CN108975546A - A kind of high temperature water filling fine filtration device - Google Patents
A kind of high temperature water filling fine filtration device Download PDFInfo
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- CN108975546A CN108975546A CN201811114411.8A CN201811114411A CN108975546A CN 108975546 A CN108975546 A CN 108975546A CN 201811114411 A CN201811114411 A CN 201811114411A CN 108975546 A CN108975546 A CN 108975546A
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- filter
- ultrafiltration
- pipe
- high temperature
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 195
- 238000001914 filtration Methods 0.000 title claims abstract description 38
- 238000011049 filling Methods 0.000 title abstract description 16
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 93
- 239000000835 fiber Substances 0.000 claims abstract description 39
- 239000010865 sewage Substances 0.000 claims abstract description 28
- 239000012141 concentrate Substances 0.000 claims abstract description 24
- 238000005554 pickling Methods 0.000 claims description 18
- 239000003518 caustics Substances 0.000 claims description 15
- 239000003814 drug Substances 0.000 claims description 15
- 238000004458 analytical method Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 238000013327 media filtration Methods 0.000 claims description 3
- 238000005201 scrubbing Methods 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 7
- 238000000034 method Methods 0.000 description 10
- 239000012528 membrane Substances 0.000 description 9
- 230000008929 regeneration Effects 0.000 description 7
- 238000011069 regeneration method Methods 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 239000000706 filtrate Substances 0.000 description 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 206010067868 Skin mass Diseases 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000013480 data collection Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention discloses a kind of high temperature water filling fine filtration device, including double medium filters, fiber ball filter, cartridge filter and the ultrafiltration apparatus being sequentially communicated, the water inlet of double medium filters is connected to water inlet pipe, double medium filters and fiber ball filter are connected to sewage backwash pipe, and the water outlet of ultrafiltration apparatus is connected to outlet pipe;The water outlet of middle water pot is communicated with filter recoil pump, and filter recoil pump is connected to the bottom of the bottom of double medium filters and fiber ball filter respectively;The water outlet of ultrafiltration apparatus is connected to the water outlet that hyperfiltration reverse-rinsing pumps, and the water inlet of hyperfiltration reverse-rinsing pump is connected to outlet pipe;The top sidewall of ultrafiltration apparatus is additionally provided with side water outlet, and one end of ultrafiltration sewage backwash pipe is connected to the water inlet of ultrafiltration apparatus bottom end and side water outlet respectively, and ultrafiltration sewage backwash pipe is connected to by ultrafiltration concentrate recirculation pump with middle water pot.High temperature water filling fine filtration device of the present invention significantly improves the filter effect of high temperature water filling.
Description
Technical field
The present invention relates to filter device technical fields, fill the water fine filtration device more particularly to a kind of high temperature.
Background technique
Currently, being reached both at home and abroad using techniques such as oil removing, filterings in processing to the processing method of offshore production platform recovered water
Reinjection into reservoir again after mark, had both reduced pollution, and had also reduced development cost.It is some new however as going deep into for production development
Problem gradually draws attention, and mainly has following two points: (1) when oil field reinjection water temperature higher (50 DEG C of >), using conventional ultrafiltration
When film is handled, fenestra expands under high temperature environment causes effluent quality to be deteriorated;And oil field extracted water is injected at present
It is required that higher and higher, it is desirable that reach A1 grades or more of SY/T5329 " clastic rock reservoir water water quality fertilizer index and analysis method "
Water standard, therefore conventional water treatment device is not able to satisfy the environment of high-temperature water processing;(2) when higher due to water temperature, water quality is easy
Fouling, leads to that filtrate is hardened, membrane tube blocking, and backwash effect is poor;(3) currently on the market, ultrafiltration membrane operating temperature≤45 DEG C, when
When temperature is higher than this temperature, leakage easily occurs for putamina, fenestra easily expands and becomes larger, and effluent quality is not up to standard.
Summary of the invention
The object of the present invention is to provide a kind of high temperature to fill the water fine filtration device, to solve above-mentioned of the existing technology ask
Topic improves the filter effect of high temperature water filling.
To achieve the above object, the present invention provides following schemes: the present invention provides a kind of high temperature water filling fine filtering dress
It sets, double medium filters, fiber ball filter, cartridge filter and ultrafiltration apparatus including passing sequentially through connecting tube connection, institute
The water inlet for stating double medium filters is connected to water inlet pipe, double medium filters and the fiber ball filter with recoil
Sewage pipe connection is washed, the water outlet of the ultrafiltration apparatus is connected to outlet pipe;
The water outlet of middle water pot is communicated with filter recoil pump, the filter recoil pump by connecting tube respectively with it is described
The bottom of double medium filters is connected to the bottom of the fiber ball filter;The water outlet and hyperfiltration reverse-rinsing of the ultrafiltration apparatus
The water outlet of pump is connected to, and the water inlet of hyperfiltration reverse-rinsing pump is connected to the outlet pipe;The top sidewall of the ultrafiltration apparatus is also set
It is equipped with side water outlet, one end of ultrafiltration sewage backwash pipe is discharged with the water inlet of the ultrafiltration apparatus bottom end and the side respectively
Mouth is connected to by connecting tube, and the other end of the ultrafiltration sewage backwash pipe is connected to the water inlet that ultrafiltration concentrate recirculation pumps, institute
The water outlet for stating ultrafiltration concentrate recirculation pump is connected to the water inlet of the middle water pot by connecting tube;The sewage backwash pipe,
Valve is provided in the ultrafiltration sewage backwash pipe and each connecting tube.
It preferably, further include pickling tank and caustic treater, the top of the top of the pickling tank and the caustic treater leads to respectively
It crosses connecting tube to be connected to the outlet pipe, the bottom of the bottom of the pickling tank and the caustic treater passes through connecting tube and medicine respectively
The water inlet connection of pump is washed, the water outlet that the medicine washes pump is connected to the water inlet of the cartridge filter.
Preferably, the side water outlet also passes through concentrate recirculation pipe is connected to the water inlet that the ultrafiltration concentrate recirculation pumps.
Preferably, the connecting tube between the ultrafiltration concentrate recirculation pump and the middle water pot passes through a connecting tube and described pair
Connecting tube connection between medium filter and the fiber ball filter.
Preferably, water level sensor, the water inlet are provided in the middle water pot, the pickling tank and the caustic treater
Flowmeter, water quality online analyzer and temperature sensor are provided on pipe, the outlet pipe and the concentrate recirculation pipe;It is described
Water level sensor, the flowmeter, the water quality online analyzer and the temperature sensor are electrically connected with PLC controller respectively
It connects.
Preferably, the valve is pneumatic ball valve, and all valves are electrically connected with the PLC controller.
Preferably, it is provided with dosing mouth at the top of double medium filters, is provided at the dosing mouth and the PLC
The flowmeter of controller electrical connection;Microvovtex reactor, double media filtrations are additionally provided at the top of double medium filters
The bottom of device is provided with waterpower Scrubbing apparatus.
It preferably, further include the cloud platform and management server being connect respectively with the PLC controller.
Preferably, double medium filters, the fiber ball filter, the middle water pot and the filter recoil pump
For first unit, the cartridge filter, the ultrafiltration apparatus, the pickling tank, the caustic treater, the medicine wash pump, described
Hyperfiltration reverse-rinsing pump and ultrafiltration concentrate recirculation pump are second unit, and the first unit is set under the second unit
Side.
Preferably, double medium filters, the fiber ball filter, the water inlet pipe, double medium filters
The connecting tube between connecting tube and the fiber ball filter and the cartridge filter between the fiber ball filter
It is connected to respectively with blow-down pipe.
High temperature water filling fine filtration device of the present invention achieves following technical effect compared with the existing technology:
High temperature water filling fine filtration device of the present invention significantly improves the filter effect of high temperature water filling.High temperature water filling of the present invention
Fine filtration device still ensures that stable effluent quality reaches A1 grades of reinjected water when water water quality is poor using three-stage filtration
Standard is reduced occupation area of equipment, is met the small feature of offshore production platform area using equipment mounted on top mode.This hair
Bright high temperature water filling fine filtration device package unit is all made of temperature-resistant material, when realizing that water water temperature is higher, stable effluent quality
It is up to standard, whole Corrosion Protection is improved, service life of equipment is extended, reduces maintenance cost.High temperature water filling essence of the present invention
Thin filter device using full-automatic intelligent control, realization device normal filtration, filtrate backwash and regeneration, the backwash of ultrafiltration membrane air water,
Medicine washes the automation control of the processes such as regeneration, facilitates operation.Suspended matter, oil content are realized using water quality online analyzer simultaneously
On-line analysis detection reduces workload without sampling.Data can store while can teletransmission, the long-range monitoring of realization and operation, guarantee
Bad weather or in special circumstances equipment remain to run well.Network information cloud platform realizes that the cloud of equipment real time data is shared,
User and manufacturer can pass through the terminal devices such as mobile phone, computer observation device operation conditions at any time.
Detailed description of the invention
It in order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the invention
Example, for those of ordinary skill in the art, without any creative labor, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the structural schematic diagram that high temperature of the present invention fills the water fine filtration device;
Fig. 2 is the wire frame diagram that high temperature of the present invention fills the water fine filtration device;
Wherein, 1- water inlet pipe, the bis- medium filters of 2-, 3- fiber ball filter, 4- cartridge filter, 5- ultrafiltration apparatus,
6- outlet pipe, 7- hyperfiltration reverse-rinsing pump, 8- ultrafiltration concentrate recirculation pump, 9- pickling tank, 10- caustic treater, 11- medicine wash pump, water in 12-
Tank, 13- filter recoil pump, 14- concentrate recirculation pipe, 15- sewage backwash pipe, 16- blow-down pipe, 17- water level sensor, 18-
Temperature sensor, 19- water quality online analyzer, 20- flowmeter.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The object of the present invention is to provide a kind of high temperature to fill the water fine filtration device, of the existing technology to solve the problems, such as,
Improve the filter effect of high temperature water filling.
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, with reference to the accompanying drawing and specific real
Applying mode, the present invention is described in further detail.
As shown in Figs. 1-2, the present embodiment high temperature water filling fine filtration device includes double Jie for passing sequentially through connecting tube connection
Mass filter 2, fiber ball filter 3, cartridge filter 4 and ultrafiltration apparatus 5, the water inlet and water inlet pipe 1 of double medium filters 2
Connection, double medium filters 2 and fiber ball filter 3 be connected to sewage backwash pipe 15, the water outlet of ultrafiltration apparatus 5 with out
Water pipe 6 is connected to.
The water outlet of middle water pot 12 is communicated with filter recoil pump 13, filter recoil pump 13 by connecting tube respectively with it is double
The bottom of medium filter 2 is connected to the bottom of fiber ball filter 3;Water outlet and the hyperfiltration reverse-rinsing pump 7 of ultrafiltration apparatus 5 goes out
The water inlet of mouth of a river connection, hyperfiltration reverse-rinsing pump 7 is connected to outlet pipe 6;The top sidewall of ultrafiltration apparatus 5 is additionally provided with side water outlet
Mouthful, one end of ultrafiltration sewage backwash pipe 15 is connected with the water inlet of 5 bottom end of ultrafiltration apparatus and side water outlet by connecting tube respectively
Logical, the other end of ultrafiltration sewage backwash pipe 15 is connected to the water inlet of ultrafiltration concentrate recirculation pump 8, ultrafiltration concentrate recirculation pump 8
Water outlet is connected to the water inlet of middle water pot 12 by connecting tube;Sewage backwash pipe 15, ultrafiltration sewage backwash pipe 15 and each
Valve is provided in a connecting tube.Side water outlet also passes through concentrate recirculation pipe 14 and the water inlet of ultrafiltration concentrate recirculation pump 8 connects
It is logical.Connecting tube between ultrafiltration concentrate recirculation pump 8 and middle water pot 12 passes through a connecting tube and double medium filters 2 and fibrous nodules mistake
Connecting tube connection between filter 3.
The present embodiment high temperature water filling fine filtration device further includes pickling tank 9 and caustic treater 10, the top of pickling tank 9 and alkali
The top of cleaning of evaporator 10 passes through connecting tube respectively and is connected to outlet pipe 6, and the bottom of pickling tank 9 and the bottom of caustic treater 10 pass through respectively
Connecting tube is connected to the water inlet that medicine washes pump 11, and the water outlet that medicine washes pump 11 is connected to the water inlet of cartridge filter 4.
It is provided with water level sensor 17 in middle water pot 12, pickling tank 9 and caustic treater 10, water inlet pipe 1, outlet pipe 6 and dense
Flowmeter 20, water quality online analyzer 19 and temperature sensor 18 are provided on water return pipe 14;Water level sensor 17, flow
Meter 20, water quality online analyzer 19 and temperature sensor 18 are electrically connected with PLC controller respectively.Each valve is pneumatic ball valve,
All valves are electrically connected with PLC controller.The top of double medium filters 2 is provided with dosing mouth, be provided at dosing mouth with
The flowmeter 20 of PLC controller electrical connection, to realize automatic feedback dosing;The top of double medium filters 2 is additionally provided with microvovtex
Reactor, double medium filters 2 bottom be provided with waterpower Scrubbing apparatus, realize washed by rubbing with the hands in filtrate backwash process with backwash simultaneously into
Row improves media regeneration efficiency.It further includes the cloud connecting respectively with PLC controller that the present embodiment high temperature, which fills the water fine filtration device,
Platform and management server realize automatic data collection, storage, update and teletransmission, realize mobile phone and computer terminal to equipment
Real time monitoring.
Middle water pot 12 uses enclosed oxygen isolation technology, reduces content of oxygen dissolved in water, package unit is in view of marine complicated ring
Border, selected device, pipeline, instrument and meter etc. are all made of anti-corrosion material with material, reduce corrosion of the water quality to equipment, and extending equipment makes
Use the service life.
Package unit use fully-automatic intelligent networked control systems, based on Internet of Things combine cloud platform technology, it can be achieved that
System filtering, backwash, the Automatic Control for receiving the processes such as oil, blowdown, water quality on-line analysis detection, while data can upload, it is real
Existing equipment remote monitoring and operation.By means of system flow+intelligent control element+Internet of Things technical advantage, building is information-based
Cloud platform realizes the Real-Time Sharing of equipment operating data.
Double medium filters 2, fiber ball filter 3, middle water pot 12 and filter recoil pump 13 are first unit, are ensured public security
It is second that filter 4, ultrafiltration apparatus 5, pickling tank 9, caustic treater 10, medicine, which wash pump 11, hyperfiltration reverse-rinsing pump 7 and ultrafiltration concentrate recirculation pump 8,
Unit, first unit are set to the lower section of second unit, and equipment mounted on top mode reduces occupation area of equipment, meet marine
The small feature of production platform area.
Between double medium filters 2, fiber ball filter 3, water inlet pipe 1, double medium filters 2 and fiber ball filter 3
Connecting tube and fiber ball filter 3 and cartridge filter 4 between connecting tube be connected to respectively with blow-down pipe 16, with facilitate will be residual
The emptying of extraction raffinate body.
The course of work that the present embodiment high temperature fills the water fine filtration device is as follows:
(1) normal filtration process:
Water enters double medium filters 2 by pneumatic ball valve, and double medium filters 2 carry out primary filter to water, it
Enter fiber ball filter 3 afterwards, fiber ball filter 3 carries out secondary filtration to water, through the filtered water of fiber ball filter 3
The pretreatment before ultrafiltration is carried out through cartridge filter 4, pretreated water enters ultrafiltration apparatus 5 and carries out fine processing, after processing
Water through pneumatic ball valve by 6 remittance abroad of outlet pipe;Still ensure that effluent quality is steady when water water quality is poor using three-stage filtration
Surely reach reinjected water A1 grade standard;
It should be noted that ultrafiltration is dense when water enters fiber ball filter 3 by the filtering of double medium filters 2
Water reflux pump 8 pumps the concentrated water of ultrafiltration apparatus 5 into the connecting tube between double medium filters 2 and fiber ball filter 3, so that
The concentrate recirculation water of ultrafiltration apparatus 5 and the water for passing through double medium filters 2 are collaborated, and the dense of ultrafiltration apparatus 5 can not only be made
Water recirculation water is refiltered by fiber ball filter 3, while can also reduce the temperature of water, is convenient for subsequent ultrafiltration device 5
Filtering;High temperature resistant ultrafiltration membrane is used inside ultrafiltration apparatus 5, guarantees that ultrafiltration membrane remains to work normally when water quality temperature is higher;
(2) counter-flushing process of ultrafiltration apparatus 5:
Upper backwash process: the backwashing water of ultrafiltration apparatus 5 is ultra-filtration water, and ultra-filtration water is pumped through outlet pipe 6, hyperfiltration reverse-rinsing
7 and the water outlet of ultrafiltration apparatus 5 enter the backwash regeneration that ultrafiltration apparatus 5 carries out film, sewage backwash water finally fills through ultrafiltration
The side water outlet for setting 5 tops pumps water pot 12 in 8 entrance through ultrafiltration concentrate recirculation by ultrafiltration sewage backwash pipe 15, as double media
The backwash water of filter 2 and fiber ball filter 3;
Lower backwash process: the backwashing water of ultrafiltration apparatus 5 is ultra-filtration water, and ultra-filtration water is pumped through outlet pipe 6, hyperfiltration reverse-rinsing
7 and the water outlet of ultrafiltration apparatus 5 enter the backwash regeneration that ultrafiltration apparatus 5 carries out film, sewage backwash water finally fills through ultrafiltration
The water inlet for setting 5 bottom ends pumps water pot 12 in 8 entrance through ultrafiltration concentrate recirculation by ultrafiltration sewage backwash pipe 15, as double medium mistakes
The backwash water of filter 2 and fiber ball filter 3;
The backwash of ultrafiltration apparatus 5 is carried out using upper backwash and lower backwash two ways, from both direction to ultrafiltration apparatus 5
In ultrafiltration membrane cleaned, enhance the effect of backwash, ensure that can be more thorough by ultrafiltration Membrane cleaning;
Ultrafiltration medicine wash journey:
When Pollution of Ultrafiltration Membrane in ultrafiltration apparatus 5 is serious, medicine need to be carried out to ultrafiltration apparatus 5 and washed, medicament pickling tank 9, alkali cleaning
Tank 10 washes pump 11 through medicine and enters ultrafiltration apparatus 5 to ultrafiltration membrane progress backwash and regeneration, and backwash water passes back into pickling tank 9 through outlet pipe 6
With caustic treater 10;
(3) counter-flushing process of double medium filters 2 and fiber ball filter 3:
The backwash water of double medium filters 2 and fiber ball filter 3 is the sewage backwash water of ultrafiltration apparatus 5, in
Sewage backwash water in water pot 12 respectively enters fiber ball filter 3 and double medium mistakes after the promotion of filter recoil pump 13
Filter 2 carries out the backwash and regeneration of filtrate, and sewage backwash water is finally discharged through backwash sewage pipe;
Using ultrafiltration apparatus 5 sewage backwash water as double medium filters 2 and fiber ball filter 3 backwash come
The backwash water amount of device entirety is greatly saved in water.
In the description of the present invention, it should be noted that the orientation or positional relationship of the instructions such as term " on ", "inner" is base
In orientation or positional relationship shown in the drawings, it is merely for convenience of description of the present invention and simplification of the description, rather than indication or suggestion
Signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to this
The limitation of invention.In addition, term " first ", " mat woven of fine bamboo strips two " are used for description purposes only, it is not understood to indicate or imply relatively heavy
The property wanted.
Specific examples are applied in the present invention, and principle and implementation of the present invention are described, above embodiments
Illustrate to be merely used to help understand method and its core concept of the invention;At the same time, for those skilled in the art, according to
According to thought of the invention, there will be changes in the specific implementation manner and application range.In conclusion the content of the present specification
It should not be construed as limiting the invention.
Claims (10)
1. a kind of high temperature fills the water fine filtration device, it is characterised in that: double media filtrations including passing sequentially through connecting tube connection
The water inlet of device, fiber ball filter, cartridge filter and ultrafiltration apparatus, double medium filters is connected to water inlet pipe, institute
State double medium filters and the fiber ball filter be connected to sewage backwash pipe, the water outlet of the ultrafiltration apparatus with out
Water pipe connection;
The water outlet of middle water pot is communicated with filter recoil pump, and the filter recoil pump is situated between with described pair respectively by connecting tube
The bottom of mass filter is connected to the bottom of the fiber ball filter;Water outlet and the hyperfiltration reverse-rinsing pump of the ultrafiltration apparatus
The water inlet of water outlet connection, hyperfiltration reverse-rinsing pump is connected to the outlet pipe;The top sidewall of the ultrafiltration apparatus is additionally provided with
Side water outlet, one end of ultrafiltration sewage backwash pipe are logical with the water inlet of the ultrafiltration apparatus bottom end and the side water outlet respectively
Connecting tube connection is crossed, the other end of the ultrafiltration sewage backwash pipe is connected to the water inlet that ultrafiltration concentrate recirculation pumps, described super
The water outlet of filter concentrate recirculation pump is connected to the water inlet of the middle water pot by connecting tube;It is the sewage backwash pipe, described
Valve is provided in ultrafiltration sewage backwash pipe and each connecting tube.
2. high temperature according to claim 1 fills the water fine filtration device, it is characterised in that: further include pickling tank and alkali cleaning
The top of tank, the top of the pickling tank and the caustic treater passes through connecting tube respectively and is connected to the outlet pipe, the pickling
The bottom of the tank and bottom of the caustic treater passes through connecting tube respectively is connected to the water inlet that medicine washes pump, the medicine washes the water outlet of pump
Mouth is connected to the water inlet of the cartridge filter.
3. high temperature according to claim 2 fills the water fine filtration device, it is characterised in that: the side water outlet also passes through dense
Water return pipe is connected to the water inlet that the ultrafiltration concentrate recirculation pumps.
4. high temperature according to claim 3 fills the water fine filtration device, it is characterised in that: the ultrafiltration concentrate recirculation pump with
Connecting tube between the middle water pot passes through between a connecting tube and double medium filters and the fiber ball filter
Connecting tube connection.
5. high temperature according to claim 4 fills the water fine filtration device, it is characterised in that: the middle water pot, the pickling
Water level sensor, the water inlet pipe, the outlet pipe and the concentrate recirculation Guan Shangjun are provided in tank and the caustic treater
It is provided with flowmeter, water quality online analyzer and temperature sensor;The water level sensor, the flowmeter, the water quality exist
Line analysis instrument and the temperature sensor are electrically connected with PLC controller respectively.
6. high temperature according to claim 5 fills the water fine filtration device, it is characterised in that: the valve is pneumatic ball valve,
All valves are electrically connected with the PLC controller.
7. high temperature according to claim 6 fills the water fine filtration device, it is characterised in that: the top of double medium filters
Portion is provided with dosing mouth, and the flowmeter being electrically connected with the PLC controller is provided at the dosing mouth;Double media filtrations
Microvovtex reactor is additionally provided at the top of device, the bottom of double medium filters is provided with waterpower Scrubbing apparatus.
8. high temperature according to claim 7 fills the water fine filtration device, it is characterised in that: further include respectively with the PLC
The cloud platform and management server of controller connection.
9. high temperature according to any one of claims 1 to 8 fills the water fine filtration device, it is characterised in that: double media
Filter, the fiber ball filter, the middle water pot and the filter recoil pump are first unit, security personnel's filtering
Device, the ultrafiltration apparatus, the pickling tank, the caustic treater, the medicine wash pump, hyperfiltration reverse-rinsing pump and the ultrafiltration concentrated water
Reflux pump is second unit, and the first unit is set to the lower section of the second unit.
10. high temperature according to any one of claims 1 to 8 fills the water fine filtration device, it is characterised in that: double Jie
Between mass filter, the fiber ball filter, the water inlet pipe, double medium filters and the fiber ball filter
Connecting tube between connecting tube and the fiber ball filter and the cartridge filter is connected to blow-down pipe respectively.
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CN109502853A (en) * | 2018-12-29 | 2019-03-22 | 河南绿色九州环保科技股份有限公司 | Sewerage disposing system for circulating cooling water of power plant |
Citations (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5745391A (en) * | 1980-09-02 | 1982-03-15 | Hitachi Kiden Kogyo Ltd | Backwashing method for contact filter media in immersion filter bead treatment method for sewage |
EP0460499A2 (en) * | 1990-06-02 | 1991-12-11 | Schenk-Filterbau Gesellschaft Mit Beschränkter Haftung | Method for the filtration of beverages and of chemical, pharmaceutical and similar liquids |
JP2005052689A (en) * | 2003-08-04 | 2005-03-03 | Toray Ind Inc | Membrane washing method and membrane filtration device |
JP2007196126A (en) * | 2006-01-26 | 2007-08-09 | Miura Co Ltd | Membrane filtration system |
JP2007301544A (en) * | 2006-05-12 | 2007-11-22 | Takahashi Kinzoku Kk | Membrane type oil-water separator, membrane washing method, washing system using membrane type oil-water separator, and oil-water separating system of water-soluble coolant liquid |
CN101935118A (en) * | 2010-08-16 | 2011-01-05 | 刘春喜 | Process for purifying and recycling hot water by membrane method |
CN202449890U (en) * | 2012-02-17 | 2012-09-26 | 武汉艾科滤膜技术有限公司 | Aeration type external pressure low-energy consumption running micro-filtration or ultra-filtration membrane separation system |
CN202542924U (en) * | 2012-04-26 | 2012-11-21 | 天津市华宇膜技术有限公司 | Device for preventing ultrafiltration back flush water pollution |
CN202785752U (en) * | 2012-08-20 | 2013-03-13 | 浙江东发环保工程有限公司 | Ultrafiltration membrane device |
CN103212300A (en) * | 2013-05-17 | 2013-07-24 | 中国海洋大学 | Cleaning method of ultrafiltration membrane in sea water desalination by whole membrane technology |
CN104086014A (en) * | 2014-07-29 | 2014-10-08 | 中国海洋石油总公司 | High-standard water injection refined filtration treatment process of offshore low-permeability oil field |
CN104230076A (en) * | 2013-06-13 | 2014-12-24 | 中国石油化工股份有限公司 | Processing method of reverse osmosis concentrate during urban sewage reuse process |
CN104710040A (en) * | 2015-03-19 | 2015-06-17 | 南京九思高科技有限公司 | High-recovery-rate process for treating high-sulfate-content high-hardness mine water |
CN104787931A (en) * | 2015-04-24 | 2015-07-22 | 山东恒安纸业有限公司 | Deep treatment system and process for paper-making wastewater |
CN105597634A (en) * | 2016-01-29 | 2016-05-25 | 卓达新材料科技集团有限公司 | Supercritical drying method for glass wool/silicon-aluminum aerogel composite heat preservation plate |
CN105817060A (en) * | 2016-05-24 | 2016-08-03 | 浙江金龙自控设备有限公司 | Rotating type self-scrubbing filter |
CN106044949A (en) * | 2016-07-12 | 2016-10-26 | 海南立昇净水科技实业有限公司 | Ultrafiltration membrane water purifying system and water purifying method thereof |
CN205773712U (en) * | 2016-07-01 | 2016-12-07 | 徐州腾达焦化有限公司 | Circulating sewage processing means |
CN106517248A (en) * | 2016-08-29 | 2017-03-22 | 天津膜天膜科技股份有限公司 | Refining system and refining process of brine for production of salt from sea water |
CN207659200U (en) * | 2017-11-29 | 2018-07-27 | 三达膜科技(厦门)有限公司 | Cross-flow loop ultrafiltration system |
CN209113605U (en) * | 2018-09-25 | 2019-07-16 | 浙江金龙自控设备有限公司 | A kind of high temperature water filling fine filtration device |
-
2018
- 2018-09-25 CN CN201811114411.8A patent/CN108975546B/en active Active
Patent Citations (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5745391A (en) * | 1980-09-02 | 1982-03-15 | Hitachi Kiden Kogyo Ltd | Backwashing method for contact filter media in immersion filter bead treatment method for sewage |
EP0460499A2 (en) * | 1990-06-02 | 1991-12-11 | Schenk-Filterbau Gesellschaft Mit Beschränkter Haftung | Method for the filtration of beverages and of chemical, pharmaceutical and similar liquids |
JP2005052689A (en) * | 2003-08-04 | 2005-03-03 | Toray Ind Inc | Membrane washing method and membrane filtration device |
JP2007196126A (en) * | 2006-01-26 | 2007-08-09 | Miura Co Ltd | Membrane filtration system |
JP2007301544A (en) * | 2006-05-12 | 2007-11-22 | Takahashi Kinzoku Kk | Membrane type oil-water separator, membrane washing method, washing system using membrane type oil-water separator, and oil-water separating system of water-soluble coolant liquid |
CN101935118A (en) * | 2010-08-16 | 2011-01-05 | 刘春喜 | Process for purifying and recycling hot water by membrane method |
CN202449890U (en) * | 2012-02-17 | 2012-09-26 | 武汉艾科滤膜技术有限公司 | Aeration type external pressure low-energy consumption running micro-filtration or ultra-filtration membrane separation system |
CN202542924U (en) * | 2012-04-26 | 2012-11-21 | 天津市华宇膜技术有限公司 | Device for preventing ultrafiltration back flush water pollution |
CN202785752U (en) * | 2012-08-20 | 2013-03-13 | 浙江东发环保工程有限公司 | Ultrafiltration membrane device |
CN103212300A (en) * | 2013-05-17 | 2013-07-24 | 中国海洋大学 | Cleaning method of ultrafiltration membrane in sea water desalination by whole membrane technology |
CN104230076A (en) * | 2013-06-13 | 2014-12-24 | 中国石油化工股份有限公司 | Processing method of reverse osmosis concentrate during urban sewage reuse process |
CN104086014A (en) * | 2014-07-29 | 2014-10-08 | 中国海洋石油总公司 | High-standard water injection refined filtration treatment process of offshore low-permeability oil field |
CN104710040A (en) * | 2015-03-19 | 2015-06-17 | 南京九思高科技有限公司 | High-recovery-rate process for treating high-sulfate-content high-hardness mine water |
CN104787931A (en) * | 2015-04-24 | 2015-07-22 | 山东恒安纸业有限公司 | Deep treatment system and process for paper-making wastewater |
CN105597634A (en) * | 2016-01-29 | 2016-05-25 | 卓达新材料科技集团有限公司 | Supercritical drying method for glass wool/silicon-aluminum aerogel composite heat preservation plate |
CN105817060A (en) * | 2016-05-24 | 2016-08-03 | 浙江金龙自控设备有限公司 | Rotating type self-scrubbing filter |
CN205773712U (en) * | 2016-07-01 | 2016-12-07 | 徐州腾达焦化有限公司 | Circulating sewage processing means |
CN106044949A (en) * | 2016-07-12 | 2016-10-26 | 海南立昇净水科技实业有限公司 | Ultrafiltration membrane water purifying system and water purifying method thereof |
CN106517248A (en) * | 2016-08-29 | 2017-03-22 | 天津膜天膜科技股份有限公司 | Refining system and refining process of brine for production of salt from sea water |
CN207659200U (en) * | 2017-11-29 | 2018-07-27 | 三达膜科技(厦门)有限公司 | Cross-flow loop ultrafiltration system |
CN209113605U (en) * | 2018-09-25 | 2019-07-16 | 浙江金龙自控设备有限公司 | A kind of high temperature water filling fine filtration device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109502853A (en) * | 2018-12-29 | 2019-03-22 | 河南绿色九州环保科技股份有限公司 | Sewerage disposing system for circulating cooling water of power plant |
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