CN201002988Y - Double-tower type two-stage demineralizing equipment - Google Patents
Double-tower type two-stage demineralizing equipment Download PDFInfo
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- CN201002988Y CN201002988Y CNU2006201282453U CN200620128245U CN201002988Y CN 201002988 Y CN201002988 Y CN 201002988Y CN U2006201282453 U CNU2006201282453 U CN U2006201282453U CN 200620128245 U CN200620128245 U CN 200620128245U CN 201002988 Y CN201002988 Y CN 201002988Y
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Abstract
The utility model relates to a water desalination treatment device, in particular to a double-tower type second-level desalination device, which overcomes the defects of complex operation and highly demanded medicine dose consumption of the prior art, and comprises two ion exchangers; wherein, the two ion exchangers are respectively divided into two parts; the upper part is provided with a cation exchange resin tank body, namely a cation exchange unit, while the lower part is provided with an anion exchange resin tank body, namely an anion exchange resin unit; the cation exchange unit and the anion exchange unit are respectively overlapped to form two ion exchange towers; the first-level cation exchange unit and the second-level anion exchange unit form an ion exchange tower; whereas the second-level cation exchange unit and the first-level anion exchange unit are formed a second ion exchange tower. The utility model has the advantages of easy operation, safety, reliability, less medicine dose consumption and low construction expenses, as well as good regeneration effect, less regenerated waste liquid, and less externally discharged salt amount, thus greatly reducing environmental pollution.
Description
Technical field
The utility model relates to a kind of desalination treatment facility of water, specifically a kind of double-tower type two-stage desalting device.
Background technology
The salt processing method that removes of water has multiplely, and the ion-exchange demineralization method is China's a kind of method commonly used.But owing in the treating processes, consume a large amount of bronsted lowry acids and bases bronsted lowries and carry out regeneration of ion-exchange resin, and the regeneration waste liquid that regeneration back produces is the waste water of supersalinity, handles very difficultly, finally causes the pollution to natural stream networks.
In recent years, along with the development of water technology and the raising of environmental requirement, utilized reverse osmosis (RO) method desalination to begin widespread usage.But the ratio of desalinization of reverse osmosis method is generally 96%～99%, can not satisfy the needs of some industrial sectors, the needs of heat power plant boiler make up water particularly, thereby need further desalination again of rearmounted ion-exchange demineralization device.Rearmounted at present ion-exchange demineralization device mostly is the secondary mixed ion exchanger.Secondary mixed ion exchanger system as shown in Figure 1 (following mixed ion exchanger abbreviation mixes bed), reverse osmosis desalination plant water outlet origin water inlet 10 enters one-level and mixes bed 1, through the mixed bed 2 of secondary, draws the finished product pure water by finished product pure water water outlet 11 again.When regenerating after mixed bed 1 and 2 operational failures, introduce backwash water by bottom backwash water import 18, utilize the proportion difference of cationic, anionic exchange resin (hereinafter to be referred as resin), with its layering, positive resin 13 is following, and negative resin 12 is last.Acid solution by hydrochloric acid is stored and metering system 4 is introduced is entered by the bottom of mixing bed, therefrom arranges mechanism 14 and discharges, and positive resin 13 is regenerated; Alkali lye by caustic soda is stored and metering system 3 is introduced is entered by the top of mixing bed, therefrom arranges mechanism 14 and discharges, and negative resin 12 is regenerated.After the input of acid, alkali lye reaches set amount, introduce pure water by former pipeline again, the acid in the equipment, alkali lye are cemented out, after displacement is finished, carry out suitable draining, introduce pressurized air by compressed air tank 5, enter from mixing the bed bottom, two kinds of resins of yin, yang are stirred, mix; Water inlet 10 water inlets are always just being washed water port 19 and are being opened again, just wash, and after water outlet was qualified, two mixed beds 1 and 2 can be contacted and be put into operation.Mix acid, alkali wasteliquids of discharging bed 1 and 2 regeneration backs and enter neutralization tank 7, utilize acid adding machine structure 6 and online PH table 9, regulate the add-on of acid automatically, make pH value qualified after, stir and output pump 8 is discharged waste water by waste water.
During mixed ion exchanger regeneration, anion and cation exchange resin need be carried out layering and married operation during regeneration in same equipment, so complicated operation, causes crossed contamination easily.Cause the regeneration failure easily as careless manipulation.Regenerating acid and the consumption of regeneration alkali simultaneously is very high, and under the normal circumstances, the consumption of hydrochloric acid is 4.4 times of theoretical value, and the consumption of sodium hydroxide is 12.5 times of theoretical value.The acid of these surpluses, alkali will be discharged with regeneration waste liquid, in order to make draining keep neutral, need establish the pH value adjustment mechanism, still need in waste water, to add a large amount of acid solutions, so not only cause acid, alkali consumption big, working cost improves, and more seriously the salt of these high resolutions enters nature the most at last in the waste water, causes the pollution of natural stream networks.
Summary of the invention
The purpose of this utility model is to overcome existing desalination treatment facility complicated operation, the required high defective of reagent consumption, proposes a kind of double-tower type two-stage desalting device, and it is simple to operate, and is safe and reliable, and reagent consumption is few and cost of erection is low.
The utility model is to adopt following technical scheme to realize: a kind of double-tower type two-stage desalting device, comprise two ion-exchangers, wherein, respectively two ion-exchangers are divided into two, top is set to be equipped with the tank body of Zeo-karb, i.e. cationic exchange unit, and the bottom is set to be equipped with the tank body of anionite-exchange resin, be the anionresin unit, cationic exchange unit and anionresin unit superpose respectively and constitute two ion exchange towers.
In the utility model, one-level cationic exchange unit and secondary anionresin unit constitute an ion exchange tower, and secondary cationic exchange unit and one-level anionresin unit constitute second ion exchange tower.
In desalting process, come water inlet to be connected with one-level cationic exchange unit, one-level cationic exchange unit is by the water inlet water distribution mechanism on its discharge mechanism and top, one-level anionresin unit, be connected with one-level anionresin unit, one-level anionresin unit is connected with secondary cationic exchange unit by the discharge mechanism of its underpart, secondary cationic exchange unit is by the water inlet water distribution mechanism on its discharge mechanism and top, secondary anionresin unit, be connected with secondary anionresin unit, secondary anionresin unit is connected with finished product pure water water outlet by the discharge mechanism of its underpart.
In the Zeo-karb regenerative process, regeneration acid solution storage and metering system are connected with secondary cationic exchange unit, secondary cationic exchange unit is connected with the unitary bottom of one-level cationic exchange by the discharge mechanism of its underpart, and one-level cationic exchange unit is connected with the leakage fluid dram that is provided with in the middle by the middle mechanism of arranging.
In the anionite-exchange resin regenerative process, regeneration alkali lye storage and metering system are connected with secondary anionresin unit, secondary anionresin unit is connected with the unitary bottom of one-level anionresin by the discharge mechanism of its underpart, and one-level anionresin unit is connected with the leakage fluid dram that is provided with in the middle by the middle mechanism of arranging.
Described cationic exchange unit discharge mechanism adopts porous plate and a water cap and a tubular type, and anionresin unit discharge mechanism adopts quartz sand thickness.Wherein, the ion exchange resin that loads in the cationic exchange unit is having concurrently of strong acid sun type resin or weak acid sun type resin or both.The ion exchange resin that loads in the anionresin unit is having concurrently of the cloudy type resin of highly basic or the cloudy type resin of weak base or both.
Described ion exchange tower also can constitute primary demineralixation system by separate unit.
The beneficial effects of the utility model are: the regeneration of ion-exchange resin that realize by this device (1), and the waste liquid that discharge the regeneration back is neutral, waste water need be set transfer pH value mechanism; (2) required regenerative agent amount is theoretical value substantially in the regenerative process, reduce greatly than mixed ion exchanger: compare with the mixed ion exchanger of prior art, its acid consumption only is 23% of a mixed ion exchanger, and alkaline consumption only is 8% of a mixed ion exchanger; (3) regeneration waste liquid is few, and outer brine rate is few, has alleviated environmental pollution greatly; Zeo-karb is regenerated in different equipment respectively with anionite-exchange resin when (4) regenerating, and does not have crossed contamination, favorable regeneration effect, and operating capacity is big, and is simple to operate and safe and reliable; (5) construction cost is low, compares with the secondary mixed ion exchanger, handles the device of the same water yield, and cost of erection reduces about 20% approximately.
Be that certain installed capacity is the medium-sized fuel-burning power plant of 4 * 300MW condensing-type unit below, former water saltiness 1000 mg/litre of boiler water-filling, it need be prepared into pure water, as boiler water-filling, amount of makeup water is 120t/h, according to ratio of desalinization be 96% carry out reverse osmosis desalination after, rearmounted respectively secondary mixed ion exchanger and double-tower type two-stage desalting device compare.The water production rate of two kinds of desalination plants is 150t/h, and the cycle of operation is 30 hours, and all requires effluent quality to be: electric conductivity＜0.2ms/cm, silicon-dioxide＜0.02mg/l.Prove by example: the regeneration of ion-exchange resin specific consumption that utilizes the secondary mixed ion exchanger to be reached is:
Zeo-karb: 4.4 times of theoretical value
Anionite-exchange resin: 12.5 times of theoretical value
The regeneration of ion-exchange resin specific consumption that utilizes double-tower type two-stage desalting device to reach is:
Zeo-karb: 1.0 is theoretical value
Anionite-exchange resin: 1.0 is theoretical value
In addition, the contrast of the acid-base consumption of above-mentioned two examples and regenerative wastewater quantity discharged is as follows:
| Sequence number | Project | The secondary mixed ion exchanger | The double tower two-stage desalting device | Remarks |
| 1 | 30% hydrochloric acid consumption (ton/year) | 224.8 | 51.1 | |
| 2 | 30% caustic soda consumption (ton/year) | 700.00 | 56.0 | |
| 3 | Regenerative wastewater amount ( |
341.95 | 96.38 | |
| 4 | Regenerative wastewater is transferred the minimum acid consumption of pH value (ton/year) | 413.9 | 0 | |
| 5 | Year medicament expense (ten thousand yuan) | 80.32 | 6.426 | 600 yuan/ton in 600 yuan of/ton 30% caustic soda of 30% hydrochloric acid |
Description of drawings
Fig. 1 is the structural representation of the present secondary hybrid ionic exchange system of using always;
Fig. 2 is a structural representation of the present utility model.
Embodiment
Embodiment 1
As shown in Figure 2, the utility model is formed a secondary desalting system by two ion exchange towers, and wherein, one-level cationic exchange unit 1 and secondary anionresin unit 2 constitute first ion exchange tower; Secondary cationic exchange unit 3 constitutes second ion exchange tower with one-level anionresin unit 4.Cationic exchange unit 1 and 3 lays respectively at the top of ion exchange tower, and anionresin unit 2 and 4 lays respectively at the bottom of ion exchange tower.Cationic exchange unit 1 and 3 discharge mechanism 12 adopt cationic exchange unit porous plates 18 and a water cap and a tubular type, and anionresin unit 2 and 4 discharge mechanism adopt anionresin unit bottom bed course 14, and this bed course is a quartz sand thickness.Wherein, the ion exchange resin that loads in the cationic exchange unit is having concurrently of strong acid sun type resin or weak acid sun type resin or both.The ion exchange resin that loads in the anionresin unit is having concurrently of the cloudy type resin of highly basic or the cloudy type resin of weak base or both.
When carrying out desalination work by this device, whole device is work like this: the reverse osmosis desalination plant water outlet enters one-level cationic exchange unit 1 by coming water inlet 7, porous plate 18 in the discharge mechanism 12 of cationic exchange unit 1, the water inlet water distribution mechanism 15 on water cap and female arm and top, one-level anionresin unit enters one-level anionresin unit 4, then draw by the anionresin unit bottom bed course 14 of 4 bottoms, one-level anionresin unit, enter secondary cationic exchange unit 3, porous plate 18 in the discharge mechanism 12 of secondary cationic exchange unit 3 then, the water inlet water distribution mechanism 15 on water cap and female arm and 2 tops, secondary anionresin unit, enter secondary anionresin unit 2, draw the finished product pure water by finished product pure water water outlet 8 at last.Finished desalting process by above step.
After Zeo-karb in the device (hereinafter to be referred as positive resin) and anionite-exchange resin (hereinafter to be referred as the negative resin) operational failure, need regenerate to positive resin and negative resin.Its middle-jiao yang, function of the spleen and stomach regeneration of resin process is: the acid solution of will regenerating, hydrochloric acid soln for example, draw by hydrochloric acid storage and metering system 5, enter secondary cationic exchange unit 3, flow into by its top, flow out from its underpart, it is the drag flow regenerative process, enter the bottom of one-level cationic exchange unit 1 by the discharge mechanism 12 of 3 bottoms, secondary cationic exchange unit, the middle row mechanism 11 in one-level cationic exchange unit is by leakage fluid dram 16 effluent discharges that are provided with in the middle, wherein in one-level cationic exchange unit 1, implement adverse current and starve regeneration, promptly the waste liquid when discharge is about to occur before the acidity, ends the acid operation, keeps effluent discharge one-tenth neutral.After the entering of regeneration acid solution finished, introduce pure water by former pipeline again, the acid solution in the equipment is cemented out, realized positive regeneration of resin.
The regenerative process of negative resin is: the alkali lye of will regenerating, caustic soda soln for example, draw by caustic soda storage and metering system 6, enter secondary anionresin unit 2, enter by its top, flow out from its underpart, it is the drag flow regenerative process, enter the bottom of one-level anionresin unit 4 by the bottom cushion 14 of 2 bottoms, secondary anionresin unit, the middle row mechanism 13 through one-level anionresin unit 4 is by leakage fluid dram 17 effluent discharges that are provided with in the middle, wherein in one-level anionresin unit 4, implement adverse current and starve regeneration, promptly the waste liquid when discharge is about to occur before the alkalescence, ends the alkali operation, keeps effluent discharge to become neutrality.After the entering of alkali lye of regenerating finished, introduce pure water by former pipeline again, the alkali lye in the equipment is cemented out.After positive resin and negative resin were finished replacement process, 7 water inlets of origin water inlet were contacted to device and just to be washed, and the wash water is discharged by just washing water port 19, were just washing to get final product normal operation input after qualified.
The utility model is simple to operate, and is safe and reliable, and reagent consumption is low, significantly reduced cost of erection, and regeneration waste liquid is few, outer brine rate is few, alleviated environmental pollution greatly, the postposition that can make reverse osmosis desalination plant is demineralization plant more further, replaces the secondary mixed ion exchanger.
Embodiment 2
In the utility model, the ion exchange tower of separate unit can constitute primary demineralixation system, and its principle of work is identical with embodiment 1.
Claims (7)
1, a kind of double-tower type two-stage desalting device, comprise two ion-exchangers, it is characterized in that: respectively two ion-exchangers are divided into two, top is set to be equipped with the tank body of Zeo-karb, it is the cationic exchange unit, the bottom is set to be equipped with the tank body of anionite-exchange resin, i.e. anionresin unit, cationic exchange unit and anionresin unit superpose respectively and constitute two ion exchange towers.
2, double-tower type two-stage desalting device according to claim 1 is characterized in that: but described ion exchange tower separate unit constitutes primary demineralixation system.
3, double-tower type two-stage desalting device according to claim 1, it is characterized in that: one-level cationic exchange unit and secondary anionresin unit constitute an ion exchange tower, and secondary cationic exchange unit and one-level anionresin unit constitute second ion exchange tower.
4, double-tower type two-stage desalting device according to claim 1, it is characterized in that: in desalting process, come water inlet to be connected with one-level cationic exchange unit, one-level cationic exchange unit is by the water inlet water distribution mechanism on its discharge mechanism and top, one-level anionresin unit, be connected with one-level anionresin unit, one-level anionresin unit is connected with secondary cationic exchange unit by the discharge mechanism of its underpart, secondary cationic exchange unit is by the water inlet water distribution mechanism on its discharge mechanism and top, secondary anionresin unit, be connected with secondary anionresin unit, secondary anionresin unit is connected with finished product pure water water outlet by the discharge mechanism of its underpart.
5, double-tower type two-stage desalting device according to claim 1, it is characterized in that: in the Zeo-karb regenerative process, regeneration acid solution storage and metering system are connected with secondary cationic exchange unit, secondary cationic exchange unit is connected with the unitary bottom of one-level cationic exchange by the discharge mechanism of its underpart, and one-level cationic exchange unit is connected with the leakage fluid dram that is provided with in the middle by the middle mechanism of arranging.
6, double-tower type two-stage desalting device according to claim 1, it is characterized in that: in the anionite-exchange resin regenerative process, regeneration alkali lye storage and metering system are connected with secondary anionresin unit, secondary anionresin unit is connected with the unitary bottom of one-level anionresin by the discharge mechanism of its underpart, and one-level anionresin unit is connected with the leakage fluid dram that is provided with in the middle by the middle mechanism of arranging.
7, according to claim 4,5 or 6 described double-tower type two-stage desalting devices, it is characterized in that: described cationic exchange unit discharge mechanism adopts porous plate and a water cap and a tubular type, and anionresin unit discharge mechanism adopts quartz sand thickness.
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2006201282453U CN201002988Y (en) | 2006-11-24 | 2006-11-24 | Double-tower type two-stage demineralizing equipment |
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| CNU2006201282453U CN201002988Y (en) | 2006-11-24 | 2006-11-24 | Double-tower type two-stage demineralizing equipment |
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| CN201002988Y true CN201002988Y (en) | 2008-01-09 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102653426A (en) * | 2011-03-03 | 2012-09-05 | 彭悦 | Demineralized water device of six-tower fluidized bed |
| CN109052435A (en) * | 2018-09-27 | 2018-12-21 | 中蓝长化工程科技有限公司 | A kind of adsorption tower group mentioning lithium for salt lake bittern |
| CN109796063A (en) * | 2019-02-18 | 2019-05-24 | 湖南海富环境污染治理有限公司 | A kind of shallow demineralizer of integration |
-
2006
- 2006-11-24 CN CNU2006201282453U patent/CN201002988Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102653426A (en) * | 2011-03-03 | 2012-09-05 | 彭悦 | Demineralized water device of six-tower fluidized bed |
| CN109052435A (en) * | 2018-09-27 | 2018-12-21 | 中蓝长化工程科技有限公司 | A kind of adsorption tower group mentioning lithium for salt lake bittern |
| CN109796063A (en) * | 2019-02-18 | 2019-05-24 | 湖南海富环境污染治理有限公司 | A kind of shallow demineralizer of integration |
| CN109796063B (en) * | 2019-02-18 | 2021-07-13 | 湖南海富环境污染治理有限公司 | Shallow desalination device of integration |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080109 Termination date: 20091224 |