CN205472840U - Sulphur removal sterilizing equipment - Google Patents
Sulphur removal sterilizing equipment Download PDFInfo
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- CN205472840U CN205472840U CN201620066904.9U CN201620066904U CN205472840U CN 205472840 U CN205472840 U CN 205472840U CN 201620066904 U CN201620066904 U CN 201620066904U CN 205472840 U CN205472840 U CN 205472840U
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- pump
- water
- tank
- brine
- strong brine
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Abstract
The utility model provides a sulphur removal sterilizing equipment, the constant voltage self priming pump is connected between clear water pipeline and demineralized water unit, and supply water to the demineralized water unit, the demineralized water unit passes through pipeline and demineralized water strong brine jar, it connects to soften the water pitcher, demineralized water strong brine pump passes through the pipeline to demineralized water strong brine jar supply strong brine, the constant voltage self priming pump, the clarified water pump, rare brine pump, the fan, the solenoid valve, the dosing pump, demineralized water strong brine pump is connected with the switch board respectively and controlled by the switch board through the cable, soften the water pitcher, the clarified water pump, the solenoid valve, change salt pond and strong brine pond, rare salt water pitcher is connected, demineralized water strong brine pump pass through the cable respectively with the switch board, the solenoid valve, soften the water pitcher, floater liquid level changer, change salt pond and strong brine pond, rare salt water pitcher is connected, it has had very obvious economic benefits in the aspect of the sewage treatment of oil field, and the work intensity of workers is reduced, it disinfects to the secondary pollution of environment to have reduced the medicament.
Description
Technical field
This utility model relates to oilfield sewage sulphur removal disinfection equipment field, particularly relates to a kind of sulphur removal sterilizing unit.
Background technology
Each elephant is when produced-water reinjection, and water injection equipment, pipeline and water injection well pit shaft easily occur water quality due to bacteria breed
Pollute, block, corrosion etc., typically solve, by filling antibacterial, the harm that antibacterial is caused, current disinfection equipment is costly, right
The person is poisoned big, and environment is existed secondary pollution.
Summary of the invention
In order to solve problem above, this utility model provides a kind of sulphur removal sterilizing unit, and it is in terms of disposing polluted water in oil
There is obviously economic benefit, saved fund, alleviated the labor intensity of workman, decreased medicament disinfecting to environment
Secondary pollution, and sodium hypochlorite sterilization is substantially, and action time and distance are longer, and this device is fully automatic operation, without personnel
Watching at the scene, can be operated according to the program of PLC, automaticity is high, has host computer transporting function, workman on duty doing
The working condition of equipment just can be seen in public room.
The technical solution of the utility model is: providing a kind of sulphur removal sterilizing unit, it is by electro connecting pressure gauge, dosing
Pump, weak brine pump, proportioner, sodium hypochlorite tank, blower fan, effusion meter one, effusion meter two, dilute hydrochloric acid tank, weak brine tank, change salt pond
Open with strong brine pond, electromagnetic valve, electrolysis bath, clarified water pump, water softener tank, softening water unit, rectification output counter, switch board, air channel
Closing, soften water strong brine pump, soften water strong brine tank, floating-ball fluid level transmitter and constant voltage self priming pump composition, constant voltage self priming pump is even
It is connected on fresh water pipeline and softens between water unit, and supplying water to softening water unit, softening water unit and pass through pipeline and soften water
The connection of strong brine tank, water softener tank, softens water strong brine pump by pipeline to softening water strong brine tank supply strong brine, and constant voltage is certainly
Sucking pump, clarified water pump, weak brine pump, blower fan, electromagnetic valve, dosing pump, softening water strong brine pump are by cable respectively with switch board even
Connecing and controlled cabinet controls, water softener tank, clarified water pump, electromagnetic valve, change salt pond are connected with strong brine pond, weak brine tank, soften water
Strong brine pump is connected with constant voltage self priming pump, clarified water pump, weak brine pump, blower fan respectively by cable, softens water strong brine pump and passes through
Cable is respectively with switch board, electromagnetic valve, water softener tank, floating-ball fluid level transmitter, change salt pond with strong brine pond, weak brine tank even
Connect, water softener tank by pipeline respectively with clarified water pump, electromagnetic valve, change salt pond and strong brine pond, effusion meter one, effusion meter two, dilute
Brine tank connects, and weak brine tank is connected with weak brine pump, dilute hydrochloric acid tank respectively by pipeline, weak brine tank pass through pipeline respectively with
Weak brine pump, electro connecting pressure gauge, effusion meter two, electrolysis bath connect, electrolysis bath by pipeline respectively with dilute hydrochloric acid tank, hypochlorous acid
Sodium tank connects, and dilute hydrochloric acid tank is connected with effusion meter one, effusion meter two respectively by proportioner, and sodium hypochlorite tank is with dosing pump even
Connecing, blower fan upper end is provided with air channel switch, and rectification output counter is connected with electrolysis bath by cable.
Preferably, the saturated strong brine made in softening water unit, change salt pond and strong brine pond, after proportioner, is made into
The weak brine of concentration 3% 5%.
Preferably, electrolysis bath is U-PVC material, pmma material, and when starting work, electrolysis bath must be full of dilute salt
Water, pipeline pressure can not be low, and temperature is not above 50 DEG C, and sodium hypochlorite tank is not high level.
Compared with prior art, the beneficial effects of the utility model are: continuous dosing of can advancing, indirect dosing, impact
Dosing, when sewage quantity is big when, dosing just needs to strengthen, and prevents from not reaching sterilization purpose, will reduce when dirt amount reduces when
Chemical feeding quantity, in order to avoid causing the wave to sodium hypochlorite to give up, and the concentration of dosing can be many according to sodium hypochlorite in sewage
Few, artificial is adjusted.
Accompanying drawing explanation
Further this utility model is illustrated below according to figure
Figure is structure chart of the present utility model；
Shown in figure: 1, electro connecting pressure gauge, 2, dosing pump, 3, weak brine pump, 4, proportioner, 5, sodium hypochlorite tank, 6,
Blower fan, 7, effusion meter one, 8, effusion meter two, 9, dilute hydrochloric acid tank, 10, weak brine tank, 11, change salt pond and strong brine pond, 12, electricity
Magnet valve, 13, electrolysis bath, 14, clarified water pump, 15, water softener tank, 16, soften water unit, 17, rectification output counter, 18, switch board,
19, air channel switch, 20, soften water strong brine pump, 21, soften water strong brine tank, 22, floating-ball fluid level transmitter, 23, constant voltage self-priming
Pump.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is described in further detail, it should be noted that accompanying drawing is only used for solving
Release this utility model, be that this utility model embodiment is schematically illustrated, and it is not intended that to restriction of the present utility model.
In description of the present utility model, except as otherwise noted, term " on ", D score, "left", "right", " interior ", " outward ",
The orientation of the instruction such as " front end ", " rear end ", " head ", " afterbody " or position relationship are to close based on orientation shown in the drawings or position
System, is for only for ease of description this utility model and simplifies description rather than instruction or imply that the device of indication or element are necessary
There is specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.
In description of the present utility model, it should be noted that unless otherwise clearly defined and limited, term " phase
Even ", " connection " should be interpreted broadly, for example, it may be fixing connection, it is also possible to be to removably connect, or be integrally connected；Can
To be mechanical connection, it is also possible to be electrical connection；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary.For this
For the those of ordinary skill in field, above-mentioned term concrete meaning in this utility model can be understood with concrete condition.
As it can be seen, sulphur removal sterilizing unit, it be by electro connecting pressure gauge 1, dosing pump 2, weak brine pump 3, proportioner 4,
Sodium hypochlorite tank 5, blower fan 6, effusion meter 1, effusion meter 28, dilute hydrochloric acid tank 9, weak brine tank 10, change salt pond and strong brine pond
11, electromagnetic valve 12, electrolysis bath 13, clarified water pump 14, water softener tank 15, soften water unit 16, rectification output counter 17, switch board 18,
Air channel switch 19, softening water strong brine pump 20, softening water strong brine tank 21, floating-ball fluid level transmitter 22 and constant voltage self priming pump 23 groups
Becoming, constant voltage self priming pump 23 is connected to fresh water pipeline and softens between water unit 16, and supplies water to softening water unit 16, softens
Water unit 16 by pipeline with soften water strong brine tank 21, water softener tank 15 is connected, soften water strong brine pump 20 pass through pipeline to
Soften water strong brine tank 21 and supply strong brine, constant voltage self priming pump 23, clarified water pump 14, weak brine pump 3, blower fan 6, electromagnetic valve 12, add
Teat pipette 2, soften water strong brine pump 20 and be connected with switch board 18 respectively by cable and controlled cabinet 18 controls, water softener tank 15,
Clarified water pump 14, electromagnetic valve 12, change salt pond are connected with strong brine pond 11, weak brine tank 10, soften water strong brine pump 20 and pass through cable
It is connected with constant voltage self priming pump 23, clarified water pump 14, weak brine pump 3, blower fan 6 respectively, softens water strong brine pump 20 by cable respectively
With switch board 18, electromagnetic valve 12, water softener tank 15, floating-ball fluid level transmitter 22, change salt pond and strong brine pond 11, weak brine tank 10
Connect, water softener tank 15 by pipeline respectively with clarified water pump 14, electromagnetic valve 12, change salt pond and strong brine pond 11, effusion meter 1,
Effusion meter 28, weak brine tank 10 connect, and weak brine tank 10 is connected with weak brine pump 3, dilute hydrochloric acid tank 9 respectively by pipeline, dilute salt
Water pot 10 is connected with weak brine pump 3, electro connecting pressure gauge 1, effusion meter 28, electrolysis bath 13 respectively by pipeline, and electrolysis bath 13 leads to
Cross pipeline to be connected with dilute hydrochloric acid tank 9, sodium hypochlorite tank 5 respectively, dilute hydrochloric acid tank 9 by proportioner 4 respectively with effusion meter 1, stream
Gauge 28 connects, and sodium hypochlorite tank 5 is connected with dosing pump 2, and blower fan 6 upper end is provided with air channel switch 19, and rectification output counter 17 passes through
Cable is connected with electrolysis bath 13.
Preferably, soften water unit 16, change the saturated strong brine made in salt pond and strong brine pond 11 through proportioner 4
After, it is made into the weak brine of concentration 3% 5%.
Preferably, electrolysis bath 13 is U-PVC material, pmma material, and when starting work, electrolysis bath 13 must be full of dilute
Saline, pipeline pressure can not be low, and temperature is not above 50 DEG C, and sodium hypochlorite tank 5 is not high level.
Softening water unit 16 and changing the saturated strong brine made in salt pond and strong brine pond 11 through proportioner 4 with pressure
After, it is made into the weak brine of concentration 3% 5%, enters in weak brine tank 10, after weak brine pump 3 pressurizes, send into electrolysis bath 13
In, weak brine is entered by the bottom of electrolysis bath 13, flows through each electrolytic chamber in electrolysis bath 13 from the bottom to top, galvanic
Under effect, produce liquor natrii hypochloritis, electrolysis bath 13 export in pipeline enters sodium hypochlorite tank 5, added by dosing pump 2
Liquor natrii hypochloritis delivers to after pressure chemical feeding points, and the hydrogen the produced during electrolysis air vent through sodium hypochlorite storage tank 5 top drains into
Outdoor, the hydrogen in sodium hypochlorite tank 5, blower fan 6 air intake it is discharged to outdoor by exhaustor after diluting, calcium, magnesium etc. are deposited on
Storage tank bottom, is periodically discharged by sewage draining exit.
After clear water enters, enter into constant voltage self priming pump 23 and carry out supercharging, enter afterwards and soften water unit 16, clear water is entered
Row softens work, enters in water softener tank 15 after removing part calcium, magnesium ion, and water softener tank 15 has high level and middle liquid level to clearly
The electromagnetic valve 12 of water inlet is controlled, and during water softener tank 15 high level, electromagnetic valve 12 cuts out, electricity during liquid level in water softener tank 15
Magnet valve 12 is opened and is carried out moisturizing work.Clarified water pump 14 supplies electromagnetic valve 12 after drawing softening water 16 from water softener tank 15.Electromagnetism
Valve 12 stops according to changing the salt pond high level with strong brine pond 11, and low liquid level is opened and is operated, to changing salt pond and strong brine pond
11 carry out moisturizing.Electromagnetic valve 12 stops according to the high level of weak brine tank 10, and middle liquid level is opened and is operated.Clarified water pump 14 is also subject to
The protection of the low liquid level of water softener tank, it is simply that during water softener tank 15 low liquid level, clarified water pump 14 can not work.And clarified water pump 14 and electricity
Magnet valve 12 links.When work opened by electromagnetic valve 12, soften the entrance of water unit 16, make proportioner 4 produce negative pressure, suctionization salt
Saturated strong brine in pond and strong brine pond 11 also in weak brine tank 10, makes the brine strength in weak brine tank 10 be
3%-5%.Weak brine pump 3 after sucking-off weak brine, is discharged in electrolysis bath 13 carry out being electrolysed work, produces secondary from weak brine tank 10
Sodium chlorate solution, the startup of weak brine pump 3 is started by liquid level in sodium hypochlorite tank 5, when sodium hypochlorite tank 5 high level,
Stopping the work of weak brine pump 3, when the liquid level in weak brine tank 10 is low liquid level, weak brine pump 3 is protected quitting work.
Dosing pump 2 only just starts to start work when more than liquid level in sodium hypochlorite tank 5, when sodium hypochlorite tank 5 low liquid level, and dosing
Pump 2 is can be protected, out-of-work.Electrolysis bath 13 is U-PVC material, pmma material, when starting work, and electrolysis bath 13
Must be full of weak brine, pipeline pressure can not be low, and temperature is not above 50 DEG C, and sodium hypochlorite tank 5 is not high level.
This utility model can advance continuous dosing, indirect dosing, impact dosing, when sewage quantity is big when, dosing is just
Need to strengthen, prevent from not reaching sterilization purpose, chemical feeding quantity will be reduced when dirt amount is little when, in order to avoid causing the wave to sodium hypochlorite
Useless, and the concentration of dosing can according in sewage sodium hypochlorite number, artificial is adjusted.
This utility model has had obviously economic benefit in terms of disposing polluted water in oil, has saved fund, alleviates
The labor intensity of workman, decreases the medicament disinfecting secondary pollution to environment, and sodium hypochlorite sterilization is substantially, action time
Long, this device is fully automatic operation, guards at the scene without personnel, and it can be operated according to the program of PLC, automaticity
Height, has host computer transporting function, and workman on duty just can see the working condition of equipment in office.
The above is embodiment of the present utility model, is not limited to this utility model, for the technology of this area
For personnel, this utility model can have various modifications and variations.All made within spirit of the present utility model and principle
Within any modification, equivalent substitution and improvement etc. all should be contained in right of the present utility model.
Claims (3)
1. sulphur removal sterilizing unit, it is by electro connecting pressure gauge (1), dosing pump (2), weak brine pump (3), proportioner (4), secondary chlorine
Acid sodium tank (5), blower fan (6), effusion meter one (7), effusion meter two (8), dilute hydrochloric acid tank (9), weak brine tank (10), change salt pond are with dense
Brine pit (11), electromagnetic valve (12), electrolysis bath (13), clarified water pump (14), water softener tank (15), softening water unit (16), rectification
Output counter (17), switch board (18), air channel switch (19), softening water strong brine pump (20), softening water strong brine tank (21), ball float
Fluid level transmitter (22) and constant voltage self priming pump (23) composition, it is characterised in that: constant voltage self priming pump (23) be connected to fresh water pipeline with
Between softening water unit (16), and supply water to softening water unit (16), soften water unit (16) dense with softening water by pipeline
Brine tank (21), water softener tank (15) connect, and soften water strong brine pump (20) and are supplied to softening water strong brine tank (21) by pipeline
Answer strong brine, constant voltage self priming pump (23), clarified water pump (14), weak brine pump (3), blower fan (6), electromagnetic valve (12), dosing pump (2),
Soften water strong brine pump (20) to be connected with switch board (18) respectively by cable and controlled cabinet (18) control, water softener tank
(15), clarified water pump (14), electromagnetic valve (12), change salt pond be connected with strong brine pond (11), weak brine tank (10), softening water strong brine
Pump (20) is connected with constant voltage self priming pump (23), clarified water pump (14), weak brine pump (3), blower fan (6) respectively by cable, softens water
Strong brine pump (20) by cable respectively with switch board (18), electromagnetic valve (12), water softener tank (15), floating-ball fluid level transmitter
(22), change salt pond be connected with strong brine pond (11), weak brine tank (10), water softener tank (15) pass through pipeline respectively with clarified water pump
(14), electromagnetic valve (12), change salt pond are with strong brine pond (11), effusion meter one (7), effusion meter two (8), weak brine tank (10) even
Connecing, weak brine tank (10) is connected with weak brine pump (3), dilute hydrochloric acid tank (9) respectively by pipeline, and weak brine tank (10) passes through pipeline
Being connected with weak brine pump (3), electro connecting pressure gauge (1), effusion meter two (8), electrolysis bath (13) respectively, electrolysis bath (13) is by pipe
Line is connected with dilute hydrochloric acid tank (9), sodium hypochlorite tank (5) respectively, dilute hydrochloric acid tank (9) by proportioner (4) respectively with effusion meter one
(7), effusion meter two (8) connect, sodium hypochlorite tank (5) is connected with dosing pump (2), blower fan (6) upper end be provided with air channel switch
(19), rectification output counter (17) is connected with electrolysis bath (13) by cable.
Sulphur removal sterilizing unit the most according to claim 1, it is characterised in that: soften water unit (16), change salt pond and strong brine
The saturated strong brine made in pond (11), after proportioner (4), is made into the weak brine of concentration 3% 5%.
Sulphur removal sterilizing unit the most according to claim 1, it is characterised in that: electrolysis bath (13) is U-PVC material, lucite
Material, start work time, electrolysis bath (13) must be full of weak brine, pipeline pressure can not be low, temperature not above 50 DEG C, and
Sodium hypochlorite tank (5) is not high level.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620066904.9U CN205472840U (en) | 2016-01-22 | 2016-01-22 | Sulphur removal sterilizing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620066904.9U CN205472840U (en) | 2016-01-22 | 2016-01-22 | Sulphur removal sterilizing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205472840U true CN205472840U (en) | 2016-08-17 |
Family
ID=56639482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620066904.9U Active CN205472840U (en) | 2016-01-22 | 2016-01-22 | Sulphur removal sterilizing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205472840U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658184A (en) * | 2018-05-15 | 2018-10-16 | 廊坊市凯翔工贸有限公司 | Sulphur removal sterilizing unit |
| CN113186553A (en) * | 2021-05-08 | 2021-07-30 | 潍坊思源环保设备有限公司 | Intelligent automatic salt-blending electrolysis sodium hypochlorite generator and production method thereof |
-
2016
- 2016-01-22 CN CN201620066904.9U patent/CN205472840U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658184A (en) * | 2018-05-15 | 2018-10-16 | 廊坊市凯翔工贸有限公司 | Sulphur removal sterilizing unit |
| CN113186553A (en) * | 2021-05-08 | 2021-07-30 | 潍坊思源环保设备有限公司 | Intelligent automatic salt-blending electrolysis sodium hypochlorite generator and production method thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |