CN209537155U - A kind of power plant chemistry water manufacturing system - Google Patents
A kind of power plant chemistry water manufacturing system Download PDFInfo
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- CN209537155U CN209537155U CN201822264546.4U CN201822264546U CN209537155U CN 209537155 U CN209537155 U CN 209537155U CN 201822264546 U CN201822264546 U CN 201822264546U CN 209537155 U CN209537155 U CN 209537155U
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- water
- water tank
- reverse osmosis
- manufacturing system
- power plant
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Abstract
The utility model discloses a kind of power plant chemistry water manufacturing systems, including treating nature water device, ultrafiltration apparatus, reverse osmosis unit and ion demineralizer, treating nature water device, ultrafiltration apparatus, reverse osmosis unit and ion demineralizer can be good at automatically controlling and adjusting the starting of entire water manufacturing system, operation and stoppage in transit, it can be good at avoiding the uneven use between same type equipment, it can be good at waste of raw materials caused by the fault for avoiding occurring in personnel's operation, original control system needs more people's rotations to operate, the more person works' intensity in control point is big in operating process, personnel's operation has been subtracted after being transformed by this technology significantly reduces the input amount and labor intensity of personnel.
Description
Technical field
The utility model relates to chemistry water technical field, specially a kind of power plant chemistry water manufacturing system.
Background technique
Original water manufacturing system control is half dynamic control of single devices, and it is totally full-automatic to be not directed to water manufacturing system whole process
Control.Chemical each subsystem single devices start stop operation of water manufacturing system is by operator according to Water flow-path separate operations processed, behaviour
The main equipment of each subsystem and the start and stop quantity and operating parameter of ancillary equipment, whole operation process are manually adjusted during making
Relatively complicated personnel carry out every adjustment operation in Chemical Control picture manually, and the operation of chemistry water plant personnel is more to be easy
There is operation error and damage is generated to equipment, the control of reaction settling basin operating load lifting dosage is all hand in water manufacturing system
Dynamic operation, it is single automatic control for covering semi-automatic operation and being not directed between mostly set ultrafiltration, equipment use that ultrafiltration system operation, which operates,
Counter-infiltration system operation operation is not directed to cover the automatic control between reverse osmosis more for single semi-automatic operation of set.Original technology is automatic
Since adjustment often results in unit exception operation not in time in the low personnel control equipment running process of change degree, such as: water manufacturing system
Fast response sedimentation basin delivery turbidity is exceeded for water inlet, medicine system is forgotten to adjust after investment leads to pretreatment, ultrafiltration and anti-not in time
It permeates misoperation and produces the deterioration of water index, influence follow-up equipment safe and stable operation.Equipment start-stop is all by artificially selecting to control
Equipment is resulted in this way using unbalanced, and the ageing equipment of long-time service is serious, mushroom breeding inside the equipment often not used
It is more, life of equipment is resulted in this way to be greatly shortened.Due to manual operation water making device cleaning process, process control is not
Very medicament and raw water is rigorously caused largely to lose.
Therefore, it is necessary to solve the above problems to invent a kind of power plant chemistry water manufacturing system.
Utility model content
The purpose of this utility model is to provide a kind of power plant chemistry water manufacturing systems, to solve to propose in above-mentioned background technique
The problem of.
To achieve the above object, the utility model provides the following technical solutions: a kind of power plant chemistry water manufacturing system, including original
Water pre-treatment means, ultrafiltration apparatus, reverse osmosis unit and ion demineralizer, the treating nature water device include raw water water intaking
Pump, reaction settling basin, air scrubbing filter, chemical pond, fire cistern and circulating water pool, the raw water water pump, reaction are heavy
Pipeline connection, the ultrafiltration dress are passed sequentially through between shallow lake pond, air scrubbing filter, chemical pond, fire cistern and circulating water pool
It sets including UF ultrafilter, active carbon filter and ultrafiltration water tank, the UF ultrafilter, active carbon filter and ultrafiltration
It is sequentially connected between water tank by pipeline, the UF ultrafiltration of the circulating water pool output end and ultrafiltration apparatus of the treating nature water device
It is connected between filter input terminal by pipeline, the reverse osmosis unit includes reverse osmosis filter and fresh-water tank, the reverse osmosis
It is connected through between filter output end and the input terminal of fresh-water tank by pipeline, the input terminal of the reverse osmosis filter and ultrafiltration
It is connected between the output end of water tank by pipeline, the ion demineralizer includes cation exchanger, intermediate water tank, anion
Exchanger, mixed ion exchanger and sweet-water tank, the cation exchanger, intermediate water tank, anion exchanger, mixing from
Sub- exchanger and sweet-water tank are sequentially connected by pipeline, the input terminal of the output end of the fresh-water tank and cation exchanger it
Between pass through pipeline connect.
Preferably, interlocking controller, the particular type of the interlocking controller are installed in the fresh-water tank and sweet-water tank
Number be Schneider CJX2-ND150 interlocking controller.
Preferably, it is connected on the output end of the sweet-water tank for feed pipe.
Preferably, the reaction settling basin is provided with two groups.
Preferably, the UF ultrafilter is provided with four groups.
Preferably, the reverse osmosis filter is provided with four groups.
Compared with prior art, the beneficial effects of the utility model are as follows: the power plant chemistry water manufacturing system, will entire chemistry
Water manufacturing system is partitioned into 4 subsystems, realizes the entirety of chemical water manufacturing system certainly by the automatic control of 4 subsystems
Dynamic control；4 subsystems are respectively treating nature water device, ultrafiltration apparatus, reverse osmosis unit and ion demineralizer can be very
Starting, operation and the stoppage in transit of good automatic control and the entire water manufacturing system of adjustment, can be good at avoiding between same type equipment
Uneven use, can be good at avoiding personnel operate in waste of raw materials caused by the fault that occurs, original control system
More people's rotations are needed to operate, the more person works' intensity in control point is big in operating process, subtracts after being transformed by this technology
Personnel operate the input amount and labor intensity for significantly reducing personnel.
Detailed description of the invention
Fig. 1 is the system structure diagram of the utility model；
Fig. 2 is the system flow structural schematic diagram of the utility model.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
A kind of power plant chemistry water manufacturing system referring to FIG. 1-2, including treating nature water device, ultrafiltration apparatus, reverse osmosis dress
Set with ion demineralizer, the treating nature water device includes raw water water pump, reaction settling basin, air scrubbing filter, change
Pond, fire cistern and circulating water pool are learned, the raw water water pump, air scrubbing filter, chemical pond, disappears at reaction settling basin
Pipeline connection is passed sequentially through between anti-pond and circulating water pool, the ultrafiltration apparatus includes UF ultrafilter, active carbon filtering
Device and ultrafiltration water tank are sequentially connected between the UF ultrafilter, active carbon filter and ultrafiltration water tank by pipeline, described
It is connected between the circulating water pool output end for the treatment of nature water device and the UF ultrafilter input terminal of ultrafiltration apparatus by pipeline,
The reverse osmosis unit includes reverse osmosis filter and fresh-water tank, the input terminal of the reverse osmosis filter output end and fresh-water tank
Between by pipeline connect, between the input terminal of the reverse osmosis filter and the output end of ultrafiltration water tank by pipeline connection,
The ion demineralizer includes cation exchanger, intermediate water tank, anion exchanger, mixed ion exchanger and demineralized water
Case, the cation exchanger, intermediate water tank, anion exchanger, mixed ion exchanger and sweet-water tank by pipeline according to
Secondary connection is connected between the output end of the fresh-water tank and the input terminal of cation exchanger by pipeline.
Specifically, interlocking controller is installed in the fresh-water tank and sweet-water tank, the particular type of the interlocking controller
Number be Schneider CJX2-ND150 interlocking controller.
Specifically, being connected on the output end of the sweet-water tank for feed pipe.
Specifically, the reaction settling basin is provided with two groups.
Specifically, the UF ultrafilter is provided with four groups.
Specifically, the reverse osmosis filter is provided with four groups.
Working principle: the technical program is a kind of scheme about chemical water manufacturing system, and scheme is interior by entire chemistry water
System Partition becomes 4 subsystems, and the whole automatic control of chemical water manufacturing system is realized by the automatic control of 4 subsystems
System；4 subsystems are respectively treating nature water device, ultrafiltration apparatus, reverse osmosis unit and ion demineralizer, now to every height
Device control mode does following explanation.
Treating nature water device includes raw water water pump, reaction settling basin, air scrubbing filter, chemical pond, fire water
Pond and circulating water pool, when chemical pond, fire cistern, circulating water pool liquidometer detect that a certain pond liquid level drops to setting liquid
Position, program controlled automatic open water replenishment door, and treating nature water device starts automatically, and control system first is by reaction settling basin and sky
Gas is cleaned each valve in filter tank and is adjusted to operating status, and then program controlled automatic starting raw water water pump, which slowly promotes frequency, makes to react
Sedimentation basin operating load slowly rises, and reaction settling basin load starts raw water medicine system and basis automatically when going up to 50t/h
Reaction settling basin operating load adjustment dosing pump running frequency ensures that treating nature water system effluent quality is qualified, raw water water pump
Operating load is automatically adjusted according to chemical pond, fire cistern and circulating water pool liquid level, chemical pond, fire cistern and
Circulating water pool liquid level after attaining to a high place each water replenishment door close treating nature water system and be automatically stopped operation.
Ultrafiltration apparatus automatic running is that interlocked control is carried out by ultrafiltration high water tank, and runing time is arranged in each ultrafiltration apparatus
When ultrafiltration high water tank reaches a certain setting value, control system is accumulated according to runing time and ultrafiltration high water tank is automatic for accumulation
The selection operation lesser ultrafiltration apparatus of accumulated time puts into operation, as ultrafiltration high water tank continues to decline ultrafiltration control system root
The alternative condition that puts into operation on accordingly continues to put into other not running ultrafiltration apparatus until ultrafiltration high water tank starts to go up, ultrafiltration water tank
After liquid level goes up to a certain setting value ultrafiltration apparatus will according to runing time accumulate selection the longer ultrafiltration apparatus of runing time into
Row is stopped transport, and will continue to stop transport other according to the above stoppage in transit alternative condition as ultrafiltration high water tank continues to rise ultrafiltration control system
Ultrafiltration is run until ultrafiltration apparatus all automatic stoppages in transit.
Reverse osmosis unit automatic running is that interlocked control is carried out by fresh-water tank liquid level, when each reverse osmosis unit setting is run
Between accumulation when fresh-water tank liquid level reaches a certain setting value control system according to runing time accumulate and fresh-water tank liquid level select automatically
It selects the operation lesser reverse osmosis unit of accumulated time to put into operation and interlock and automatically engage antisludging agent dosing pump, such as fresh-water tank liquid level
Continue to decline reverse osmosis control system will be continued to put into other not running reverse osmosis units according to the alternative condition that puts into operation above it is straight
Start to go up to fresh-water tank liquid level, reverse osmosis control system will be according to runing time after going up to a certain setting value for fresh-water tank liquid level
The accumulation selection longer reverse osmosis unit of runing time is stopped transport, as fresh-water tank liquid level continues to the reverse osmosis control system that goes up
To be continued to stop transport according to the above stoppage in transit alternative condition, other operations are reverse osmosis until reverse osmosis unit is all automatic stops transport.
Ion demineralizer automatic running is that interlocked control is carried out by sweet-water tank liquid level, each ion demineralizer setting
Runing time accumulation control system when sweet-water tank liquid level reaches a certain setting value is accumulated according to runing time and sweet-water tank
Liquid level automatically select operation the lesser ion demineralizer of accumulated time put into operation, as sweet-water tank liquid level continue to decline from
Sub- desalination control system continues to put into other not running ion demineralizers until sweet-water tank liquid level according to condition selected above
Start to go up, ion demineralizer will accumulate selection operation according to runing time after sweet-water tank liquid level goes up to a certain setting value
Time, longer ion demineralizer was stopped transport, as sweet-water tank liquid level continues to rise ion desalination control system for basis
Condition selected above continues to stop transport other operation ion demineralizers until all automatic stoppages in transit of ion demineralizer.
Product demineralized water supply user is rising in main-piping pressure decline of confessing that main-piping pressure controlled according to demineralized water
It confesses pump operation frequency more than demineralized water after setting value to increase automatically, main-piping pressure, which goes up, confesses pump more than demineralized water after setting value
Running frequency reduces automatically.
Finally, it should be noted that the above descriptions are merely preferred embodiments of the present invention, it is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic
It is equivalently replaced, within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on,
It should be included within the scope of protection of this utility model.
Claims (6)
1. a kind of power plant chemistry water manufacturing system, including treating nature water device, ultrafiltration apparatus, reverse osmosis unit and ion desalination dress
It sets, it is characterised in that: the treating nature water device includes raw water water pump, reaction settling basin, air scrubbing filter, chemical water
Pond, fire cistern and circulating water pool, the raw water water pump, reaction settling basin, air scrubbing filter, chemical pond, fire water
Passed sequentially through between pond and circulating water pool pipeline connection, the ultrafiltration apparatus include UF ultrafilter, active carbon filter and
Ultrafiltration water tank is sequentially connected between the UF ultrafilter, active carbon filter and ultrafiltration water tank by pipeline, the raw water
It is connected between the circulating water pool output end of pretreatment unit and the UF ultrafilter input terminal of ultrafiltration apparatus by pipeline, it is described
Reverse osmosis unit includes reverse osmosis filter and fresh-water tank, between the reverse osmosis filter output end and the input terminal of fresh-water tank
It is connected by pipeline, is connected between the input terminal of the reverse osmosis filter and the output end of ultrafiltration water tank by pipeline, it is described
Ion demineralizer includes cation exchanger, intermediate water tank, anion exchanger, mixed ion exchanger and sweet-water tank,
The cation exchanger, intermediate water tank, anion exchanger, mixed ion exchanger and sweet-water tank are successively connected by pipeline
It connects, is connected between the output end of the fresh-water tank and the input terminal of cation exchanger by pipeline.
2. a kind of power plant chemistry water manufacturing system according to claim 1, it is characterised in that: the fresh-water tank and sweet-water tank
Interlocking controller is inside installed, the concrete model of the interlocking controller is Schneider CJX2-ND150 interlocking controller.
3. a kind of power plant chemistry water manufacturing system according to claim 1, it is characterised in that: the output end of the sweet-water tank
On be connected with for feed pipe.
4. a kind of power plant chemistry water manufacturing system according to claim 1, it is characterised in that: the reaction settling basin is provided with
Two groups.
5. a kind of power plant chemistry water manufacturing system according to claim 1, it is characterised in that: the UF ultrafilter setting
There are four groups.
6. a kind of power plant chemistry water manufacturing system according to claim 1, it is characterised in that: the reverse osmosis filter setting
There are four groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822264546.4U CN209537155U (en) | 2018-12-31 | 2018-12-31 | A kind of power plant chemistry water manufacturing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822264546.4U CN209537155U (en) | 2018-12-31 | 2018-12-31 | A kind of power plant chemistry water manufacturing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209537155U true CN209537155U (en) | 2019-10-25 |
Family
ID=68267989
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822264546.4U Expired - Fee Related CN209537155U (en) | 2018-12-31 | 2018-12-31 | A kind of power plant chemistry water manufacturing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209537155U (en) |
-
2018
- 2018-12-31 CN CN201822264546.4U patent/CN209537155U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191025 Termination date: 20211231 |