CN202379787U - Adjusting system of potential of hydrogen of percolate - Google Patents
Adjusting system of potential of hydrogen of percolate Download PDFInfo
- Publication number
- CN202379787U CN202379787U CN2011204597691U CN201120459769U CN202379787U CN 202379787 U CN202379787 U CN 202379787U CN 2011204597691 U CN2011204597691 U CN 2011204597691U CN 201120459769 U CN201120459769 U CN 201120459769U CN 202379787 U CN202379787 U CN 202379787U
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- Prior art keywords
- percolate
- potential
- water pot
- former water
- acid
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 36
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 36
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 239000002253 acid Substances 0.000 claims abstract description 34
- 238000013019 agitation Methods 0.000 claims description 10
- 238000001223 reverse osmosis Methods 0.000 claims description 7
- 230000035939 shock Effects 0.000 claims description 3
- 238000003756 stirring Methods 0.000 abstract description 19
- 239000007788 liquid Substances 0.000 abstract description 5
- 238000004134 energy conservation Methods 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 11
- 230000008021 deposition Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to an adjusting system of the potential of hydrogen of percolate. The adjusting system comprises a raw water tank, a liquid inlet pipe, an acid tank and an acid injecting pump, wherein the liquid inlet pipe is connected with the raw water tank, and the acid injecting pump is connected with the liquid inlet pipe and the acid tank, so that acid in the acid tank is injected into the liquid inlet pipe. By adoption of the technical scheme of the utility model, the percolate is mixed with the acid before entering the raw water tank, so that the hydraulic stirring in the raw water tank is greatly reduced, and the purposes of energy conservation and emission reduction are realized.
Description
Technical field
The utility model relates to percolate reverse-osmosis treated field, especially relates to a kind of percolate potential of hydrogen regulation system.
Background technology
In the percolate reverse osmosis treatment system; Percolate in the former water pot need carry out potential of hydrogen to it and regulate before getting into the film system handles, makes its potential of hydrogen reach the technical requirements of reverse osmosis membrane; To prevent that the ion in the percolate from producing deposition on film, stop up the work-ing life that fenestra influences film.
As shown in Figure 1, the mode of common adjusting percolate potential of hydrogen realizes through directly in former water pot, adding acid; Concrete operations are: percolate is before getting into film processing system; At first be evacuated to percolate in the former water pot, directly in former water pot, add acid simultaneously, and in former water pot, utilize fluid power to stir; Percolate and acid in the former water pot are mixed equably, to reach the potential of hydrogen that meets the demands.
Yet, directly in former water pot, adding acid, not comprovincial potential of hydrogen differs bigger in the former water pot, needs long-time stirring just can make the potential of hydrogen of liquid in the former water pot reach uniformity, and therefore, energy consumption, noise are higher, and system handles efficient is low, aquifer yield is low.In addition, carry out long fluid power circulation and stir, percolate can produce a large amount of bubbles, and bubble is discharged through venting port, produces severe contamination.
Summary of the invention
In view of this, the utility model provides a kind of percolate potential of hydrogen regulation system of energy-saving and emission-reduction.
A kind of percolate potential of hydrogen regulation system comprises former water pot, liquid-inlet pipe, acid jar, annotates sour pump, and said liquid-inlet pipe connects former water pot.The sour pump of said notes is connected with the acid jar so that liquid-inlet pipe is injected in the acid of acid jar interior splendid attire with liquid-inlet pipe.
Preferably, said percolate potential of hydrogen regulation system also comprises pipe stirrer, and said pipe stirrer is arranged on the liquid-inlet pipe, and is positioned at the rear end of the notes acid point of liquid-inlet pipe.
Preferably, be provided with impeller in the said pipe stirrer, said impeller is rotatable under the shock action of flow.
Preferably, in the said former water pot hydraulic agitator is set.
Preferably, be combined with drain pipe bottom the said former water pot.
Preferably, on the said drain pipe waterflood pump is set, said waterflood pump is positioned at the front end of reverse osmosis treatment system.
Preferably, said percolate potential of hydrogen regulation system also comprises the agitation cycle valve, and said agitation cycle valve is controlled the start and stop of hydraulic agitator according to the potential of hydrogen of the percolate that flows out waterflood pump.
Preferably, when the potential of hydrogen of the percolate in the former water pot met the requirements, the agitation cycle valve was closed, and the hydraulic agitator in the former water pot stops to stir; When the potential of hydrogen of the percolate in the former water pot was undesirable, the agitation cycle valve was opened, and the hydraulic agitator in the former water pot starts and stirs.
Preferably, said former water pot top is provided with vapor pipe.
Preferably, on the said former water pot riser is set.
Compared with prior art, the utility model promptly mixed with acid before percolate gets into former water pot, therefore; Can significantly reduce the fluid power that in former water pot, carries out stirs; Thereby cut down the consumption of energy and noise, and reduce fluid power and stir the bubble that is produced, help protecting environment.
Above-mentioned explanation only is the general introduction of the utility model technical scheme; In order more to know the technique means of understanding the utility model; And can implement according to the content of specification sheets; And for let the above-mentioned of the utility model and other purposes, feature and advantage can be more obviously understandable, below in conjunction with accompanying drawing the utility model is elaborated.
Description of drawings
Fig. 1 is the synoptic diagram of existing percolate potential of hydrogen regulation system.
Fig. 2 is the synoptic diagram of the percolate potential of hydrogen regulation system that provided of the utility model embodiment.
Embodiment
See also Fig. 2, the percolate potential of hydrogen regulation system that the utility model embodiment is provided comprises former water pot 110, liquid-inlet pipe 120, acid jars 130, annotate sour pump 140, pipe stirrer 150, drain pipe 160, waterflood pump 170, agitation cycle valve 180, hydraulic agitator 190 and vapor pipe 210 and riser 220.
Liquid-inlet pipe 120 connects former water pot 110 tops, so that in former water pot 110, inject percolate.Annotate sour pump 140 and be connected with acid jar 130 with liquid-inlet pipe 120, liquid-inlet pipe 120 is injected in the acid of splendid attire in the acid jar 130, make percolate and acid mixing in liquid-inlet pipe 120 through pipeline (not label).Pipe stirrer 150 is arranged on the liquid-inlet pipe 120, and is positioned at the rear end of the notes acid point of liquid-inlet pipe 120.Be provided with impeller 152 in the pipe stirrer 150, impeller 152 rotates under the shock action of flow, and the percolate and the acid of the pipe stirrer 150 of flowing through are fully stirred, and need not other power.When needing in former water pot 110, to inject percolate; Acid in the acid jars 130 get into liquid-inlet pipe 120 down and mix with percolate liquid-inlet pipe 120 in the effect of annotating sour pump 140, get in the former water pot 110 for use after the percolate that mixes and sour fully stirs in pipe stirrer 150 together.
In the utility model, because acid is in liquid-inlet pipe 120 and the percolate blended, therefore, the utility model can reduce the fluid power that in former water pot 110, carries out and stir.Further; On liquid-inlet pipe 120, be provided with pipe stirrer 150; Percolate fully stirred through pipe stirrer 150 before getting into former water pot 110; Even it is undesirable to get into the potential of hydrogen of percolate of former water pot 110, also only needs stir a little and get final product with former water pot 110 interior hydraulic agitators 190.Therefore, the fluid power of hydraulic agitator 190 stirs intermittently and carries out, even hydraulic agitator 190 can not move for a long time, and not only energy consumption is little, noise is low, and is stirred and also corresponding will lacking of bubble of producing by fluid power, reduces the pollution to environment.In addition, reduce, help the deposition of percolate in former water pot 110, alleviate the load of reverse osmosis membrane because the fluid power of former water pot 110 stirs.
Compared with prior art; The utility model promptly mixed with acid before percolate gets into former water pot 110, and had carried out sufficient stirring, therefore; Can significantly reduce the fluid power that in former water pot 110, carries out stirs; Thereby cut down the consumption of energy and noise, and reduce fluid power and stir the bubble that is produced, help protecting environment.
More than combine accompanying drawing to describe the preferred implementation of the utility model, but the utility model is not limited to the detail in the above-mentioned embodiment.In the technical conceive scope of the utility model, can carry out multiple simple change and adjustment to the technical scheme of the utility model, these variations and adjustment all belong to the protection domain of the utility model.
Claims (9)
1. a percolate potential of hydrogen regulation system comprises former water pot, liquid-inlet pipe, acid jar, annotates sour pump, and said liquid-inlet pipe connects former water pot, it is characterized in that: the sour pump of said notes is connected with the acid jar so that liquid-inlet pipe is injected in the acid of acid jar interior splendid attire with liquid-inlet pipe.
2. percolate potential of hydrogen regulation system according to claim 1 is characterized in that: also comprise pipe stirrer, said pipe stirrer is arranged on the liquid-inlet pipe, and is positioned at the rear end of the notes acid point of liquid-inlet pipe.
3. percolate potential of hydrogen regulation system according to claim 2 is characterized in that: be provided with impeller in the said pipe stirrer, said impeller is rotatable under the shock action of flow.
4. percolate potential of hydrogen regulation system according to claim 1 is characterized in that: in the said former water pot hydraulic agitator is set.
5. percolate potential of hydrogen regulation system according to claim 4 is characterized in that: said former water pot bottom is combined with drain pipe.
6. percolate potential of hydrogen regulation system according to claim 5 is characterized in that: on the said drain pipe waterflood pump is set, said waterflood pump is positioned at the front end of reverse osmosis treatment system.
7. percolate potential of hydrogen regulation system according to claim 6; It is characterized in that: said percolate potential of hydrogen regulation system also comprises the agitation cycle valve, and said agitation cycle valve is controlled the start and stop of hydraulic agitator according to the potential of hydrogen of the percolate that flows out waterflood pump.
8. percolate potential of hydrogen regulation system according to claim 1 is characterized in that: said former water pot top is provided with vapor pipe.
9. percolate potential of hydrogen regulation system according to claim 1 is characterized in that: said former water pot upper end is provided with riser.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204597691U CN202379787U (en) | 2011-11-18 | 2011-11-18 | Adjusting system of potential of hydrogen of percolate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204597691U CN202379787U (en) | 2011-11-18 | 2011-11-18 | Adjusting system of potential of hydrogen of percolate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202379787U true CN202379787U (en) | 2012-08-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204597691U Expired - Fee Related CN202379787U (en) | 2011-11-18 | 2011-11-18 | Adjusting system of potential of hydrogen of percolate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202379787U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502938A (en) * | 2011-11-18 | 2012-06-20 | 中联重科股份有限公司 | Leachate pH value adjusting system and adjusting method thereof |
-
2011
- 2011-11-18 CN CN2011204597691U patent/CN202379787U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502938A (en) * | 2011-11-18 | 2012-06-20 | 中联重科股份有限公司 | Leachate pH value adjusting system and adjusting method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120815 Termination date: 20151118 |
|
| EXPY | Termination of patent right or utility model |