind of 1. experimental rig for being used to separate anion and cation exchange resin, it is characterised in that including splitter, the separation Post includes being used for the receiving portion for accommodating layering anion and cation exchange resin and the conveying for conveying anion and cation exchange resin Portion, the delivery section connect with the bottom of described accommodation section, and the end of the delivery section is provided with resin flow export, the delivery section Batterfly clack core and cock are sequentially provided with along resin stream outgoing direction, the batterfly clack core is connected with swing arm, for passing through rotation The swing arm drives the batterfly clack core to rotate, and the transfer passage of the delivery section is in closed or unimpeded state.
- 2. the experimental rig according to claim 1 for being used to separate anion and cation exchange resin, it is characterised in that described Cock is glass cock, and the transfer passage for making the delivery section by rotation is in closed or unimpeded state.
- 3. the experimental rig according to claim 1 for being used to separate anion and cation exchange resin, it is characterised in that described The agitator for being used for stirring anion and cation exchange resin is provided with receiving portion.
- 4. the experimental rig according to claim 3 for being used to separate anion and cation exchange resin, it is characterised in that described Agitator is double-layered stirrer.
- 5. the experimental rig according to claim 1 for being used to separate anion and cation exchange resin, it is characterised in that described The periphery wall of batterfly clack core is provided with sealing ring.
- 6. the experimental rig according to claim 1 for being used to separate anion and cation exchange resin, it is characterised in that also wrap Support is included, the splitter is fixedly connected with the support.
- 7. the experimental rig according to claim 6 for being used to separate anion and cation exchange resin, it is characterised in that described Support is connected with clip, the outer wall clamping of the clip and described accommodation section.
- 8. the experimental rig according to claim 7 for being used to separate anion and cation exchange resin, it is characterised in that also wrap Resin jigger is included, the resin jigger is located at the lower section of the resin flow export.
- 9. the experimental rig according to claim 1 for being used to separate anion and cation exchange resin, it is characterised in that described Splitter is lucite splitter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720781369.XU CN207051292U (en) | 2017-06-30 | 2017-06-30 | For separating the experimental rig of anion and cation exchange resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720781369.XU CN207051292U (en) | 2017-06-30 | 2017-06-30 | For separating the experimental rig of anion and cation exchange resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207051292U true CN207051292U (en) | 2018-02-27 |
Family
ID=61495750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720781369.XU Expired - Fee Related CN207051292U (en) | 2017-06-30 | 2017-06-30 | For separating the experimental rig of anion and cation exchange resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207051292U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107505453A (en) * | 2017-06-30 | 2017-12-22 | 大唐东北电力试验研究所有限公司 | For separating the experimental rig of anion and cation exchange resin |
-
2017
- 2017-06-30 CN CN201720781369.XU patent/CN207051292U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107505453A (en) * | 2017-06-30 | 2017-12-22 | 大唐东北电力试验研究所有限公司 | For separating the experimental rig of anion and cation exchange resin |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207051292U (en) | For separating the experimental rig of anion and cation exchange resin | |
| CN102580363A (en) | Device for adding flocculant | |
| CN107505453A (en) | For separating the experimental rig of anion and cation exchange resin | |
| CN109406711A (en) | A kind of device for absorbing tail gas and its tail gas absorption method for SCR denitration performance detection | |
| CN206103869U (en) | Full -automatic integrated liquid fertilizer production facility | |
| CN208422243U (en) | Extract production line instructional device | |
| CN107410052A (en) | A kind of hydrogeneous water mixing drawing-in device of animal husbandry | |
| CN207042493U (en) | Regeneration of ion-exchange resin device | |
| CN109876707A (en) | Heavy metal passivation device in a kind of CHARACTERISTICS OF TAILINGS SAND | |
| CN107779397A (en) | A kind of intelligent anaerobic fermentation reaction system and its reaction method | |
| CN214150580U (en) | Liquid chromatographic column maintenance device | |
| CN210965104U (en) | Pilot scale glass reation kettle | |
| CN209092876U (en) | Chloride ion removal device in a kind of fused salt using ion-exchange | |
| CN209264665U (en) | A kind of device for absorbing tail gas for SCR denitration performance detection | |
| CN216771626U (en) | Device for online sampling and measuring sulfite of desulfurized slurry | |
| CN207342569U (en) | A kind of device for improving acid base concentration measurement result accuracy | |
| CN207970494U (en) | A kind of device improving extraction reaction efficiency | |
| CN207614702U (en) | Equipment is mixed in etching solution production | |
| CN207872085U (en) | A kind of proportioner for ternary material precursor production | |
| CN208213155U (en) | A kind of waterborne polyurethane resin highly effective reaction kettle | |
| CN106872231B (en) | Soil hydrophobic fulvic acid component extraction purification device | |
| CN110079439A (en) | A kind of cell isolation method based on two-freedom continuous centrifuge | |
| CN206355870U (en) | Lithium ion battery slurry tank and conjunction pulp grinder | |
| CN217189013U (en) | Water paint processing is with deciding than compounding device | |
| CN215610911U (en) | Double-layer tank type sand prevention stirring tank |
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: 20180227 Termination date: 20180630 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |