CN207076349U - A kind of packaging type super-filter purifying device - Google Patents
A kind of packaging type super-filter purifying device Download PDFInfo
- Publication number
- CN207076349U CN207076349U CN201720889441.0U CN201720889441U CN207076349U CN 207076349 U CN207076349 U CN 207076349U CN 201720889441 U CN201720889441 U CN 201720889441U CN 207076349 U CN207076349 U CN 207076349U
- Authority
- CN
- China
- Prior art keywords
- water
- pipeline
- ultrafiltration membrane
- membrane pressure
- vertical
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of packaging type super-filter purifying device, including packaging open frame, milipore filter film group, water inlet system, water production system, backwashing system, on-line cleaning filter, selecting type medicament addition device and control system, milipore filter film group includes the ultrafiltration membrane pressure container that at least one interior plummet is disposed with least ten film wires, water inlet system connects with raw water, water inlet system and each ultrafiltration membrane pressure reservoir, water inlet system successively connects with selecting type medicament addition device and on-line cleaning filter, water production system front and back end connects with each vertical ultrafiltration membrane pressure container and water producing tank respectively, backwashing system respectively with backwash water and each vertical ultrafiltration membrane pressure reservoir, control system is all connected with miscellaneous part respectively.A kind of packaging type super-filter purifying device of the utility model is simple in construction, realizes a variety of membrane components or pressure vessel general exchange, the purified treatment suitable for multiple-quality water, purification efficiency is high, can effectively reduce cost.
Description
Technical field
A kind of filter is the utility model is related to, more particularly to a kind of packaging type super-filter purifying device.
Background technology
At present, for the water process in industrial and municipal field, possessed some all-in-one formula super-filter purifying devices, but this
A little all-in-one formula super-filter purifying devices are only applicable to the supply of family drinking water mostly, or indivedual industrial circle water demands compared with
The sewage disposal of small enterprise.Due to the complexity of ultrafiltration system itself, its integrating device is caused to be difficult to transport, install, it is difficult to
Multiple-quality water demand is tackled with simple technological means, how different pretreatments medicament is added according to the difference of water quality, how had
Effect prevents that film is dirty stifled, how easy completion integrity detection, judge system fracture of wire etc., therefore these all-in-one formula ultrafiltration water purification
Limitation on device technique limits its application in the middle-size and small-size water process project in industrial and municipal field.In addition, at present
Ultrafiltration membrane elements do not have unified standard, and commercial ultra-filtration membrane component size differs, exist full stream, cross-flow, backwash, just wash,
A variety of methods of operation such as air bump rinse operation, cause the bundle sale of ultrafiltration membrane elements and super-filter purifying device, and film strips are changed for the later stage
Limitation, while add ultrafiltration membrane system Life cycle capital cost.
The content of the invention
The utility model is completed to solve deficiency of the prior art, and the purpose of this utility model is to provide one
Plant general exchange simple in construction, to realize a variety of membrane components or pressure vessel, the purified treatment suitable for multiple-quality water, purification effect
Rate is high, can effectively reduce the packaging type super-filter purifying device of cost.
A kind of packaging type super-filter purifying device of the present utility model, including packaging open frame and it is installed on the packaging type
The milipore filter film group of machine frame inside, water inlet system, water production system, backwashing system, on-line cleaning filter, selecting type medicament are thrown
Feeder apparatus and control system, the milipore filter film group include at least one vertical ultrafiltration membrane pressure container, the ultrafiltration membrane pressure
Plummet is disposed with least ten film wires in container, and the water inlet system front end is with being arranged at the packaging type Shelf External
The adjustable connection of raw water, the water inlet system rear end with it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, institute
State and successively connected in the middle part of water inlet system with the selecting type medicament addition device and the on-line cleaning filter, the selection
Formula medicament addition device includes at least four pharmacy jars and medicament delivery pipeline, the medicament delivery pipeline respectively with the water inlet
System connects with the backwashing system adjustable-flow, the water production system front and back end respectively with each vertical ultrafiltration mould
Force container connects with the water producing tank positioned at the packaging type Shelf External or with adjustable-flow at water, the backwashing system front end
With middle part respectively with backwash water and it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, the control system difference
With the milipore filter film group, the water inlet system, the backwashing system, the water production system, the on-line cleaning filter
It is all connected with the selecting type medicament addition device.
A kind of packaging type super-filter purifying device of the present utility model can also be：
The packaging type machine frame inside is located at the milipore filter film group opening position and is provided with the transfer pipeline for surrounding framework, institute
The top for stating transfer pipeline is located at opening position on the top of the milipore filter film group to lower and bottom, the transfer pipeline
Bottom is located at the opening position on the bottom of the milipore filter film group, and the transfer pipeline flows with water inlet system and backwashing system
Measure adjustable connection.
The transfer pipeline includes the upper lateral tube for being positioned horizontally in upper and lower part and lower transverse tubule and is vertically arranged at left part
Left vertical tube and right vertical tube with right part, the left vertical tube and right vertical tube are respectively perpendicular and are arranged at the upper lateral tube and the lower transverse tubule
Left and right end portions, the upper lateral tube left and right ends connect with the left vertical tube and right riser upper end respectively, a left side for the lower transverse tubule
Lower end of the right both ends respectively with the left vertical tube and the right vertical tube connects, and the upper lateral tube, lower transverse tubule and right vertical tube are and institute
Water inlet system connection is stated, the left vertical tube connects with the backwashing system, and the upper lateral tube and the lower transverse tubule are located at institute respectively
State below vertical ultrafiltration membrane pressure container top and at the top position of bottom.
The water inlet system includes inlet pipeline, water inlet interface and the intake pump for adjusting flow, the inlet pipeline
By water inlet interface with needing the water of filtration, purification to connect, the intake pump is arranged on the inlet pipeline for front end, it is described enter
Water lines interlude passes through enterprising moisture pipe respectively with being connected in the middle part of transfer pipeline among the upper and lower part of the transfer pipeline
Be in charge of and connected with the latter half adjustable-flow of the inlet pipeline with lower water inlet, the inlet pipeline rear end respectively with it is each
The vertical adjustable connection of ultrafiltration membrane pressure container flow, the on-line cleaning filter are arranged at the intake pump and institute
Between stating transfer pipeline, the selecting type medicament addition device be arranged at the intake pump and the on-line cleaning filter it
Between.
The backwashing system includes backwash pipeline, backwash water out and the backwashing pump on backwash pipeline, the backwash
The front end of pipeline is connected with backwash water by backwashing pump adjustable-flow, the end of the backwash pipeline with it is each described vertical super
Filter membrane pressure vessel connect, the backwash pipeline it is upper in the backwashing pump between the vertical ultrafiltration membrane pressure container with institute
The connection of selecting type medicament addition device adjustable-flow is stated, the latter half of the backwash pipeline connects with the transfer pipeline,
The backwash water out is arranged at the backwash pipeline latter half end.
The backwash pipeline is provided with before entering the vertical ultrafiltration membrane pressure container and is total to what the water production system shared
With pipeline, the common conduit is arranged at the over top of the vertical ultrafiltration membrane pressure container, the common conduit with it is each
The equal adjustable-flow connection of the vertical ultrafiltration membrane pressure container, the latter half of the backwash pipeline be provided with it is described enter water system
The common-use tunnel that system passes through, the common-use tunnel connect with the transfer pipeline.
The water production system includes water producing pipe road and production water out, and the water producing pipe road is located at the vertical ultrafiltration membrane pressure
The top of container, the water producing pipe road connect with each vertical equal adjustable-flow of ultrafiltration membrane pressure container, the production water
Outlet is arranged at the end on the water producing pipe road, and the production water out is with water producing tank or with being connected at water.
The selecting type medicament addition device includes at least four pharmacy jars and the medicament delivery pipeline, and described at least four
The acid medicine and basic agent for strengthening backwash for chemistry are respectively provided with two pharmacy jars in individual pharmacy jar, residue is at least
Two pharmacy jars, which take up, to be respectively provided with for adding in the tiny flocculation agent in raw water and coagulant, and each pharmacy jar is and institute
State the adjustable connection of medicament delivery piping flow.
Compound pump is provided with each pharmacy jar, the compound pump adjustable-flow is arranged at the medicament delivery
On pipeline.
The packaging type machine frame inside is provided with moving air detection means, the moving air detection means and each institute
Vertical ultrafiltration membrane pressure container is stated to connect.
A kind of packaging type super-filter purifying device of the present utility model, including packaging open frame and it is installed on the packaging type
The milipore filter film group of machine frame inside, water inlet system, water production system, backwashing system, on-line cleaning filter, selecting type medicament are thrown
Feeder apparatus and control system, the milipore filter film group include at least one vertical ultrafiltration membrane pressure container, the ultrafiltration membrane pressure
Plummet is disposed with least ten film wires in container, and the water inlet system front end is with being arranged at the packaging type Shelf External
The adjustable connection of raw water, the water inlet system rear end with it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, institute
State and successively connected in the middle part of water inlet system with the selecting type medicament addition device and the on-line cleaning filter, the selection
Formula medicament addition device includes at least four pharmacy jars and medicament delivery pipeline, the medicament delivery pipeline respectively with the water inlet
System connects with the backwashing system adjustable-flow, the water production system front and back end respectively with each vertical ultrafiltration mould
Force container connects with the water producing tank positioned at the packaging type Shelf External or with adjustable-flow at water, the backwashing system front end
With middle part respectively with backwash water and it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, the control system difference
With the milipore filter film group, the water inlet system, the backwashing system, the water production system, the on-line cleaning filter
It is all connected with the selecting type medicament addition device.So, its mainly applied to 50-5000 ton per day low discharges industry and
The water process in municipal field.Raw water can be underground water, surface water and the sanitary sewage through two stage treatment or industrial wastewater, sea
Water etc..Production water after processing can be used directly, also can be as the water inlet of successive depths processing.So when in use, needs are worked as
During filtering, control system detects the water quality for needing raw water to be processed first, and adjusts selecting type adding of agent according to water quality situation
Device needs the species for the medicament launched and measured, it is necessary to which the raw water handled is entered in packaging open frame by water inlet system
Portion, before on-line cleaning filter is entered, thrown using the selecting type medicament connected with water inlet system adjustable-flow
Feeder apparatus will select the medicament of species according to raw water quality before and a selected amount of medicament is added in water inlet system and carried out with raw water
The physical-chemical reactions such as mixed sufficient tiny flocculation, coagulation so that a part of pollutant is directly removed, and contaminant remaining is then
The small flco that can be removed by ultra-filtration filters is formed, these mixed liquors are then delivered to on-line cleaning filter, this
Sample, which can compare a part of particle pollutant and floccule of the major diameter between 100-300 μm, to be filtered, remaining
Mixed liquor is expelled to water inlet system from the online cleaning and filtrating equipment that inclines, and then enters back into each vertical ultrafiltration membrane pressure and holds
Ultra-filtration filters are carried out in device, the amount for the raw water that can be handled as needed sets one or more vertical ultrafiltration membrane pressure to hold
Device.And membrane component can select inner pressed membrane component to select outer formula membrane component in pressure vessel, i.e., need not limit
It is which kind of membrane component.Filtering into the mixed liquor in vertical ultrafiltration membrane pressure container Jing Guo film wire, by floccule, suspension and
Colloidal substance filters out, and is purified water and produces water.Production water after the filtering of vertical ultrafiltration membrane pressure container is from water production system
It is expelled to production water tank or with place of water.After running a period of time, film wire table of the pollutant in vertical ultrafiltration membrane pressure container
Face is enriched with so that the increase of milipore filter film wire transmembrane pressure, membrane flux reduce.After transmembrane pressure increases to default value, control
System control backwashing system processed is opened, and is now closed water inlet system, is carried out the backwash of vertical ultrafiltration membrane pressure container.In backwash
Cheng Zhong, production water can be used as backwash water, can also select to be separately provided backwash water, backwash water enters each vertical by backwashing system
In ultrafiltration membrane pressure container, each film wire can remove the polluter of film wire surface retention under backwash water flushing action, reduce
Transmembrane pressure, recover membrane flux, and then recover the filter capacity of the film wire in each vertical ultrafiltration membrane pressure container, improve whole
The filter efficiency and filter capacity of the milipore filter film group of body, effectively extend the life-span of film wire, that is, extend the vertical ultrafiltration mould
In the life-span of force container, reduce maintenance cost.Certainly, if by backwash several times, when membrane flux recovers not comply with one's wishes, then need to carry out
Chemical enhanced cleaning, now control system control fill the selecting type adding of agent connected with backwashing system adjustable-flow
Put unlatching so that the chemistry that film wire in a certain amount of cleaning vertical ultrafiltration membrane pressure container can be added in backwash water is clear
Lotion, the backwash water for being so mixed with chemical enter each vertical ultrafiltration membrane pressure cleaning container film wire, Ke Yiyou
Effect recovers the membrane flux of film wire, improves milipore filter film group filter efficiency, and extends the service life of milipore filter film group, effectively reduces
Maintenance and operating cost.And because the mixed liquor for entering each vertical ultrafiltration membrane pressure container can carry out flow control,
And then ensure that the water for supplying each vertical ultrafiltration membrane pressure container is consistent, then it is further ensured that film wire pair
In the uniformity of pollutant retention, extend the life-span of film, reduce operating cost.Because control system can be according to the original detected
The species of medicament and the amount of each medicament that water water quality adjustment is added in raw water, therefore the raw water of different quality can be handled, expand
The scope of the raw water of processing, improve the scope of application of overall packaging type super-filter purifying device.Simultaneously because vertical ultrafiltration is set
Film film group, therefore different membrane components can be set according to different situations, you can to set inner pressed membrane component, can also set
External-compression type membrane component is put, can also be other kinds of membrane component, so this packaging type super-filter purifying device can be caused to have
Well compatibility, can according to requirement and water quality characteristicses from different types, different size membrane component, Er Qieke
To realize a variety of methods of operation, reach good operational effect.A kind of packaging type super-filter purifying device of the present utility model, relatively
It is in the advantages of prior art：It is simple in construction, realize the general exchange of a variety of membrane components in pressure vessel, suitable for multiple-quality water
Purified treatment, purification efficiency is high, can effectively reduce cost.
Brief description of the drawings
Schematic diagram on front side of a kind of packaging type super-filter purifying device of Fig. 1 the utility model.
Schematic diagram on rear side of a kind of packaging type super-filter purifying device of Fig. 2 the utility model.
A portions enlarged drawing in a kind of packaging type super-filter purifying device Fig. 2 of Fig. 3 the utility model.
Figure number explanation
1 ... intake pump 2 ... inlet pipeline 3 ... on-line cleaning filter
4 ... ultrafiltration membrane pressure container 5 ... backwash pipeline 6 ... backwashing pumps
7 ... selecting type medicament addition device 8 ... guidance panel 9 ... control systems
10 ... moving air detection means 11 ... packaging open frame 12 ... upper lateral tubes
The left right vertical tube of vertical tube 15 ... of 13 ... lower transverse tubules 14 ...
16 ... backwash water out 17 ... water inlet interfaces 18 ... produce water out
19 ... production supply mains 20 ... production water branch pipe 21 ... pharmacy jars
22 ... compound pump 23 ... medicament delivery pipelines
Embodiment
Fig. 1 below in conjunction with the accompanying drawings to Fig. 3 makees further detailed to a kind of packaging type super-filter purifying device of the present utility model
Describe in detail bright.
A kind of packaging type super-filter purifying device of the present utility model, it refer to Fig. 1 related each figures into Fig. 3, including packaging
Open frame 11 and the milipore filter film group being installed on inside the packaging open frame 11, water inlet system, water production system, backwash system
System, on-line cleaning filter 3, selecting type medicament addition device 7 and control system 9, the milipore filter film group include at least one
Individual vertical ultrafiltration membrane pressure container 4, plummet is disposed with least ten film wires in the ultrafiltration membrane pressure container 4, it is described enter
Water system front end with the raw water flow being arranged at outside the packaging open frame 11 is adjustable connects, the water inlet system rear end with
The each vertical adjustable-flow of ultrafiltration membrane pressure container 4 connection, water inlet system middle part priority and the selecting type medicine
Agent throwing device 7 connects with the on-line cleaning filter 3, and the selecting type medicament addition device 7 includes at least four medicines
Agent tank 21 and medicament delivery pipeline 23, the medicament delivery pipeline 23 respectively with the water inlet system and the backwashing system flow
Adjustable connection, the water production system front and back end is respectively with each vertical ultrafiltration membrane pressure container 4 and positioned at the packaging
Water producing tank outside open frame 11 is connected with adjustable-flow at water, the backwashing system front end and middle part respectively with backwash water
Connected with each vertical adjustable-flow of ultrafiltration membrane pressure container 4, the backwashing system rear end is with being arranged at the packaging
The backwash water collecting device connection of discharge outside open frame 11, the control system 9 respectively with the milipore filter film group, described
Water inlet system, the backwashing system, the water production system, the on-line cleaning filter 3 and the selecting type adding of agent
Device 7 is all connected with.So, it is mainly applied to the water process in the industrial and municipal field of 50-5000 ton per day low discharges.It is former
Water can be underground water, surface water and sanitary sewage through two stage treatment or industrial wastewater, seawater etc..Production water after processing is
It can be used directly, also can be as the water inlet of successive depths processing.So when in use, when needing filtering, control system 9 is first
Detection needs the water quality of raw water to be processed, and the medicament for needing to launch according to water quality situation regulation selecting type medicament addition device 7
Species and amount, it is necessary to which the raw water handled is entered inside packaging open frame 11 by water inlet system, into on-line cleaning
Before filter 3, basis before being incited somebody to action using the selecting type medicament addition device 7 connected with water inlet system adjustable-flow
The medicament and a selected amount of medicament of the selected species of raw water quality are added in water inlet system to carry out mixing sufficient tiny flocculation, mixes with raw water
It is solidifying to wait physical-chemical reaction so that a part of pollutant is directly removed, and contaminant remaining, which is then formed, can pass through ultrafiltration
Then these mixed liquors are delivered to on-line cleaning filter 3 by the small flco being filtered to remove, so can be by a part
Grain, which will compare pollutant and floccule of the major diameter between 100-300 μm, to be filtered, and remaining mixed liquor inclines clearly from online
Wash and water inlet system is expelled in filter, then enter back into and ultra filtration is carried out in each vertical ultrafiltration membrane pressure container 4
Filter, the amount for the raw water that can be handled as needed set one or more vertical ultrafiltration membrane pressure container 4.And pressure vessel
Interior membrane component can select inner pressed membrane component to select outer formula membrane component, i.e., which kind of membrane component need not limit is.
Filtering into the mixed liquor in vertical ultrafiltration membrane pressure container 4 Jing Guo film wire, floccule, suspension and colloidal substance are filtered
Fall, be purified water and produce water.Production water after the filtering of vertical ultrafiltration membrane pressure container 4 is expelled to production water water from water production system
Case or with place of water.After running a period of time, film wire surface enrichment of the pollutant in vertical ultrafiltration membrane pressure container 4 so that
The increase of milipore filter film wire transmembrane pressure, membrane flux reduce.After transmembrane pressure increases to default value, control system 9 controls
Backwashing system is opened, and is now closed water inlet system, is carried out the backwash of vertical ultrafiltration membrane pressure container 4.In backwash process, water is produced
Backwash water can be used as, can also select to be separately provided backwash water, backwash water enters each vertical ultrafiltration mould by backwashing system
In force container 4, each film wire can remove the polluter of film wire surface retention under backwash water flushing action, reduce transmembrane pressure
Difference, recover membrane flux, and then recover the filter capacity of the film wire in each vertical ultrafiltration membrane pressure container 4, improve overall
The filter efficiency and filter capacity of milipore filter film group, effectively extend the life-span of film wire, that is, extend the vertical ultrafiltration membrane pressure and hold
In the life-span of device 4, reduce maintenance cost.Certainly, if by backwash several times, when membrane flux recovers not comply with one's wishes, then needs
Learn and strengthen cleaning, now control system 9, which controls, fills the selecting type adding of agent connected with backwashing system adjustable-flow
Put 7 unlatchings so that the chemistry of film wire in a certain amount of cleaning vertical ultrafiltration membrane pressure container 4 can be added in backwash water
Cleaning agent, the backwash water for being so mixed with chemical enter each vertical ultrafiltration membrane pressure container 4 and clean film wire, can be with
Effectively recover the membrane flux of film wire, improve milipore filter film group filter efficiency, and extend the service life of milipore filter film group, effectively drop
Low-maintenance and operating cost.And because the mixed liquor for entering each vertical ultrafiltration membrane pressure container 4 can carry out flow control
System, and then ensure that the water for supplying each vertical ultrafiltration membrane pressure container 4 is consistent, then it is further ensured that film
Silk extends the life-span of film, reduces operating cost for the uniformity of pollutant retention.Because control system 9 can be according to detection
To raw water quality the regulation species of medicament and the amount of each medicament that add in raw water, therefore the original of different quality can be handled
Water, the scope of the raw water of processing is expanded, improve the scope of application of overall packaging type super-filter purifying device.Simultaneously because set vertical
Formula milipore filter film group, therefore different membrane components can be set according to different situations, you can to set inner pressed membrane component,
External-compression type membrane component can be set, can also be other kinds of membrane component, can so cause this packaging type ultrafiltration water purification cartridge
Put with well compatibility, can according to requirement and water quality characteristicses from different types, different size membrane component,
And a variety of methods of operation can be realized, reach good operational effect.A kind of packaging type ultrafiltration water purification cartridge of the present utility model
Put, be relative to the advantages of prior art：It is simple in construction, realize the general exchange of membrane component in a variety of pressure vessels, be applied to
The purified treatment of multiple-quality water, purification efficiency is high, can effectively reduce cost.Wherein control system 9 control each system open or
Close or control flow, while control each vertical ultrafiltration membrane pressure container 4 to carry out filtering reaction.Certainly described control system
System 9 can be intelligence control system 9, as long as milipore filter film group, water inlet system, water production system, backwash system can be automatically controlled
System, on-line cleaning filter 3, selecting type medicament addition device 7 according to process and time and need what is carried out to filter, instead
Wash, produce water etc..Additionally, due to above-mentioned milipore filter film group, water inlet system, water production system, backwashing system, on-line cleaning filtering
Device 3, selecting type medicament addition device 7 may be contained within above-mentioned packaging open frame 11, therefore transport and install more convenient, have
Beneficial to long-distance transport and installation.Control system 9 connects with a guidance panel 8, and guidance panel 8 has Operation switch and operation knob,
Control system 9 transmits a signal to display instrument, it is shown the operational factor in packaging type super-filter purifying device running,
Such as pressure, flow, actuating procedure switch or rotation process knob can control the control system 9 to control each part
System.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The packaging open frame 11, which is internally located at the milipore filter film group opening position and is provided with, to be surrounded
The transfer pipeline of framework, the top of the transfer pipeline are located at the position on top to the lower and bottom of the milipore filter film group
Place, the bottom of the transfer pipeline are located at the opening position on the bottom of the milipore filter film group, the transfer pipeline and water inlet
System connects with the equal adjustable-flow of backwashing system.The conveying for surrounding framework being arranged at the milipore filter film group neighbouring position
Pipeline can change the position that water inlet system enters each vertical ultrafiltration membrane pressure container 4.Various membrane elements can so be met
The different running method of part, therefore increase the compatibility of the vertical ultrafiltration membrane pressure container 4, further increase packaging type ultrafiltration
The filtering scope of application of purifier.Further preferred technical scheme is in the technology of previous technique scheme：The conveying
Pipeline includes the upper lateral tube 12 for being positioned horizontally in upper and lower part and lower transverse tubule 13 and is vertically arranged at left part and a left side for right part is erected
Pipe 14 and right vertical tube 15, the left vertical tube 14 and right vertical tube 15, which are respectively perpendicular, is arranged at the upper lateral tube 12 and the lower transverse tubule 13
Left and right end portions, the left and right ends of upper lateral tube 12 connect with the left vertical tube 14 and the upper end of right vertical tube 15 respectively, the lower horizontal stroke
Lower end of the left and right ends of pipe 13 respectively with the left vertical tube 14 and the right vertical tube 15 connects, the upper lateral tube 12, lower transverse tubule
13 and right vertical tube 15 connected with the water inlet system, the left vertical tube 14 connects with the backwashing system, the upper lateral tube 12
With the lower transverse tubule 13 respectively below the vertical top of ultrafiltration membrane pressure container 4 and at the top position of bottom.So, institute
Upper lateral tube 12, right vertical tube 15, lower transverse tubule 13 and left vertical tube 14 that transfer pipeline includes being sequentially communicated are stated, is so existed into can
Upper lateral tube 12 or lower transverse tubule 13 are turned on and off in the presence of control system 9 so that the needs of conveying surpass in water inlet system
The mixed liquor of filtration filter is delivered to the vertical ultrafiltration membrane pressure from each vertical top of ultrafiltration membrane pressure container 4 or bottom
In container 4, and then expand the scope of application of the vertical ultrafiltration membrane pressure container 4, you can to increase the vertical milipore filter
The method of operation of pressure vessel 4, improve filter efficiency and the flexibility of the vertical ultrafiltration membrane pressure container 4.Certainly due to entering
A part for water system overlaps setting with a backwashing system part, therefore backwashing system also connects with the transfer pipeline, convenient
Rinse in each vertical ultrafiltration membrane pressure container 4 the backwash water discharge of pollutant and floccule etc. in film wire.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The water inlet system includes inlet pipeline 2, water inlet interface 17 and for adjusting entering for flow
Water pump 1, by water inlet interface 17 with needing the water of filtration, purification to connect, the intake pump 1 is arranged at for the front end of inlet pipeline 2
On the inlet pipeline 2, the interlude of inlet pipeline 2 in the middle part of transfer pipeline with connecting, and the top of the transfer pipeline is with
It is in charge of respectively by enterprising moisture pipe and lower water inlet among portion and is connected with the latter half adjustable-flow of the inlet pipeline 2,
The rear end of inlet pipeline 2 connects with each vertical adjustable-flow of ultrafiltration membrane pressure container 4 respectively, the on-line cleaning
Filter 3 is arranged between the intake pump 1 and the transfer pipeline, and the selecting type medicament addition device 7 is arranged at institute
State between intake pump 1 and the on-line cleaning filter 3.So, raw water is passed through entrance water interface by intake pump 1 when in use
It is pumped into the first half of inlet pipeline 2, then by the selecting type medicament addition device 7 by the water quality of the raw water according to suction
The medicament mixing of the species and amount of selection, which adds in inlet pipeline 2 to mix with raw water, carries out the reaction such as tiny flocculation and coagulation, removes
A part of pollutant, then mixture, which enters in the on-line cleaning filter 3, filters out the pollutant of bulky grain and cotton-shaped
Thing, then mixed liquor be again introduced into the stage casing of water inlet system, subsequently into the transfer pipeline, under the control of control system 9
Entered according to selected pattern from top or bottom and ultra-filtration filters are carried out in the vertical ultrafiltration membrane pressure container 4, after filtering
Discharged out of water production system.The latter half of certain inlet pipeline 2 can include water inlet manifold and water inlet pipe, water inlet branch
Pipe quantity is consistent with the quantity of the vertical ultrafiltration membrane pressure container 4, the water inlet pipe and the corresponding vertical milipore filter
The adjustable-flow of pressure vessel 4 connects, and the other end of the water inlet pipe connects with the water inlet manifold, can so pass through control
The amount for the mixed liquor that the control of system 9 processed enters each vertical ultrafiltration membrane pressure container 4 is consistent, is ensured into described vertical
The uniformity of the mixed liquor of ultrafiltration membrane pressure container 4, extend film wire service life, reduce maintenance cost.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The backwashing system includes backwash pipeline 5, backwash water out 16 and positioned at backwash pipeline 5
On backwashing pump 6, the front end of the backwash pipeline 5 connected with backwash water by the adjustable-flow of backwashing pump 6, the backwash pipeline
5 end connects with each vertical ultrafiltration membrane pressure container 4, on the backwash pipeline 5 positioned at the backwashing pump 6 with it is described
Connected between vertical ultrafiltration membrane pressure container 4 with the adjustable-flow of selecting type medicament addition device 7, the backwash pipeline 5
Latter half connected with the transfer pipeline, the backwash water out 16 is arranged at the latter half end of backwash pipeline 5.
So in use for some time, membrane filtration efficiency comparison is low or when filter effect is bad, and control system 9 controls first half
Water inlet system and at least latter half water production system are out of service or close, and backwashing pump 6 either individually sets production water before
The backwash water put is pumped to backwash pipeline 5, and each vertical ultrafiltration mould is delivered in adjustable-flow by backwash pipeline 5
In force container 4, the amount for the backwash water that the control backwash of control system 9 pipeline 5 enters in the vertical ultrafiltration membrane pressure container 4 is one
Cause, ensure that each vertical ultrafiltration membrane pressure container 4 is equably cleaned.Backwash water enters the vertical ultrafiltration membrane pressure and held
In device 4, backward erosion film wire, after the pollutant that will be attached on film wire inwall or outer wall, floccule and colloidal substance wash away
Discharged from the latter half end of backwash pipeline 5 by backwash water out 16, so reduce transmembrane pressure, recovered membrane flux, enter
And recover the filter capacity of the film wire in each vertical ultrafiltration membrane pressure container 4, improve the filtering of overall milipore filter film group
Efficiency and filter capacity, effectively extend the life-span of film wire, that is, extend the life-span of the vertical ultrafiltration membrane pressure container 4, reduce dimension
Protect cost.Certainly, after by backwash several times, control system 9 can also be by running the selecting type medicament addition device 7
A selected amount of acid medicine and basic agent are added in backwashing system so that be mixed with the backwash water of medicament to each described vertical
Ultrafiltration membrane pressure container 4 carries out reinforcing Chemical cleaning, further extends the life-span of film wire, reduces maintenance cost.In previous technique
The technical further preferred technical scheme of scheme is：The backwash pipeline 5 enter the vertical ultrafiltration membrane pressure container 4 it
Preceding to be provided with the common conduit shared with the water production system, the common conduit is arranged at the vertical ultrafiltration membrane pressure container 4
Over top, the common conduit connects with each vertical 4 equal adjustable-flow of ultrafiltration membrane pressure container, the backwash
The latter half of pipeline 5 is provided with the common-use tunnel passed through with the water inlet system, and the common-use tunnel connects with the transfer pipeline
It is logical.So, because backwash pipeline 5 and water production system are provided with shared common conduit, backwash pipeline 5 has shared with water inlet system
Common-use tunnel, therefore effectively reduce the complexity of pipeline, reduce the length of each pipeline, reduce pipeline and set, further reduce
Cost, while meet requirement of the different membrane components for different running method well.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The water production system includes water producing pipe road and production water out 18, and the water producing pipe road is located at
The top of the vertical ultrafiltration membrane pressure container 4, the water producing pipe road and each vertical 4 equal flow of ultrafiltration membrane pressure container
Adjustable connection, the production water out 18 are arranged at the end on the water producing pipe road, the production water out 18 and water producing tank or use
Connected at water.Purified water so after each vertical ultrafiltration membrane pressure container 4 of the milipore filter film group filters produces water
Water producing tank is delivered to from water producing pipe road by producing water out 18 or with water.Because the control supply of control system 9 is each described vertical
The water of formula ultrafiltration membrane pressure container 4 is consistent, hence in so that water producing pipe road can be equably from each vertical ultrafiltration mould
The output of force container 4 produces water, ensures the uniformity of each vertical aquifer yield of ultrafiltration membrane pressure container 4, avoids vertical ultrafiltration mould
The uneven equal loss of membrane component technical scheme further preferred in the technology of previous technique scheme is in force container 4：It is described
Water producing pipe road includes production supply mains 19 and production water branch pipe 20, and production supply mains 19 connects with production water out 18, the production water branch pipe 20
Quantity it is consistent with the quantity of the vertical ultrafiltration membrane pressure container 4, one end of the production water branch pipe 20 described is stood with corresponding
Formula ultrafiltration membrane pressure container 4 connects, and the other end of the production water branch pipe 20 is equalWithThe production supply mains 19 connects, described vertical super
Production water in filter membrane pressure vessel 4 from production 20 uniform output of water branch pipe and then is collected to after production supply mains 19 by producing water out 18
Discharge.And the common-use tunnel that water production system noted earlier shares with the backwash pipeline 5 can be production supply mains 19 and each production water
Branch pipe 20.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The selecting type medicament addition device 7 includes at least four pharmacy jars 21 and the medicament
Pipeline 23 is launched, the acid for strengthening backwash for chemistry is respectively provided with two pharmacy jars 21 at least four pharmacy jar 21
Property medicament and basic agent, remaining at least two pharmacy jars 21 take up be respectively provided with for adding in the tiny flocculation agent in raw water and
Coagulant, each pharmacy jar 21 connect with the adjustable-flow of medicament delivery pipeline 23.If set certainly more
Pharmacy jar 21 when, adsorbent and reactant can be separately added into multiple pharmacy jars, as existed to film in the raw water
Element has during the material of detrimental effect, it is necessary to add tiny flocculation agent, such as aluminium polychloride, polyaluminium sulfate, plays tiny flocculation
Membrane component in effect protection packaging type super-filter purifying device, influence effluent quality when excessive colloid or suspension in raw water be present
When, it is necessary to add coagulant, such as aluminum sulfate, ferrous sulfate, ferric trichloride, improve the filtering effect of packaging type super-filter purifying device
Rate, when more organic matter in raw water be present, it is necessary to add adsorbent, such as wet type activated carbon, flyash, pass through the suction of adsorbent
It is attached effect remove partial organic substances, when phosphorus in raw water be present, it is necessary to add reactant, such as aluminium chloride, lime, reactant with
Polymerisation occurs for the phosphorus in raw water, improves clearance of the packaging type super-filter purifying device to phosphorus.So, control system 9 can be with
The water quality selection of the raw water handled as needed extracts variety classes and different amounts of medicine out of it internal multiple pharmacy jars 21
Added after agent mixing by medicament delivery pipeline 23 in water inlet system, tiny flocculation and coagulation etc. are carried out to the raw water in water inlet system
Reaction treatment, remove a part of pollutant.Certainly it is also an option that backwashing system is added after acid medicine or basic agent, to institute
State vertical ultrafiltration membrane pressure container 4 and carry out reinforcing Chemical cleaning.So expand the species of accessible raw water, expand whole packaging
The scope of application of formula super-filter purifying device.Further preferred technical scheme is in the technology of previous technique scheme：Each institute
State and compound pump 22 is provided with pharmacy jar 21, the adjustable-flow of compound pump 22 is arranged at the medicament delivery pipeline 23
On.
A kind of packaging type super-filter purifying device of the present utility model, Fig. 1 related each figures into Fig. 3 are refer to, in above skill
It can also be on the basis of art scheme：The packaging open frame 11 is internally provided with moving air detection means 10, the flowing
Air detecting device 10 connects with each vertical ultrafiltration membrane pressure container 4.The moving air detection means 10 is every
The individual vertical ultrafiltration membrane pressure container 4 provides compressed air.Control system 9 can control water inlet system and backwashing system to close
Close, start moving air detection means 10 and compressed air is passed through in each vertical ultrafiltration membrane pressure container 4, compressed air is led to
Enter so that membrane component influent side and production or change at water lateral pressure in the ultrafiltration membrane pressure container 4, the control system 9 will
The pressure value detected is delivered to the display instrument of the guidance panel 8 on the packaging open frame 11, according to display
The change for the pressure value that instrument is shown, and then detect that the membrane component in which vertical ultrafiltration membrane pressure container 4 is to damage
Bad, the convenient membrane component changed in time in the vertical ultrafiltration membrane pressure container 4, it can so ensure the same of filter efficiency
When, the membrane component in the vertical ultrafiltration membrane pressure container 4 is changed in time, it is not necessary to vertical ultrafiltration membrane pressure described in integral demounting
Membrane component in container 4 is the breakage that can determine whether membrane component, reduces operation difficulty, and then reduce operating cost.
It is above-mentioned that only several specific embodiments in the utility model are illustrated, but can not be used as of the present utility model
Protection domain, equivalent change or modification or equal proportion amplification or contracting made by every design spirit according in the utility model
It is small etc., it is deemed to fall the scope of protection of the utility model.
Claims (10)
- A kind of 1. packaging type super-filter purifying device, it is characterised in that：Including packaging open frame and it is installed on the packaging type machine Milipore filter film group inside frame, water inlet system, water production system, backwashing system, on-line cleaning filter, selecting type adding of agent Device and control system, the milipore filter film group include at least one vertical ultrafiltration membrane pressure container, and the ultrafiltration membrane pressure holds Plummet is disposed with least ten film wires, the water inlet system front end and the original for being arranged at the packaging type Shelf External in device The adjustable connection of water, the water inlet system rear end with it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, it is described Successively connected in the middle part of water inlet system with the selecting type medicament addition device and the on-line cleaning filter, the selecting type Medicament addition device includes at least four pharmacy jars and medicament delivery pipeline, the medicament delivery pipeline respectively with it is described enter water system System connected with the backwashing system adjustable-flow, the water production system front and back end respectively with each vertical ultrafiltration membrane pressure Container connects with the water producing tank positioned at the packaging type Shelf External or with adjustable-flow at water, the backwashing system front end and Middle part respectively with backwash water and it is each the vertical ultrafiltration membrane pressure container flow is adjustable connects, the control system respectively with The milipore filter film group, the water inlet system, the backwashing system, the water production system, the on-line cleaning filter and The selecting type medicament addition device is all connected with.
- A kind of 2. packaging type super-filter purifying device according to claim 1, it is characterised in that：The packaging type machine frame inside The transfer pipeline for surrounding framework is provided with positioned at the milipore filter film group opening position, the top of the transfer pipeline is positioned at described super Opening position on the top of filter membrane film group to lower and bottom, the bottom of the transfer pipeline is located at the bottom of the milipore filter film group Opening position on portion, the transfer pipeline connect with water inlet system and the equal adjustable-flow of backwashing system.
- A kind of 3. packaging type super-filter purifying device according to claim 2, it is characterised in that：The transfer pipeline includes water Flat upper lateral tube and lower transverse tubule below and above and the left vertical tube of left part and right part and right vertical tube are vertically arranged at, it is described Left vertical tube and right vertical tube are respectively perpendicular the left and right end portions for being arranged at the upper lateral tube and the lower transverse tubule, the upper lateral tube or so two End connects with the left vertical tube and right riser upper end respectively, the left and right ends of the lower transverse tubule respectively with the left vertical tube and described The lower end connection of right vertical tube, the upper lateral tube, lower transverse tubule and right vertical tube connect with the water inlet system, the left vertical tube and institute State backwashing system connection, the upper lateral tube and the lower transverse tubule respectively below the vertical ultrafiltration membrane pressure container top and At the top position of bottom.
- A kind of 4. packaging type super-filter purifying device according to claim 2, it is characterised in that：The water inlet system include into Water lines, water inlet interface and the intake pump for adjusting flow, the inlet pipeline front end are filtered by water inlet interface with needing The water connection of purification, the intake pump are arranged on the inlet pipeline, the inlet pipeline interlude and transfer pipeline middle part Connect, be in charge of and the inlet pipeline by enterprising moisture pipe and lower water inlet respectively among the upper and lower part of the transfer pipeline Latter half adjustable-flow connection, the inlet pipeline rear end respectively with each vertical ultrafiltration membrane pressure container flow Adjustable connection, the on-line cleaning filter are arranged between the intake pump and the transfer pipeline, the selecting type Medicament addition device is arranged between the intake pump and the on-line cleaning filter.
- A kind of 5. packaging type super-filter purifying device according to claim 2, it is characterised in that：The backwashing system includes anti- Pipeline, backwash water out and the backwashing pump on backwash pipeline are washed, front end and the backwash water of the backwash pipeline pass through backwash The adjustable connection of pump discharge, the end of the backwash pipeline and each vertical ultrafiltration membrane pressure reservoir, the backwash On pipeline between the backwashing pump and the vertical ultrafiltration membrane pressure container with the selecting type medicament addition device flow Adjustable connection, the latter half of the backwash pipeline connect with the transfer pipeline, and the backwash water out is arranged at described Backwash pipeline latter half end.
- A kind of 6. packaging type super-filter purifying device according to claim 5, it is characterised in that：The backwash pipeline enters institute The common conduit shared with the water production system is provided with before stating vertical ultrafiltration membrane pressure container, the common conduit is arranged at institute State the over top of vertical ultrafiltration membrane pressure container, the common conduit and each vertical equal flow of ultrafiltration membrane pressure container Adjustable connection, the latter half of the backwash pipeline are provided with the common-use tunnel passed through with the water inlet system, and described share is led to Road connects with the transfer pipeline.
- 7. a kind of packaging type super-filter purifying device according to claim 1 to 6 any one claim, its feature exist In：The water production system includes water producing pipe road and production water out, and the water producing pipe road is located at the vertical ultrafiltration membrane pressure container Top, the water producing pipe road connects with each vertical equal adjustable-flow of ultrafiltration membrane pressure container, the production water out It is arranged at the end on the water producing pipe road, the production water out is with water producing tank or with being connected at water.
- 8. a kind of packaging type super-filter purifying device according to claim 1 to 6 any one claim, its feature exist In：The selecting type medicament addition device includes at least four pharmacy jars and the medicament delivery pipeline, at least four medicine The acid medicine and basic agent for strengthening backwash for chemistry, residue at least two are respectively provided with two pharmacy jars in agent tank Pharmacy jar, which takes up, to be respectively provided with for adding in the tiny flocculation agent in raw water and coagulant, each pharmacy jar with the medicine The adjustable connection of piping flow is launched in agent.
- A kind of 9. packaging type super-filter purifying device according to claim 8, it is characterised in that：On each pharmacy jar Compound pump is provided with, the compound pump adjustable-flow is arranged on the medicament delivery pipeline.
- 10. a kind of packaging type super-filter purifying device according to claim 1 to 6 any one claim, its feature exist In：The packaging type machine frame inside is provided with moving air detection means, and the moving air detection means is stood with each described Formula ultrafiltration membrane pressure container connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720889441.0U CN207076349U (en) | 2017-07-20 | 2017-07-20 | A kind of packaging type super-filter purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720889441.0U CN207076349U (en) | 2017-07-20 | 2017-07-20 | A kind of packaging type super-filter purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207076349U true CN207076349U (en) | 2018-03-09 |
Family
ID=61424261
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720889441.0U Active CN207076349U (en) | 2017-07-20 | 2017-07-20 | A kind of packaging type super-filter purifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207076349U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107224877A (en) * | 2017-07-20 | 2017-10-03 | 金科水务工程(北京)有限公司 | A kind of packaging type super-filter purifying device |
| CN111039440A (en) * | 2020-02-17 | 2020-04-21 | 南京壹净新材料科技有限公司 | Bench type multi-water quality water purification system and method |
-
2017
- 2017-07-20 CN CN201720889441.0U patent/CN207076349U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107224877A (en) * | 2017-07-20 | 2017-10-03 | 金科水务工程(北京)有限公司 | A kind of packaging type super-filter purifying device |
| CN107224877B (en) * | 2017-07-20 | 2023-11-03 | 金科环境股份有限公司 | Assembled ultrafiltration water purifying device |
| CN111039440A (en) * | 2020-02-17 | 2020-04-21 | 南京壹净新材料科技有限公司 | Bench type multi-water quality water purification system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US7699977B2 (en) | Assembling unit for filtration and adsorption of waste and sewage water | |
| CN103030237B (en) | Treatment device and treatment method for recycling coal slurry sewage | |
| CN207076349U (en) | A kind of packaging type super-filter purifying device | |
| CN107224877A (en) | A kind of packaging type super-filter purifying device | |
| CN105879441A (en) | Integrated filtering water-purifying system based on modularized separating component | |
| CN109336222A (en) | Immersion gravity stream ceramic membrane microkinetic ultrafiltration system sewage disposal device and method | |
| CN204981422U (en) | Categorised advanced treatment unit of sewage treatment plant | |
| CN108002639A (en) | Integrated form integration ecological water factory | |
| CN106007040B (en) | Heavy metal wastewater treatment system and method | |
| CN210595635U (en) | Drinking water treatment device | |
| CN205088040U (en) | Sewage treatment plant carries mark technological transformation degree of depth filtration system | |
| CN201308815Y (en) | Wastewater ultra-filtration treatment device | |
| CN205933508U (en) | Automatic effluent treatment plant who arranges mud of integration | |
| CN101665295A (en) | Water treatment device, water treatment system and water treatment method thereof | |
| CN111533303B (en) | Surface water quality purification device | |
| CN204661466U (en) | Mark sub-prime advanced treatment system is carried by sewage work | |
| CN206955866U (en) | RO pre-treatment system | |
| CN106630248A (en) | Hardly degradable organic matter adsorption separation method and system thereof | |
| CN209210442U (en) | A kind of immersion gravity stream ceramic membrane microkinetic ultrafiltration system sewage disposal device | |
| KR101469634B1 (en) | Water treatment system use of tubular filter module | |
| CN208802923U (en) | A kind of municipal domestic sewage treatment device | |
| CN207845311U (en) | A kind of cutting wastewater processing system | |
| CN207435103U (en) | A kind of animal protein wastewater membrane filtration system apparatus | |
| CN205398301U (en) | Full -automatic high -efficient water purification system | |
| CN205974027U (en) | Heavy metal waste water treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100102 2, 209-226, block C, Luo wa building, two district, Li Ze, Zhongyuan two, Chaoyang District, Beijing, Wangjing. Patentee after: Jinke environmental Limited by Share Ltd Address before: 100102 2, 209-226, block C, Luo wa building, two district, Li Ze, Zhongyuan two, Chaoyang District, Beijing, Wangjing. Patentee before: GreenTech Water Engineering Co., Ltd. |