CN216837458U - Automatic regulating and treating system for boiler water - Google Patents
Automatic regulating and treating system for boiler water Download PDFInfo
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- CN216837458U CN216837458U CN202220351834.7U CN202220351834U CN216837458U CN 216837458 U CN216837458 U CN 216837458U CN 202220351834 U CN202220351834 U CN 202220351834U CN 216837458 U CN216837458 U CN 216837458U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 137
- 230000001105 regulatory effect Effects 0.000 title claims abstract description 11
- 239000011347 resin Substances 0.000 claims abstract description 52
- 229920005989 resin Polymers 0.000 claims abstract description 52
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 50
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 24
- 239000013505 freshwater Substances 0.000 claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 11
- 230000000844 anti-bacterial effect Effects 0.000 claims abstract description 10
- 239000003899 bactericide agent Substances 0.000 claims abstract description 10
- 238000011084 recovery Methods 0.000 claims abstract description 8
- 238000003475 lamination Methods 0.000 claims abstract description 6
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 238000011033 desalting Methods 0.000 claims abstract description 4
- 150000001450 anions Chemical class 0.000 claims description 28
- 150000001768 cations Chemical class 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 27
- 239000002455 scale inhibitor Substances 0.000 claims description 7
- 238000011010 flushing procedure Methods 0.000 claims description 6
- 230000003750 conditioning effect Effects 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 6
- 230000002035 prolonged effect Effects 0.000 abstract description 5
- 241000894006 Bacteria Species 0.000 abstract description 4
- 238000004140 cleaning Methods 0.000 abstract description 4
- 239000008394 flocculating agent Substances 0.000 abstract description 4
- 244000005700 microbiome Species 0.000 abstract description 4
- 239000003814 drug Substances 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 230000002829 reductive effect Effects 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000009296 electrodeionization Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000002147 killing effect Effects 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
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Abstract
The utility model discloses an automatic regulating and treating system for boiler water, which comprises a raw water pipe, a raw water tank, a lamination filter, an ultrafiltration device, a security filter, a recovery water tank, a reverse osmosis device, a carbon remover, a fresh water tank, an anode bed, a cathode bed, a mixed bed, a resin catcher and a desalting water tank; the utility model has the advantages that: bacteria, microorganisms and suspended matters in raw water are cleaned by adding medicaments such as a bactericide, a flocculating agent, hydrochloric acid and the like, and the raw water is further filtered under the matching of a lamination filter, an ultrafiltration device, a security filter and a reverse osmosis device, so that the raw water meets the production requirement, the impurities in the water are reduced, the problem of equipment blockage is solved, the cleaning period is prolonged, and the working efficiency is ensured; during the operation of the water making equipment, the current processing capacity and processing efficiency of each equipment are met by adjusting the water inlet flow of the relevant equipment, the technical problem of overload operation of the equipment is solved, and the filtering effect of raw water is ensured.
Description
The technical field is as follows:
the utility model relates to a water treatment technical field, concretely relates to automatic adjustment processing system of boiler water.
Background art:
boiler feed water treatment plays crucial effect in the whole operation of boiler, has and improves the boiler and mends individual water quality for the steam quality of boiler can both be controlled within the standard value, thereby slows down the problem of scale deposit and corruption in the boiler, makes the relative extension of cleaning cycle, has guaranteed work efficiency.
The treatment mode of present boiler water is carried out through the mode of ultrafiltration + reverse osmosis + electrodeionization combination, however, long-term operation still can have the problem of equipment jam, in case equipment uses for a long time, the efficiency of handling will descend, and the flow can not be adjusted according to the condition of reality to the system moreover for equipment overload work, the safety of direct influence unit, healthy and steady operation lead to filterable effect also then to worsen moreover.
The utility model has the following contents:
an object of the utility model is to provide an automatically regulated processing system of boiler water.
The utility model discloses by following technical scheme implement: the automatic regulating and treating system for boiler water includes raw water pipe, raw water tank, laminated filter, ultrafilter, safety filter, recovering water tank, reverse osmosis unit, carbon eliminator, fresh water tank, cation bed, anion bed, mixed bed, resin catcher and desalting water tank;
the raw water pipe is communicated with the inlet of the raw water tank, the outlet of the raw water tank is communicated with the inlet of the laminated filter, the outlet of the laminated filter is communicated with the inlet of the ultrafiltration device, the produced water outlet of the ultrafiltration device is communicated with the inlet of the ultrafiltration water tank, the outlet of the ultrafiltration water tank is respectively communicated with the inlet of the security filter and the back flush inlet of the ultrafiltration device, the outlet of the security filter is communicated with the inlet of the reverse osmosis device, the produced water outlet of the reverse osmosis device is communicated with the inlet of the carbon remover, the outlet of the carbon remover is communicated with the inlet of the fresh water tank, the outlet of the fresh water tank is respectively communicated with the inlet of the cation bed and the back flush inlet of the reverse osmosis device, the outlet of the cation bed is communicated with the inlet of the anion bed, and the outlet of the anion bed is communicated with the inlet of the mixed bed, an outlet of the mixed bed is communicated with an inlet of the resin catcher, and an outlet of the resin catcher is communicated with an inlet of the desalting water tank;
the concentrated water outlet of the ultrafiltration device, the concentrated outlet of the reverse osmosis device, the flushing water outlet of the ultrafiltration device and the flushing water outlet of the reverse osmosis device are respectively communicated with the inlet of the recovery water tank.
Furthermore, a heater and a bactericide mixer are arranged on the raw water pipe.
Furthermore, a flocculating agent mixer is arranged on a pipeline between the raw water tank and the lamination filter.
Furthermore, a dosing mixer is arranged on a pipeline between the ultrafiltration water tank and the ultrafiltration device.
Furthermore, a scale inhibitor mixer is arranged on a pipeline between the ultrafiltration water tank and the cartridge filter.
Furthermore, a first liquid level meter is arranged on the raw water tank, a second liquid level meter is arranged on the ultrafiltration water tank, a third liquid level meter is arranged on the fresh water tank, a first electromagnetic flow valve is arranged on the raw water pipe, a second electromagnetic flow valve is arranged on a pipeline between the laminated filter and the ultrafiltration device, and a third electromagnetic flow valve is arranged on a pipeline between the fresh water tank and the cation bed;
the first liquid level meter, the second liquid level meter and the third liquid level meter are respectively electrically connected with the input end of a controller, and the output end of the controller is respectively electrically connected with the first electromagnetic flow valve, the second electromagnetic flow valve and the third electromagnetic flow valve.
Further, the device also comprises an anode bed resin transfer tank, wherein an inlet of the anode bed resin transfer tank is communicated with an outlet of the anode bed, and an outlet of the anode bed resin transfer tank is communicated with an inlet of the anode bed.
Further, still including the anion bed resin transfer jar, the anion bed resin transfer jar the entry with the export intercommunication of anion bed, the anion bed resin transfer jar the export with the entry intercommunication of anion bed.
Further, the device also comprises a mixed bed resin transfer tank, wherein an inlet of the mixed bed resin transfer tank is communicated with an outlet of the mixed bed, and an outlet of the mixed bed resin transfer tank is communicated with an inlet of the mixed bed.
The utility model has the advantages that: bacteria, microorganisms and suspended matters in raw water are cleaned by adding medicaments such as a bactericide, a flocculating agent, hydrochloric acid and the like, and the raw water is further filtered under the matching of a lamination filter, an ultrafiltration device, a security filter and a reverse osmosis device, so that the raw water meets the production requirement, the impurities in the water are reduced, the problem of equipment blockage is solved, the cleaning period is prolonged, and the working efficiency is ensured; during the water preparation equipment operation, according to the raw water tank liquid level trend that first level gauge detected, adjust first electromagnetic control valve's aperture, according to the ultrafiltration water tank liquid level trend that the second level gauge detected, adjust second electromagnetic control valve's aperture, according to the fresh water tank liquid level trend that the third level gauge detected, adjust third electromagnetic control valve's aperture, through the regulation to relevant equipment inflow, satisfy the current throughput and the treatment effeciency of each equipment, the technical problem of equipment overload operation has been solved, the steady of system has been guaranteed, the operation of safety, the life of equipment has been prolonged, guarantee the filter effect of raw water.
Description of the drawings:
in order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural view of the utility model;
in the figure: the device comprises a raw water pipe 1, a raw water tank 2, a heater 3, a bactericide mixer 4, a flocculant mixer 5, a dosing mixer 6, a laminated filter 7, an ultrafiltration device 8, an ultrafiltration water tank 9, a cartridge filter 10, a reverse osmosis device 11, a decarbonizer 12, a fresh water tank 13, a cation bed 14, an cation bed resin dump tank 141, a anion bed 15, an anion bed resin dump tank 151, a mixed bed 16, a mixed bed resin dump tank 161, a resin catcher 17, a desalted water tank 18, a recovery water tank 19, a first liquid level meter 20, a second liquid level meter 21, a third liquid level meter 22, a first electromagnetic flow valve 23, a second electromagnetic flow valve 24, a third electromagnetic flow valve 25, a controller 26 and a scale inhibitor mixer 27.
The specific implementation mode is as follows:
the technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
As shown in fig. 1, the automatic regulating and treating system for boiler water comprises a raw water pipe 1, a raw water tank 2, a laminated filter 7, an ultrafiltration device 8, a cartridge filter 10, a recovery water tank 19, a reverse osmosis device 11, a carbon remover 12, a fresh water tank 13, a cation bed 14, an anion bed 15, a mixed bed 16, a resin catcher 17 and a demineralized water tank 18;
the raw water pipe 1 is communicated with an inlet of a raw water tank 2, the raw water pipe 1 is provided with a heater 3 and a bactericide mixer 4, the heater 3 heats raw water to ensure that the raw water meets the optimal running state of a subsequent membrane system, the bactericide has the function of killing bacteria and microorganisms in the raw water and is sodium hypochlorite, the bactericide mixer 4, a flocculant mixer 5, a dosing mixer 6 and a scale inhibitor mixer 27 which are mentioned in the embodiment are all the existing static mixers, the method belongs to the prior art, the specific structure is not repeated, an outlet of the raw water tank 2 is communicated with an inlet of a laminated filter 7, a flocculant mixer 5 is arranged on a pipeline between the raw water tank 2 and the laminated filter 7, suspended matters in water are subjected to flocculation treatment by adding a flocculant, the suspended matters are cleaned through the laminated filter 7, and an outlet of the laminated filter 7 is communicated with an inlet of an ultrafiltration device 8, the water outlet of the ultrafiltration device 8 is communicated with the inlet of the ultrafiltration water tank 9, the ultrafiltration water tank 9 is used for storing the water treated by the ultrafiltration device 8 and adjusting the water yield of the ultrafiltration water tank 9 according to the working condition of subsequent equipment, the outlet of the ultrafiltration water tank 9 is respectively communicated with the inlet of the safety filter 10 and the back flush inlet of the ultrafiltration device 8, a dosing mixer 6 is arranged on a pipeline between the ultrafiltration water tank 9 and the ultrafiltration device 8, a bactericide and hydrochloric acid are added in the dosing mixer 6 to reduce the alkalinity of the water and further sterilize the water, a scale inhibitor mixer 27 is arranged on the pipeline between the ultrafiltration water tank 9 and the safety filter 10, the scale inhibitor mixer 27 is used for preventing a pipeline and a membrane system structure by adding a scale inhibitor into the pipeline, the outlet of the safety filter 10 is communicated with the inlet of the reverse osmosis device 11, the water outlet of the reverse osmosis device 11 is communicated with the inlet of the decarbonizer 12, the carbon dioxide in the water is removed by the carbon remover 12, the outlet of the carbon remover 12 is communicated with the inlet of the fresh water tank 13, the fresh water tank 13 is used for storing the water treated by the carbon remover 12, the outlet of the fresh water tank 13 is respectively communicated with the inlet of the cation bed 14 and the back-washing inlet of the reverse osmosis device 11, bacteria, microorganisms and suspended matters in raw water are cleaned by adding bactericides, flocculating agents, hydrochloric acid and other medicaments, and the raw water is further filtered under the cooperation of the lamination filter 7, the ultrafiltration device 8, the security filter 10 and the reverse osmosis device 11, so that the raw water meets the production requirements, impurities in the water are reduced, the problem of equipment blockage is solved, the cleaning period is prolonged, and the working efficiency is ensured.
The device also comprises a cation bed resin transfer tank 141, wherein the inlet of the cation bed resin transfer tank 141 is communicated with the outlet of the cation bed 14, the outlet of the cation bed resin transfer tank 141 is communicated with the inlet of the cation bed 14, the outlet of the cation bed 14 is communicated with the inlet of the anion bed 15, and the cation bed resin transfer tank 141 has the function of transferring resin in the cation bed 14 into the cation bed resin transfer tank 141 when the cation bed 14 is overhauled.
Still including anion bed resin transfer tank 151, the export intercommunication of the entry of anion bed resin transfer tank 151 and anion bed 15, the export of anion bed resin transfer tank 151 and the entry intercommunication of anion bed 15, the export of anion bed 15 and the entry intercommunication that mixes the bed 16, when anion bed resin transfer tank 151's effect overhauls for anion bed 15, can be with the resin transfer in the anion bed 15 to in the anion bed resin transfer tank 151.
The system also comprises a mixed bed resin transfer tank 161, wherein the inlet of the mixed bed resin transfer tank 161 is communicated with the outlet of the mixed bed 16, the outlet of the mixed bed resin transfer tank 161 is communicated with the inlet of the mixed bed 16, and the anion bed resin transfer tank 151 is used for transferring the resin in the mixed bed 16 into the mixed bed resin transfer tank 161 when the mixed bed 16 is overhauled.
The outlet of the mixed bed 16 is communicated with the inlet of the resin trap 17, the outlet of the resin trap 17 is communicated with the inlet of the desalted water tank 18, and the resin entrained in the desalted water is recovered by the resin trap 17.
The concentrated water outlet of the ultrafiltration device 8, the concentration outlet of the reverse osmosis device 11, the flushing water outlet of the ultrafiltration device 8 and the flushing water outlet of the reverse osmosis device 11 are respectively communicated with the inlet of the recovery water tank 19, the recovery water tank 19 is used for recovering the concentrated water generated by the system, and the concentrated water is treated by a subsequent sewage treatment system.
A first liquid level meter 20 is arranged on the raw water tank 2, a second liquid level meter 21 is arranged on the ultrafiltration water tank 9, a third liquid level meter 22 is arranged on the fresh water tank 13, a first electromagnetic flow valve 23 is arranged on the raw water pipe 1, a second electromagnetic flow valve 24 is arranged on a pipeline between the laminated filter 7 and the ultrafiltration device 8, and a third electromagnetic flow valve 25 is arranged on a pipeline between the fresh water tank 13 and the cation bed 14;
the first liquid level meter 20, the second liquid level meter 21 and the third liquid level meter 22 are respectively and electrically connected with the input end of a controller 26, the output end of the controller 26 is respectively and electrically connected with a first electromagnetic flow valve 23, a second electromagnetic flow valve 24 and a third electromagnetic flow valve 25, during the operation of the water making equipment, the opening degree of the first electromagnetic flow valve 23 is adjusted according to the liquid level change trend of the raw water tank 2 detected by the first liquid level meter 20, the opening degree of the second electromagnetic flow valve 24 is adjusted according to the liquid level change trend of the ultra-filtration water tank 9 detected by the second liquid level meter 21, the opening degree of the third electromagnetic flow valve 25 is adjusted according to the liquid level change trend of the fresh water tank 13 detected by the third liquid level meter 22, the current processing capacity and the processing efficiency of each equipment are met by adjusting the water inlet flow of the relevant equipment, the technical problem of overload operation of the equipment is solved, the stable and safe operation of the system is ensured, the service life of the equipment is prolonged, and the filtering effect of raw water is ensured.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (9)
1. The automatic regulating and treating system for boiler water is characterized by comprising a raw water pipe, a raw water tank, a lamination filter, an ultrafiltration device, a security filter, a recovery water tank, a reverse osmosis device, a carbon remover, a fresh water tank, a cation bed, a anion bed, a mixed bed, a resin catcher and a demineralized water tank;
the raw water pipe is communicated with an inlet of the raw water tank, an outlet of the raw water tank is communicated with an inlet of the laminated filter, an outlet of the laminated filter is communicated with an inlet of the ultrafiltration device, a water production outlet of the ultrafiltration device is communicated with an inlet of the ultrafiltration water tank, an outlet of the ultrafiltration water tank is respectively communicated with an inlet of the security filter and a back flush inlet of the ultrafiltration device, an outlet of the security filter is communicated with an inlet of the reverse osmosis device, a water production outlet of the reverse osmosis device is communicated with an inlet of the carbon remover, an outlet of the carbon remover is communicated with an inlet of the fresh water tank, an outlet of the fresh water tank is respectively communicated with an inlet of the cation bed and a back flush inlet of the reverse osmosis device, an outlet of the cation bed is communicated with an inlet of the anion bed, and an outlet of the anion bed is communicated with an inlet of the mixed bed, an outlet of the mixed bed is communicated with an inlet of the resin catcher, and an outlet of the resin catcher is communicated with an inlet of the desalting water tank;
and a concentrated water outlet of the ultrafiltration device, a concentrated outlet of the reverse osmosis device, a flushing water outlet of the ultrafiltration device and a flushing water outlet of the reverse osmosis device are respectively communicated with an inlet of the recovery water tank.
2. The automatic conditioning treatment system for boiler water according to claim 1, characterized in that said raw water pipe is equipped with a heater and a bactericide mixer.
3. The system of claim 1, wherein a flocculant mixer is provided in the line between the raw water tank and the laminated filter.
4. The automatic regulating and treating system for boiler water according to claim 1, wherein a dosing mixer is provided on a pipeline between the ultrafiltration water tank and the ultrafiltration device.
5. The automatic regulating and treating system for boiler water according to claim 1, wherein a scale inhibitor mixer is provided on the pipeline between the ultrafiltration water tank and the cartridge filter.
6. The automatic regulating and processing system for boiler water according to claim 1, wherein a first level gauge is installed on the raw water tank, a second level gauge is installed on the ultrafiltration water tank, a third level gauge is installed on the raw water tank, a first electromagnetic flow valve is installed on the raw water pipe, a second electromagnetic flow valve is installed on the pipeline between the laminated filter and the ultrafiltration device, and a third electromagnetic flow valve is installed on the pipeline between the raw water tank and the anode bed;
the first liquid level meter, the second liquid level meter and the third liquid level meter are respectively electrically connected with the input end of a controller, and the output end of the controller is respectively electrically connected with the first electromagnetic flow valve, the second electromagnetic flow valve and the third electromagnetic flow valve.
7. The system of claim 1, further comprising a cation bed resin dump tank, wherein an inlet of the cation bed resin dump tank is communicated with an outlet of the cation bed, and an outlet of the cation bed resin dump tank is communicated with an inlet of the cation bed.
8. The system of claim 1, further comprising a resin transfer tank, wherein an inlet of the resin transfer tank is connected to an outlet of the anion bed, and an outlet of the resin transfer tank is connected to an inlet of the anion bed.
9. The automatic regulating and treating system for boiler water according to claim 1, further comprising a mixed bed resin dump tank, wherein an inlet of the mixed bed resin dump tank is communicated with an outlet of the mixed bed, and an outlet of the mixed bed resin dump tank is communicated with an inlet of the mixed bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220351834.7U CN216837458U (en) | 2022-02-21 | 2022-02-21 | Automatic regulating and treating system for boiler water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220351834.7U CN216837458U (en) | 2022-02-21 | 2022-02-21 | Automatic regulating and treating system for boiler water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216837458U true CN216837458U (en) | 2022-06-28 |
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ID=82090715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220351834.7U Expired - Fee Related CN216837458U (en) | 2022-02-21 | 2022-02-21 | Automatic regulating and treating system for boiler water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216837458U (en) |
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2022
- 2022-02-21 CN CN202220351834.7U patent/CN216837458U/en not_active Expired - Fee Related
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220628 |
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| CF01 | Termination of patent right due to non-payment of annual fee |