Film core pre-pressing structure
Technical field
The present invention relates to the film core pre-pressing structure in filtration, purification field more particularly to the nanofiltration in water treatment field or instead
Permeable membrane core pre-pressing structure.
Background technology
Present applicant develops a kind of membrane filtration module being mainly used for sewage nanofiltration or reverse-osmosis treated, this
Membrane filtration module, including shell, mandrel, film core, first end cover component, second end cover component, film core pre-pressing structure and raw material
Fluid input port and purification fluid outlet, the film core retainer plate is located on mandrel and is made of multiple membrane filter units, by these
The film core of membrane filter unit composition is placed in the first end cover group by film core pre-pressing structure is configured to axial compression state
Between part and second end cover component, the shell is arranged in the outside of film core and is separately connected the first end cover component and second
End-cap assembly;When filtering, material flow is set after the material flow input port flows into through opposite with second end cover component
Film core axial end passes sequentially through that each membrane filter unit is opposite with first end cover component backward and the film mandrel set is to end motion, is already expired
The purification fluid of filter is discharged from the purification fluid outlet.
By applicant application Publication No. CN103657414A, it is entitled " with end disengaging water separating filter film column and its
The patent document (calling bibliography in the following text) of feed liquid processing method " discloses a kind of membrane filtration module, which is exactly logical
Cross what aforesaid way was filtered;In addition, the document is also specifically disclosed that the film core pre-pressing structure of the membrane filtration module, the film
Core pre-pressing structure includes the nut being arranged on mandrel, and the axial pre tightening force applied by the nut on mandrel makes film core in axial
Impaction state and be placed between first end cover component and second end cover component.
Applicant during the long-time service of above-mentioned membrane filtration module to having found, the often film after a period of operation
Filter assemblies just will appear the problem of leakage and filter effect variation.
In order to probe into the reason of this problem occurs, applicant uses operation of a variety of test equipments to membrane filtration module
Work carries out data monitoring, and unrecoverable data found when analysis comparison over time, is arranged in film core pre-pressing structure and exists
Nut on mandrel its pretightning force after membrane filtration module works a period of time will be less than design pretightning force, tighten nut again
Afterwards, membrane filtration module can restore normal operating conditions.
Applicant has found after further testing, the fastening frequency of the nut to being arranged on mandrel need to control 1 time/
200 hours or so, be just avoided that because pretightning force weakens cause membrane filtration module to leak the problem of, and actual industrial give birth to
In production, sewage disposal is often matched using multiple membrane filtration modules with other devices, to improve sewage treating efficiency and reality
Existing automation control, thus causes high to the maintenance cost of multiple membrane filtration modules in actual production, greatly reduces film
The convenience that filter assemblies use.
On the basis of the above, inventor has found after further experiment and research, and above-mentioned nut pretightning force is caused to weaken
Principal element is:It is in axial compression state since membrane filter unit is under the action of film core pre-pressing structure, and filtered
Cheng Zhong, due to the effect of filtration pressure difference, fluid impingement force etc., smaller plastic deformation easily occurs for membrane filter unit, so as to cause
Film core pre-pressing structure is affected to the axial compression of film core, axial compression state when the no longer holding installation of film core,
Leakage, blowby just easily occur for material flow and/or purification fluid in membrane filtration module, to seriously affect membrane filtration module
Sealing effect and filter effect.
Invention content
In view of the above technical problems, the present invention is intended to provide a kind of can preferably ensure film of the film mandrel to impaction state
Filter assemblies and its film core pre-pressing structure and parts peculiar.
The membrane filtration module of the present invention, including shell, mandrel, film core, first end cover component, second end cover component, film core
Pre-pressing structure and material flow input port and purification fluid outlet, the film core retainer plate are located on mandrel and by multiple membrane filtrations
Unit forms, and the film core being made of these membrane filter units is placed in by film core pre-pressing structure is configured to axial compression state
Between the first end cover component and second end cover component, the shell is arranged in the outside of film core and is separately connected described first
End-cap assembly and second end cover component;When filtering, material flow is after the material flow input port flows into, warp and second end cover
The film core axial end that component is opposite and sets passes sequentially through that each membrane filter unit is opposite with first end cover component backward and the film core set
Axial end motion, filtered purification fluid are discharged from the purification fluid outlet;The film core pre-pressing structure has in mistake
The floating type hold-down mechanism moved towards the direction of axial compression film core when filter.
The floating type hold-down mechanism can play each membrane filter unit when film core is filtered the work for fastening of floating
With effectively avoiding film core from leading to film core pre-pressing structure pair due to for a long time by the effect of filtration pressure difference, material flow impact force etc.
Membrane filtration module is greatly reduced to preferably ensure the axial compression state of film core in the case where pretightning force of film core weakens
Frequency of maintenance and lead to the risk factor of seal failure because film mandrel is affected to impaction state, improves membrane filtration module
Ease of use, so that membrane filtration module is kept preferable strainability in a long time, reduce production and safeguard at
This has important economic implications and environmental protection on the basis of not increasing enterprise's excessive cost to entire filtration, purification industry
Meaning.
For the film core pre-pressing structure of above-mentioned membrane filtration module, the film core retainer plate is located on mandrel and by multiple membrane filtration list
Member composition, the film core being made of these membrane filter units are placed in the by the way that film core pre-pressing structure is configured to axial compression state
Between one end-cap assembly and second end cover component;When filtering, material flow passes through film mandrel that is opposite with second end cover component and setting
Pass sequentially through that each membrane filter unit is opposite with first end cover component backward to end and the film mandrel set is to end motion;The film core pre-tightens
Structure has the floating type hold-down mechanism moved towards the direction of axial compression film core in filtering.
Preferably, the floating type hold-down mechanism can be transported with the adaptive direction towards compression film core of the state change of film core
It is dynamic.
Specifically, the floating type hold-down mechanism includes by film mandrel to being pressed in first end cover component and second end cover group
Retention mechanism between part, and between second end cover component and film core and can be driven and court by material flow in filtering
The floating member of the direction movement of axial compression film core.
The floating member on the one hand can be under the premise of retention mechanism applies axial pre tightening force to film core, in filtering
It is driven by material flow and further compresses film core, so that film core is remained preferable axial compression state, and to membrane filtration list
Member generates micro compressive deformation and plays compensating action in an axial direction in filtering, avoids because of film core in filter process because of its film mistake
The case where filtering unit and generate micro compressive deformation in an axial direction, and the pretightning force of retention mechanism is caused to weaken;Described in another aspect
Floating member can also share pressure of the material flow to film core, to mitigate filtration pressure difference, raw material flow to a certain extent
Body impact etc. further decreases the pretightning force impaired risks coefficient of retention mechanism in filtered journey to the active force of film core.
Preferably, the floating member and mandrel linkage is arranged, and floating member energy band moving mandrel is whole towards compressing film core
Direction moves, to ensureing that the axial compression state of film core has better effect.
Optionally, the floating member is vacantly arranged with second end cover component.
Another optional structure is that the floating member is located on second end cover component.
It is useful for making the equally distributed shunting disk of material flow due to setting up in membrane filtration module, and shunting disk is existing
Membrane filtration module in be fixedly connected with second end cover component, therefore in order to simplify structure, reduce the making of membrane filtration module
Cost, it is preferred that the floating member includes the shunting disk being sheathed on mandrel, and the shunting disk is set to film core and second end
It is flexibly connected between cap assemblies and with second end cover component, the same of uniform divided flows is being carried out to material flow using shunting disk in this way
When, so that it may directly utilize the driving force of material flow that shunting disk is driven to move, to compress film core under the action of shunting disk.
When using the structure being vacantly arranged, the entire end face of shunting disk can be contacted with material flow, therefore be conducive to increase
Material flow is to the active area of shunting disk, to increase driving force.
And shunting disk is located at the structure on second end cover component, then is more conducive to and ensures shunting disk relative to mandrel
Radial equilibrium, and the radial equilibrium for the film core being further ensured that on shunting disk, to be more conducive to film core in raw material
Axially loaded is uniform under the action of fluid, and each membrane filter unit of film core is avoided to cause micro inclination to become because of axially loaded unevenness
Shape.
When shunting disk is located on second end cover component, it to be used for the preferred structure of shunting disk of above-mentioned membrane filtration module
It is, including disk body that the side of the disk body is equipped with fluid inlet orifice, and the axial end face of disk body is equipped with Fluid-exiting apertures, the fluid
Connect into hole and Fluid-exiting apertures to be formed side into fluid split channel.In use, material flow enters shunting through fluid inlet orifice
It is arranged from Fluid-exiting apertures to film core behind channel.Side into fluid split channel, can utilize material flow to fluid inlet orifice above
The active force of disk body wall pushes disk body band moving mandrel axially movable, and further compresses film core.
Further, the Fluid-exiting apertures are along the axially extending formation outlet fluid of disk body, the fluid inlet orifice edge
Disk body extends radially to be formed fluid inlet channel, the fluid inlet channel and fluid output at the outlet fluid
Channel connects to form the L-shaped split channel in cross section.Such structure fabrication is convenient, and the shunting that cross section is L-shaped
Channel can also play material flow certain cushioning effect, to be conducive to reduce material flow to a certain extent to film
The pressure of core.
Preferably, for more convenient processing, the fluid inlet channel is axially through the disk opposite with Fluid-exiting apertures
Body axial end is arranged notch in the edge part of disk body end face opposite with Fluid-exiting apertures and setting, utilizes the notch and second end
Gap between cap assemblies can be used as the fluid inlet channel.
Further, the outlet fluid includes the different epimere output channel of inner diameter size and connects on described
The hypomere output channel of section output channel and fluid inlet channel.When the internal diameter of epimere output channel is less than hypomere output channel
When internal diameter, to a certain extent, be conducive to increase material flow to the active area of disk body wall to play preferably driving work
With.
Preferably, the internal diameter of the epimere output channel is more than the internal diameter of hypomere output channel.In this way when fluid is from fluid
When input channel enters epimere output channel through hypomere output channel, the speed of fluid will reduce, and the relative pressure of fluid will
It increased, advantageously ensure that film core has higher filter efficiency.
Preferably, the fluid inlet orifice is domed, simple in structure, easy to make.
Preferably, the fluid inlet orifice and Fluid-exiting apertures are uniformly distributed along the circumferential direction of disk body.Such structure can guarantee raw material flow
Body is also uniformly distributed after entering film core, to be conducive to improve film core in membrane filter unit overall utilization rate and ensure film core by
Power is uniform.
Preferably, the shunting disk is equipped with the centre bore for being socketed with mandrel, and the fluid inlet orifice and Fluid-exiting apertures are inclined
It is arranged from the centre bore.
Preferably, the shunting disk is fixedly connected with mandrel, for example, shunting disk and mandrel can be connected through a screw thread it is fixed or
It is fixed using modes such as splicing.
Preferably, the connection structure of above-mentioned shunting disk and mandrel, including shunting disk and mandrel, the shunting disk and mandrel it
Between be formed with welded gaps and/or welding groove, shunting disk and mandrel are welded at the welded gaps and/or welding groove
It is integrated.Using the structure being welded to connect, the fixation between shunting disk and mandrel can be made more secured, be more advantageous to shunting disk
Lower band moving mandrel is driven to be moved towards the direction of axial compression film core in material flow, to preferably ensure the axial compression of film core
State.
Specifically, the shunting disk axial direction at least one end of the centre bore and mandrel formed the welded gaps and/
Or welding groove.
Further, the mandrel be equipped with ladder shaft part, the centre bore be equipped with the ladder shaft part corresponding matching with
The stage portion of axially position is formed to mandrel, shunting disk forms welded gaps, shunting disk in the big end of the stage portion with mandrel
In the small end of the stage portion welding groove is formed with mandrel.The outside diameter of the stage portion is more than the diameter of axle of ladder shaft part,
It can play the role of axially position in this way and form the welded gaps, convenient for welding.In practical application, shunting disk and core
Axis full weld at the welded gaps and welding groove, and weld seam must not be higher than base material.
For the welding tooling of the shunting disk and mandrel, including fixed part, the fixed part includes supporting rack;Limit
Portion, the limiting section include the first limit base that can coordinate with mandrel and be correspondingly arranged with first limit base and can with point
Second limit base of flow table cooperation, first limit base and the second limit base connect respectively with support frame as described above after described the
The operating space being welded to connect for shunting disk and mandrel is formed between one limit base, the second limit base and supporting rack.The welding
Tool structure is simple, can more accurately control the concentricity of shunting disk and mandrel, and ensure to weld easy to operate.
To be further simplified structure, and make easier for installation, first limit base and second of mandrel and shunting disk
Limit base is separately positioned on the axial both ends of supporting rack.
Preferably, second limit base includes the second mounting plate, and second mounting plate is equipped with can be to the shunting disk
Carry out the limiting slot of axially position;First limit base includes the first mounting plate and the limit shaft that can coordinate with the mandrel
Set, first mounting plate is equipped in an axial direction can carry out limit shaft sleeve axially position and can make the mandrel coordinated with limit shaft sleeve
The stepped hole of shunting disk is connected after passing through.In actual installation, it need to only ensure the concentricity and ruler of the stepped hole and limiting slot
Very little and limit shaft sleeve precision is that can guarantee shunting disk and the concentricity after mandrel installation.Pass through limit shaft sleeve and limiting slot
Respectively to the constraint of mandrel and shunting disk, it can ensure that the precision after shunting disk is welded with mandrel is higher.
Preferably, second mounting plate is equipped with corresponding with the stepped hole and is at least used as the operating space in an axial direction
A part through-hole.Opening up for the through-hole can to the greatest extent may be used on the basis of the axially position for not influencing limiting slot to shunting disk
It can guarantee and be relatively large in diameter, in order to weld operation.
Preferably, support frame as described above includes the more supporting bars being connected between the first limit base and the second limit base,
To ensure the stabilized structure of entire welding tooling.In addition, support frame as described above can also use engraved structure, need to only it meet structure
On the basis of firm, ensure that there are the operating spaces convenient for welding.
Shunting disk and mandrel are welded and fixed using above-mentioned welding tooling, can greatly improve the structure of shunting disk and mandrel
Stability avoids generating centainly during using flexible connection and shunting disk is caused to compress film core under material flow driving
Shake or tilt etc..Vertical or horizontal mode can be used in practical application and put for the welding tooling, when using vertical
When storing, preferably it is placed on workbench.
Optionally, the floating member further includes elastic compensation element.The elastic compensation element can provide balancing force,
Avoid causing retention mechanism there is a situation where loosening because of filtering, and due to filtering when material flow pressure often be in wave
Dynamic state, therefore elastic compensation element can also play the role of bumper and absorbing shock.
The elastic compensation element can be existing butterfly spring or waveform spring.
Further, the floating type hold-down mechanism, which is additionally provided with, to be moved towards the direction of axial compression film core in floating member
When, the piston element of sliding connection is kept with mandrel or second end cover component;When the piston element and second end cover group
When part keeps sliding connection, piston element is arranged with floating member and/or mandrel linkage.The piston element can play
Sealing function.
Further, the piston element keeps sliding contact frictional fit with mandrel or second end cover component.
When film core pre-pressing structure has elastic compensation element, elastic compensation element is preferably set to piston element and second
Between end-cap assembly.
Preferably, the piston element includes the piston head that sliding connection is kept with mandrel or second end cover component,
And the piston rod being connect with the piston head, the piston head are equipped with the groove coordinated with the mandrel.Such structure is also
It can be very easily to the positioning of mandrel.The groove is preferably connected through a screw thread fixation with mandrel.
When the elastic compensation element is waveform spring, the waveform spring can be sheathed on the piston rod, when
When film core pre-pressing structure is not provided with elastic compensation element, can make the piston rod pass through second end cover component after with screw threads for fastening knot
Structure is fixedly connected, which is locking nut.
Optionally, the retention mechanism includes the more pull rods being connected between first end cover component and second end cover component
Component, and the screw threads for fastening structure of the mandrel mating connection with the rod assembly and across first end cover component respectively.It is logical
It crosses and the first end cover component is set and second end cover component can realize fixation to shell and film core, while passing through pull rod again
More pull rods in component and screw threads for fastening structure, you can ensure shell, film core, first end cover component and second end cover component
Between connectivity robustness.
Although entire membrane filtration module can be made to have with the retention mechanism that screw threads for fastening structure is combined using rod assembly
Good fastness, but in actual use, since sewage disposal is often using multiple membrane filtration modules and other dresses
It sets and matches, to improve sewage treating efficiency and realize automation control, therefore just need more pull rods in application, and more
Pull rod is made of stainless steel, of high cost, and fastness is not so good as carbon steel, is made of carbon steel and is easily corroded again, and it is distributed in
The surrounding of entire membrane filtration module, makes the space occupied needed for entire membrane filtration module greatly increase, and gives the peace of membrane filtration module
Dress brings many inconvenience.
Therefore, in practical applications, another optional structure is the first end cover component and second end cover component quilt
Sealing compresses inside the housing.The first end cover component and second end cover component are by being arranged in film core, first end cover component
Sealing is compressed with the shell of second end cover component external.The retention mechanism of its film core pre-pressing structure preferably includes screw threads for fastening
The end of structure, mandrel axial direction one end connects the screw threads for fastening structure after first end cover component, and the axial direction of mandrel is another
End is slidably and sealingly connected with the holding of second end cover component.Use the membrane filtration module of this structure for non pull rod type structure, this nothing
Drawbar structure can refer to applicant's application, and Publication No. CN104128094A, entitled " one kind was detached with end Inlet and outlet water
The specific connection structure of shell and first end cover component and second end cover component in the patent document of filter membrane column ".The shell can
With the inner cavity adaptable with first end cover component and second end cover component, first end cover component and second end cover component are clamped
In enclosure, and cavity is formed between wall and film core inside the shell.The inner wall of the shell and first end cover component and the
It can be sealed compression by wedge, sealing structure or other existing similar structures between the lateral wall of two end-cap assemblies.
In practical applications, envelope core pre-pressing structure axial compression is between first end cover component and second end cover component
A variety of existing structures can be used in membrane filter unit;Preferably, the film core is by multiple films being axially sequentially stacked along mandrel
Filter element form, such structure not only install it is easy to make, but also when each membrane filter unit envelope core pre-pressing structure along axis
To after compression, film core can be axially formed multiple filtering runners, to obtain better filter effect, and in film core size one
Under the premise of fixed, the quantity for increasing membrane filter unit is also helped, accordingly increases filter area, improves filter efficiency, and make
Filter effect is more preferable.
Preferably, the membrane filter unit includes the flow guiding disc and diaphragm that several Zhang Yici are socketed on mandrel, every adjacent
Two flow guiding discs between a diaphragm is installed;Each flow guiding disc includes flow guiding disc ontology and is used on the flow guiding disc ontology
In the first centre bore coordinated with mandrel, and deviate the first flow-guiding channel of first centre bore, each flow guiding disc ontology
The annular diversion cavity for accommodating corresponding diaphragm is additionally provided on side, each annular diversion cavity is connected with corresponding first flow-guiding channel;Respectively
Diaphragm include diaphragm ontology and on the diaphragm ontology for the second centre bore for coordinating with mandrel, and deviate this second
Second flow-guiding channel of centre bore;Each diaphragm ontology includes upper diaphragm, lower diaphragm and the sky between upper diaphragm and lower diaphragm
Chamber, the cavity are connected with the second centre bore;It is respectively equipped between each upper diaphragm and the inner edge of corresponding annular diversion cavity close
Seal structure is respectively equipped with sealing structure between each lower diaphragm and the inner edge of corresponding annular diversion cavity;The mandrel is equipped with
The flow-guiding structure be connected respectively with the second centre bore of each diaphragm, cavity and second center of the flow-guiding structure with each diaphragm
Hole constitutes the purification fluid conveying flow path be connected with purification fluid outlet;First flow-guiding channel of each flow guiding disc and each diaphragm
Second flow-guiding channel, which is sequentially communicated, constitutes material flow conveying flow path.
Further, if setting projected area of individual diaphragm on the cross section of mandrel as A square metres, individual diaphragm it is outer
Diameter is D meters, and the diaphragm quantity in the membrane filtration module is N, then:
Wherein, 250≤B≤320.
Wherein projected area of the diaphragm on the cross section of mandrel is A square metres, and projected area here is in this membrane filtration
In component include the second centre bore and make material flow pass through diaphragm the second flow-guiding channel cross-sectional area, it is found by the applicant that
Ratio between the projected area and the number product and the area of a circle constituted with diaphragm outer diameter of diaphragm is between 250 to 320
When, compared to conventional membrane filtration module, the filter efficiency and filtering rejection of the application membrane filtration module significantly improve, and generate
The unexpected effect of those skilled in the art.Floating type to the progress of each membrane filter unit using floating type hold-down mechanism
On the basis of fastening, by the selection and combination of several key parameters to diaphragm, it is more advantageous to and ensures film core in filter process
In always be in axial compression state under the premise of, filter area can be significantly increased so that membrane filtration module filtering effect
Rate higher and filtering rejection it is unexpected good.
Further, whenWherein, when 250≤B≤320, the outer diameter of each diaphragm is 0.2 to 0.4 meter;Film
Diaphragm quantity in filter assemblies is 125 to 180, is preferably selected for one kind.
The first end cover component includes first flange disk and the first sealing plate, and the second end cover component includes the second method
Blue disk and the second sealing plate;The film core is held between first sealing plate and the second sealing plate, the first sealing plate quilt
It is held between film core and first flange disk, the second sealing plate is held between film core and second flange disk, and shell is fixed on
Between first flange disk and second flange disk, the mandrel is at least tightly connected with the first sealing plate;On the first flange disk
It is additionally provided with the material flow delivery outlet be connected with material flow conveying flow path, the material flow delivery outlet, material flow
Input port and purification fluid outlet are arranged on first flange disk around the periphery of mandrel, and the first sealing plate is equipped with connection institute
State purification fluid conveying flow path and purify the apocenosis passage of fluid outlet, be equipped in the shell by material flow delivery outlet with
Material flow conveys the first passage of the output end conducting of flow path and material flow input port and material flow is conveyed flow path
Input terminal conducting second channel.
The apocenosis passage angle with horizontal plane is preferably in 5 °~60 °, and such structure can make drain effect more preferable.
The Publication No. applied by applicant had both can be used in the output that fluid is purified in above-mentioned each membrane filtration module
Disclosed in CN103657414A, entitled " same to hold disengaging water separating filter film column and its feed liquid processing method " patent document
The drainage structure for using hollow core shaft, can also be used applicant application application No. is 201610226549.1, entitled " films
That is mentioned in the application for a patent for invention of filter assemblies " uses the drainage structure of solid mandrel.
If the mandrel is solid shafting, between each first centre bore and the second centre bore are equipped with mandrel matching part respectively
Gap, the gap may be configured as 0.5 to 2 millimeter, which can be used as the flow-guiding structure.
Further, the lobe around the first centre bore circumferential array, phase are provided in the first centre bore of each flow guiding disc
There are gaps, the outside circle of the lobe to be engaged with the mandrel between adjacent lobe, and the gap is then used as the first center
The gap in hole and mandrel matching part.
Further, the width in the gap between the adjacent lobe is 1~3 millimeter.
Lobe is arranged not only can carry out radial positioning by mandrel to film core, but also can allow purification fluid that can smoothly pass over
First centre bore, the lobe can be the plate profile structures for having rectified action.
After the material flow is inputted from material flow input port, material flow is flowed to by second channel and conveys flow path,
For material flow in the material flow conveys flow path transmission process, material flow can enter institute after the split channel of shunting disk
It states in annular diversion cavity, is flowed between flow guiding disc and diaphragm, diaphragm is allowed to carry out abundant filtration treatment to material flow.By place
Material flow (or being dope) after reason enters first passage, and enter material flow delivery outlet along the channel flows out film mistake later
Filter component.
Material flow is after diaphragm is handled, and the purification fluid generated in the cavity on diaphragm ontology is along the cavity and institute
Membrane filtration group is discharged by purifying fluid outlet after apocenosis passage in the purification fluid conveying flow path for stating the second centre bore composition
Part.Because each annular diversion cavity is connected with corresponding first flow-guiding channel, the material flow convey flow path be on flow guiding disc
Annular diversion cavity connection.It is respectively equipped with sealing structure between each upper diaphragm and the inner edge of corresponding annular diversion cavity,
It is respectively equipped with sealing structure between each lower diaphragm and the inner edge of corresponding annular diversion cavity, is to prevent material flow to the
One centre bore and the flowing of the second centre bore direction, sealing structure here can be sealing ring.
Can crack mouth on the flow guiding disc, and diaphragm is equipped with the breach being adapted to the sealing, and the sealing and breach are equal
First flow-guiding channel is formed, can realize above-mentioned material flow conveying flow path, certainly, the material flow transport Stream in this way
Road is connected to the annular diversion cavity on flow guiding disc.
The sealing and breach are opened in the water conservancy diversion panel surface or annular diversion cavity top surface or annular diversion cavity bottom surface, is stitched
Mouthful and breach at turn up, tilt to flow guiding disc two sides respectively, slope surface is formed, in this way since membrane filter unit includes several along core
The axial direction of axis is socketed in flow guiding disc and diaphragm on mandrel successively, therefore material flow can helically be transported along material flow conveying flow path
It is dynamic, to carry out abundant filtration treatment using each diaphragm, to reach good filter effect.
If the mandrel is hollow shaft, i.e., the described mandrel is in hollow tubular, then being equipped on the tube wall of the mandrel will be each
The through-hole that second centre bore of diaphragm is connected with mandrel inner cavity, at this point, the through-hole is then used as the flow-guiding structure, the pipe of mandrel
Chamber is as apocenosis passage, and the shaft end opening of mandrel is as purification fluid outlet, without being sealed in first flange disk and first
The purification fluid outlet and apocenosis passage are respectively set on plate.Axial one end of the hollow tubular mandrel can be arranged to
Enclosed construction is welded to connect with plug.Material flow generates after diaphragm is handled in the cavity on diaphragm ontology
The purification fluid conveying flow path that fluid is constituted along the through-hole of the cavity and second centre bore and mandrel is purified, through mandrel
Tube chamber after pass through the shaft end of mandrel opening discharge membrane filtration module.
Further, each diaphragm is RO films or NF films.
RO is the abbreviation of English Reverse Osmosis membrane, and Chinese means reverse osmosis.The flowing of general water
Mode is to flow to high concentration by low concentration, will be from high concentration flow to low concentration after water is once pressurize, that is, so-called reverse osmosis is former
Reason:Since the aperture of RO films is 5/1000000ths (0.0001 microns) of hairline, general naked eyes can not be seen, bacterium, disease
Poison is its 5000 times, and therefore, only hydrone and part can pass through beneficial to the mineral ion of human body, other impurity and a huge sum of money
Category is discharged by waste pipe.The process and spaceman's waste water recycling device of all sea water desalinations are all made of the method, therefore RO
Film is also known as external high-tech " artificial kidney ".At present both at home and abroad, the military civil field of medicine all takes top RO films to carry out high
Molecular filtration.
NF films are NF membrane, and nanofiltration is a kind of pressure-driven membrane separating process between reverse osmosis between ultrafiltration, is received
The pore diameter range of filter membrane is in several rans.Compared with other pressure-driven membrane separating process, occur later.NF membrane is big
Mostly from reverse osmosis membrane derivation, such as CA, CTA film, aromatic polyamide composite membrane and sulfonated polyether sulfone film.
Preferably, the first end cover component is located at mandrel upper end, and second end cover component is located at the lower end of mandrel.
It should be noted that the purification fluid outlet and apocenosis passage can also be arranged where second end cover component
End;The material flow input port and material flow delivery outlet can also be arranged at end where second end cover component.
Further, the retention mechanism further includes the screw threads for fastening structure set on second flange disk lower end.
Further, the screw threads for fastening structure with mandrel cooperation preferably includes the first preload piece and nut, and described the
One preload piece lower face contacts compression with the upper surface of the first sealing plate across first flange disk, first preload piece upper end to
On across first flange disk and with nut coordinate, first preload piece upper end preferably use double nut to push up tighten with reach into
The locking purpose of one step;The screw threads for fastening structure of second flange disk lower end includes the second preload piece and nut, and described second pre-tightens
Part is integrally provided in the lower section of second flange disk, and the upper surface of the second preload piece contacts compression with the lower face of second flange disk,
Pass through screw lock between second preload piece and second flange disk.With rod assembly cooperation screw threads for fastening structure be preferably
Nut.
The second flange disk can be fixed with the second sealing plate by screw threads for fastening structure, which is preferably
Screw.
First preload piece is preferably multidiameter structure, which contacts with the first sealing plate, described
Second preload piece is preferably disc structure.Wherein, it is pre- to be preferably greater than first for the contact area of the second preload piece and second flange disk
The contact area of tight part and the first sealing plate, the spiral shell of screw threads for fastening structure and second flange disk lower end on such first sealing plate
The pressure that line fastening structure generates, along concentrating, is conducive to provide better pretightning force to film core, and due to described to mandrel week
Sealing structure is set between each upper diaphragm and the inner edge of corresponding annular diversion cavity, thus such structure can also make upper diaphragm,
Sealing performance between lower diaphragm and the inner edge of corresponding annular diversion cavity is more preferable.
Specific implementation mode with reference to embodiments is described in further detail the above of the present invention again.
But the range that this should not be interpreted as to the above-mentioned theme of the present invention is only limitted to example below.Think not departing from the above-mentioned technology of the present invention
In the case of thinking, the various replacements or change made according to ordinary skill knowledge and customary means should all be included in this hair
In bright range.
Description of the drawings
Fig. 1 is the first structural representation of the membrane filtration module with film core pre-pressing structure in the specific embodiment of the invention
Figure.
Fig. 2 is second of structural representation of the membrane filtration module with film core pre-pressing structure in the specific embodiment of the invention
Figure.
Fig. 3 is the third structural representation of the membrane filtration module with film core pre-pressing structure in the specific embodiment of the invention
Figure.
Fig. 4 is the 4th kind of structural representation of the membrane filtration module with film core pre-pressing structure in the specific embodiment of the invention
Figure.
Fig. 5 is the 5th kind of structural representation of the membrane filtration module with film core pre-pressing structure in the specific embodiment of the invention
Figure.
Fig. 6 is the schematic top plan view of shunting disk in Fig. 1 and Fig. 4.
Fig. 7 is the schematic front view of shunting disk in Fig. 2, Fig. 3 and Fig. 5.
Fig. 8 is the elevational schematic view of shunting disk in Fig. 2, Fig. 3 and Fig. 5.
Fig. 9 is the structural representation for the welding tooling of shunting disk in Fig. 1~Fig. 5 and mandrel under a kind of use state
Figure.
Figure 10 is the structural schematic diagram of the second limit base in Fig. 9.
Figure 11 is the structural schematic diagram of piston element in Fig. 1 and Fig. 2.
Figure 12 is the structural schematic diagram of piston element in Fig. 3.
Figure 13 is the schematic top plan view of first end cover component in Fig. 1~Fig. 5.
Figure 14 is the A-A of first end cover component in Figure 13 to schematic cross-sectional view.
Figure 15 is the film core decomposition diagram of two flow guiding discs and diaphragm composition in Fig. 1~Fig. 5.
Figure 16 is the schematic cross-sectional view of the film core of two flow guiding discs and diaphragm composition in Fig. 1~Fig. 5.
Specific implementation mode
Embodiment 1:
As shown in Fig. 1, Fig. 6, Fig. 9~Figure 11, Figure 13~Figure 16, membrane filtration module, including shell 100, mandrel 200, film
Core 300, first end cover component 410, second end cover component 420, film core pre-pressing structure and material flow input port 510 and purification
Fluid outlet 520, the film core 300 is set on mandrel 200 and is made of multiple membrane filter units, by these membrane filtration lists
The film core 300 of member composition is placed in the first end cover component 410 by film core pre-pressing structure is configured to axial compression state
Between second end cover component 420, the shell 100 is arranged in the outside of film core 300 and is separately connected the first end cover group
Part 410 and second end cover component 420;When filtering, material flow is after the material flow input port 510 flows into, through with second
300 axial end of film core that end-cap assembly 420 is opposite and sets pass sequentially through each membrane filter unit backward with 410 phase of first end cover component
Pair and the axial end motion of film core 300 set, filtered purification fluid are discharged from the purification fluid outlet 520;The film
Core pre-pressing structure has the floating type hold-down mechanism moved towards the direction of axial compression film core 300 in filtering.
The floating type hold-down mechanism includes by 300 axial compression of film core in first end cover component 410 and second end cover group
Retention mechanism between part 420, and set between second end cover component 420 and film core 300 and can filter when by raw material flow
Body drive and towards the direction of axial compression film core 300 move floating member.
The floating member on the one hand can be under the premise of retention mechanism applies axial pre tightening force to film core 300, in mistake
It is driven by material flow when filter and further compresses film core 300, film core 300 is made to remain preferable axial compression state, and
Micro compressive deformation is generated in an axial direction in filtering to membrane filter unit and plays compensating action, avoids filtering because of film core 300
In the process because its membrane filter unit generates micro compressive deformation in an axial direction, and the feelings for causing the pretightning force of retention mechanism to weaken
Condition;On the other hand the floating member can also share pressure of the material flow to film core 300, to subtract to a certain extent
Light filtration pressure difference, material flow impact etc. further decrease the preload of retention mechanism in filtered journey to the active force of film core 300
Power impaired risks coefficient.
The floating member includes the shunting disk 610 being sheathed on mandrel 200.
The film core 300 is set on mandrel 200 and by multiple membrane filter unit group being axially sequentially stacked along mandrel 200
At;The membrane filter unit includes the flow guiding disc 310 and diaphragm 320 that several Zhang Yici are socketed on mandrel 200, every adjacent two
A diaphragm 320 is installed between flow guiding disc 310;Each flow guiding disc 310 is including flow guiding disc ontology and is set to the flow guiding disc sheet
The first centre bore 311 on body for coordinating with mandrel 200, and deviate the first flow-guiding channel of first centre bore 311
312, the annular diversion cavity 313 for accommodating corresponding diaphragm 320, each annular diversion cavity 313 are additionally provided on the side of each flow guiding disc ontology
It is connected with corresponding first flow-guiding channel 312;Each diaphragm 320 includes diaphragm ontology and is used on the diaphragm ontology and core
The second centre bore 321 that axis 200 coordinates, and deviate the second flow-guiding channel 322 of second centre bore 321;Each diaphragm ontology
Including upper diaphragm 323, lower diaphragm 324 and the cavity 325 between upper diaphragm 323 and lower diaphragm 324, the cavity 325 with
Second centre bore 321 is connected;It is respectively equipped with sealing between each upper diaphragm 323 and the inner edge 314 of corresponding annular diversion cavity 313
Structure 330 is respectively equipped with sealing structure 330 between each lower diaphragm 324 and the inner edge 314 of corresponding annular diversion cavity 313;Institute
It states mandrel 200 and is equipped with the flow-guiding structure 201 be connected respectively with the second centre bore 321 of each diaphragm 320, the flow-guiding structure
201 constitute the purification fluid be connected with purification fluid outlet 520 with the cavity 325 of each diaphragm 320 and the second centre bore 321
Convey flow path 521;First flow-guiding channel 312 of each flow guiding disc 310 is sequentially communicated with the second flow-guiding channel 322 of each diaphragm 320
It constitutes material flow and conveys flow path 511;The shunting disk 610, which is equipped with, is connected to the material flow input port 510 and material flow
Convey the split channel of flow path 511.
If setting individual projected area of diaphragm 320 on the cross section of mandrel 200 as A square metres, outside individual diaphragm 320
Diameter is D meters, and 320 quantity of diaphragm in the membrane filtration module is N, then:
Wherein, 250≤B≤320.
Wherein projected area of the diaphragm 320 on the cross section of mandrel 200 is A square metres, and projected area here is at this
In membrane filtration module include the second centre bore 321 with make material flow pass through diaphragm 320 the second flow-guiding channel 322 it is transversal
Area, it is found by the applicant that between the projected area and the number product and the area of a circle constituted with 320 outer diameter of diaphragm of diaphragm 320
Ratio when between 250 to 320, compared to conventional membrane filtration module, the filter efficiency of the application membrane filtration module and filtering
Rejection significantly improves, and produces the unexpected effect of those skilled in the art.Utilizing floating type hold-down mechanism pair
On the basis of each membrane filter unit carries out floating type fastening, by the selection and combination of several key parameters to diaphragm 320, more
Under the premise of advantageously ensuring that film core 300 is in axial compression state always in filter process, filter area can be significantly increased,
So that the filter efficiency higher and filtering rejection of membrane filtration module are unexpected good.
In the present embodiment, the whole cylindrical structure of the film core 300, so flow guiding disc 310 here can be disc
Structure, 320 preferred shape of the diaphragm should be also adapted with the shape of the flow guiding disc 310, the disc knot of the flow guiding disc 310
Structure can be edge extends protrusion to both sides, makes the section of the flow guiding disc 310 in I-shaped, so the just shape on flow guiding disc 310
At above-mentioned annular diversion cavity 313.
The membrane filtration module of the present embodiment includes that several axial directions along mandrel 200 are socketed in leading on mandrel 200 successively
The number of flow table 310 and diaphragm 320, flow guiding disc 310 here can be 148 or more, and the number of diaphragm 320 can be 147
More than a, 320 outer diameter of the diaphragm is 0.2 to 0.4 meter.The upper diaphragm 323 and lower diaphragm 324 are RO films or NF films.
The first end cover component 410 includes first flange disk 411 and the first sealing plate 412, the second end cover component
420 include second flange disk 421 and the second sealing plate 422;The film core 300 is held in first sealing plate 412 and
Between two sealing plates 422, the first sealing plate 412 is held between film core 300 and first flange disk 411, the second sealing plate 422
It is held between film core 300 and second flange disk 421, shell 100 is fixed on first flange disk 411 and second flange disk 421
Between, the mandrel 200 and the first sealing plate 412 are tightly connected;It is additionally provided on the first flange disk 411 and the raw material flow
Body conveys the material flow delivery outlet 530 that flow path 511 is connected, the material flow delivery outlet 530, material flow input port 510
It is arranged around the periphery of mandrel 200 on first flange disk 411 with purification fluid outlet 520, the first sealing plate 412 is equipped with
It is connected to the apocenosis passage 522 of the purification fluid conveying flow path 521 and purification fluid outlet 520.The apocenosis passage 522 with
Horizontal plane angle is in 20 °~40 °.
It is equipped in the shell 100 and material flow delivery outlet 530 is connected with the output end of material flow conveying flow path 511
First passage and material flow input port 510 and material flow are conveyed to the second channel that the input terminal of flow path 511 is connected.
Mandrel 200 described in the present embodiment is solid shafting, the first centre bore 311 and the second centre bore 321 respectively with mandrel
200 matching parts are equipped with gap, which may be configured as 1 to 1.5 millimeter, which can be used as the flow-guiding structure 201.It is described
First end cover component 410 or second end cover component 420 are equipped with cloth recirculation hole, the outlet of the cloth recirculation hole and the second channel
End connection (concrete structure here can refer to the structure in CN103657414A), also by material flow convey flow path 511 with
First passage is connected to, and after setting mandrel 200 to solid circular shafts, can bring higher pressure resistance to entire membrane filtration module
Property, in this way relative to hollow shaft member, can increase on the basis of not changing, even expanding the effective filtration area of film core 300
The number of blooming filter element improves the filtering efficiency of the membrane filtration module.
The lobe 315 around 311 circumferential array of the first centre bore is provided in first centre bore 311 of each flow guiding disc 310,
There are gaps, the outside circle of the lobe 315 to be engaged with the mandrel 200 between adjacent lobe 315, and the gap is then made
For the gap of the first centre bore 311 and 200 matching part of mandrel.The width in the gap between the adjacent lobe 315 be 1.5~
2.5 millimeter.The lobe 315 is the plate profile structure for having rectified action.The shunting disk 610 is vacantly set with the second sealing plate 422
It sets.
The shunting disk 610 is equipped with the centre bore 615 for being socketed with mandrel 200, during the split channel deviation is described
Heart hole 615 is simultaneously evenly distributed, and the Fluid-exiting apertures 612 of the split channel are axially through setting.
The connection structure of above-mentioned shunting disk 610 and mandrel 200, including shunting disk 610 and mandrel 200, the shunting disk 610
It is formed with welded gaps and/or welding groove between mandrel 200, flow table is punished in the welded gaps and/or welding groove
610 are welded as a whole with mandrel 200.The mandrel 200 is equipped with ladder shaft part, and the centre bore 615 is equipped with and the multi-diameter shaft
Section corresponding matching is to form mandrel 200 stage portion of axially position, big end and mandrel of the shunting disk 610 in the stage portion
200 form welded gaps, and shunting disk 610 forms welding groove in the small end of the stage portion with mandrel 200.
For the welding tooling of above-mentioned shunting disk 610 and mandrel 200, including fixed part, the fixed part includes supporting rack
710;Limiting section, the limiting section include the first limit base 720 that can coordinate with mandrel 200 and with first limit base
720 the second limit bases 730 that is correspondingly arranged and can coordinate with shunting disk 610, first limit base, 720 and second limit base
730 connect respectively with support frame as described above 710 after between first limit base 720, the second limit base 730 and supporting rack 710
Form the operating space being welded to connect for shunting disk 610 and mandrel 200.
First limit base, 720 and second limit base 730 is separately positioned on the axial both ends of supporting rack 710.Described
Two limit bases 730 include the second mounting plate 731, and second mounting plate 731, which is equipped with, can carry out the shunting disk 610 axially to determine
The limiting slot 732 of position;First limit base 720 includes the first mounting plate 721 and can be with the limit shaft of the cooperation of the mandrel 200
Set 722, first mounting plate 721 is equipped in an axial direction can carry out limit shaft sleeve 722 axially position and can make and limit shaft sleeve
The mandrel 200 of 722 cooperations connects the stepped hole 723 of shunting disk 610 after passing through.
Second mounting plate 731 is equipped with corresponding with the stepped hole 723 and is at least used as the operating space in an axial direction
A part through-hole 733.Support frame as described above 710 is connected to including more between the first limit base 720 and the second limit base 730
Supporting bar.It can be used between the supporting bar and the first mounting plate 721 and the second mounting plate 731 and be threadedly coupled fastening.
The concentricity of shunting disk 610 and mandrel 200 can more accurately be controlled using above-mentioned welding tooling, and ensure welding operation
Convenient, the structural stability after shunting disk 610 is welded with mandrel 200 is good, can effectively avoid causing to shunt using flexible connection
Disk 610 generates certain shaking or inclination etc. during compressing film core 200 under material flow driving.
The floating type hold-down mechanism, which is additionally provided with, to be compressed axially direction along film core 300 with moving mandrel 200 in shunting disk 610
When movement, the piston element 800 of sliding connection is kept with the second sealing plate 422, the piston element 800 includes and second
Sealing plate 422 keeps the piston head 810 of sliding connection, and the piston rod 820 being connect with the piston head 810, described
Piston head 810 is equipped with the groove 811 that cooperation is connected through a screw thread with the mandrel 200.The floating member further includes being set to institute
The elastic compensation element 900 between piston element 800 and second flange disk 421 is stated, the elastic compensation element 900 is waveform bullet
Spring, the waveform spring are sheathed on the piston rod 820.The retention mechanism includes more and is connected to first flange disk 411
Rod assembly 620 between second flange disk 421, and respectively with the rod assembly 620 and across the first sealing plate 412
Mandrel 200 be connected screw threads for fastening structure.The retention mechanism further includes being set to 421 lower end of second flange disk
Screw threads for fastening structure.
Include the first preload piece 631 and nut, second flange disk 421 with the screw threads for fastening structure that the mandrel 200 coordinates
The screw threads for fastening structure of lower end includes the second preload piece 632 and nut;First preload piece, 631 lower face passes through first flange
Disk 411 contacts compression with the upper surface of the first sealing plate 422, and 631 upper end of the first preload piece is upward through first flange disk
411 and coordinate with nut, 631 upper end of the first preload piece use double nut to tighten top to reach further locking mesh
's;Second preload piece 632 is integrally provided in the lower section of second flange disk 421, the upper surface and second of the second preload piece 632
The lower face contact of ring flange 421 compresses, and passes through screw lock between second preload piece 632 and second flange disk 421.With
The screw threads for fastening structure that rod assembly 620 coordinates is nut.421 and second sealing plate 422 of the second flange disk can pass through spiral shell
Line fastening structure is fixed, which is screw.
First preload piece 631 is multidiameter structure, which contacts with the first sealing plate 412, institute
It is disc structure to state the second preload piece 632.Wherein, the contact area of the second preload piece 632 and second flange disk 421 is more than first
The contact area of preload piece 631 and the first sealing plate 412, the screw threads for fastening structure on such first sealing plate 412 and the second method
The pressure that the screw threads for fastening structure of 421 lower end of blue disk generates is concentrated to 200 weeks edges of mandrel, is conducive to provide more preferably film core 300
Pretightning force, and since the sealing structure 330 is set to the inner edge of each upper diaphragm 323 and corresponding annular diversion cavity 313
Between 314, therefore such structure can also make the inner edge 314 of upper diaphragm 323, lower diaphragm 324 and corresponding annular diversion cavity 313
Between sealing performance it is more preferable.
After the material flow is inputted from material flow input port 510, material flow transport Stream is flowed to by second channel
Road 511, material flow the material flow convey 511 transmission process of flow path in, material flow after the split channel of shunting disk,
Can enter in the annular diversion cavity 313, be flowed between flow guiding disc 310 and diaphragm 320, allow diaphragm 320 to material flow into
The abundant filtration treatment of row.Material flow (or being dope) after treatment enters first passage, enters raw material along the channel
Membrane filtration module is flowed out after fluid outlet 530.
Material flow is after the processing of diaphragm 320, and the purification fluid generated in the cavity 325 on diaphragm ontology is along the sky
The purification fluid conveying flow path 521 that chamber 325 is constituted with second centre bore 321, by purifying fluid after apocenosis passage 522
Membrane filtration module is discharged in delivery outlet 520.Because each annular diversion cavity 313 is connected with corresponding first flow-guiding channel 312, the original
Stream body, which conveys flow path 511, to be connected to the annular diversion cavity 313 on flow guiding disc 310.In each upper diaphragm 323 and corresponding ring
Sealing structure 330, each lower diaphragm 324 and corresponding annular diversion cavity are respectively equipped between the inner edge 314 of shape diversion cavity 313
It is respectively equipped with sealing structure 330 between 313 inner edge 314, is to prevent material flow to the first centre bore 311 and second
321 direction of centre bore is flowed, and sealing structure 330 here can be sealing ring.
Can crack mouth on the flow guiding disc 310, and diaphragm 320 is equipped with the breach that be adapted to the sealing, the sealing with split
Mouth is respectively formed first flow-guiding channel 312, can realize above-mentioned material flow conveying flow path 511, certainly, the raw material in this way
Fluid conveying flow path 511 is connected to the annular diversion cavity 313 on flow guiding disc 310.
The sealing is opened on 310 surface of flow guiding disc or annular 313 top surface of diversion cavity or 313 bottom surface of annular diversion cavity and is split
Mouthful, it turns up, tilt to 310 two sides of flow guiding disc respectively at sealing and breach, slope surface is formed, in this way since membrane filter unit includes
Several axial directions along mandrel 200 are socketed in flow guiding disc 310 and diaphragm 320 on mandrel 200 successively, so material flow can be along original
Stream body conveying flow path 511 helically moves, to carry out abundant filtration treatment using each diaphragm, to reach filtering effect well
Fruit.Arrow direction is material flow flow direction in Figure 15.
Embodiment 2:
Embodiment 2 is roughly the same with the membrane filtration module structure of embodiment 1, but difference lies in:Stream is purified in the present embodiment
Body output using applicant application Publication No. CN103657414A, it is entitled " with end disengaging water separating filter film column and
The drainage structure of hollow core shaft 200 disclosed in the patent document of its feed liquid processing method ".I.e.:The mandrel 200 is in hollow tube
Shape, mandrel 200 are equipped with the through-hole (not shown) that the second centre bore 321 of each diaphragm 320 is connected with 200 inner cavity of mandrel, this
When, the through-hole is then used as the flow-guiding structure 201, and the tube chamber of mandrel 200 as apocenosis passage 522, open by the shaft end of mandrel 200
Mouth is described net without being respectively set on first flange disk 411 and the first sealing plate 412 as purification fluid outlet 520
Change fluid outlet 520 and apocenosis passage 522.
Axial one end of the hollow tubular mandrel 200 can be arranged to enclosed construction or is welded to connect with plug.It is former
Stream body is after the processing of diaphragm 320, and the purification fluid generated in the cavity 325 on diaphragm ontology is along the cavity 325 and institute
The purification fluid conveying flow path 521 for stating the through-hole composition of the second centre bore 321 and mandrel 200, after the tube chamber of mandrel 200
Pass through the shaft end opening discharge membrane filtration module of mandrel 200.
Embodiment 3:
As shown in figs. 2,7 and 8, embodiment 3 is roughly the same with the membrane filtration module structure of embodiment 1, but distinguishes
In:The shunting disk 610 is located on the second sealing plate 422 of second end cover component 420, and such structure is more conducive to guarantor
It demonstrate,proves shunting disk 610 and keeps radial equilibrium, and the film core 300 that is further ensured that on shunting disk 610 relative to mandrel 200
Radial equilibrium, it is uniform to be more conducive to axially loaded under the action of material flow of film core 300, avoid film core 300 because of axis
Lead to micro inclination and distortion to unbalance stress.And side is into the split channel of fluid, can utilize material flow to fluid into
The active force of the disk body wall of 611 top of hole pushes disk body band moving mandrel 200 axially movable, and further compresses film core 300.
The shunting disk 610 includes disk body, and the side of the disk body is equipped with fluid inlet orifice 611, and the axial end face of disk body is set
Have a Fluid-exiting apertures 612, the fluid inlet orifice 611 and Fluid-exiting apertures 612 connect to be formed side into fluid split channel.It uses
When, material flow is after fluid inlet orifice 611 enters split channel from 612 row of Fluid-exiting apertures to film core.The fluid inlet orifice 611 is in
Arch.Fluid inlet orifice 611 and Fluid-exiting apertures 612 are uniformly distributed along the circumferential direction of disk body.
The Fluid-exiting apertures 612 are along the axially extending formation outlet fluid 614 of disk body, 611 edge of the fluid inlet orifice
Disk body extends radially to formation fluid inlet channel 613, the fluid inlet channel 613 at the outlet fluid 614
It connects to form the L-shaped split channel in cross section with outlet fluid 614.Such structure fabrication is convenient, and transversal
The L-shaped split channel in face can also play material flow certain cushioning effect, to be conducive to subtract to a certain extent
Pressure of the small material flow to film core 300.
The fluid inlet channel 613 axially penetrates through the disk body axial end opposite with Fluid-exiting apertures 612, i.e., goes out with fluid
The edge part setting notch 616 for the disk body end face that hole 612 is opposite and sets, using between the notch 616 and the second sealing plate 422
Gap can be used as the fluid inlet channel 613.
The outlet fluid 614 includes the different epimere output channel of inner diameter size and the connection epimere output
The hypomere output channel in channel and fluid inlet channel 613.Wherein, it is logical to be more than hypomere output for the internal diameter of the epimere output channel
The internal diameter in road.In this way when fluid enters epimere output channel from fluid inlet channel 613 through hypomere output channel, the speed of fluid
Degree will reduce, and the relative pressure of fluid will increased, and advantageously ensure that film core 300 has higher filter efficiency.
The shunting disk 610 is equipped with the centre bore 615 for being socketed with mandrel 200, and the fluid inlet orifice 611 and fluid go out
Deviate the setting of the centre bore 615 in hole 612.Membrane filtration module in the present embodiment in a non-operative state, piston element 800
The upper surface of middle piston head 810 is not higher than the upper surface of the second sealing plate 422.
The shunting disk 610 can also use welding tooling as shown in Figure 9 and Figure 10 in embodiment 1 to carry out with mandrel 200
Welding.
Embodiment 4:
As shown in Fig. 3 and Figure 12, embodiment 4 is roughly the same with the structure of embodiment 3, and the shunting disk 610 is located at
On second sealing plate 422 of two end-cap assemblies 420, but difference lies in:Floating member does not include bullet in the film core pre-pressing structure
Property compensating element, 900.Sliding connection, piston head are kept between the piston head 810 and mandrel 200 of the piston element 800
It is preferably provided with sealing element between 810 and mandrel 200 and keeps sliding contact frictional fit.Also, it is not provided in the present embodiment
Second preload piece 632 passes through 422 He of the second sealing plate of second end cover component 420 using the piston rod 810 of piston element 800
Connect with screw threads for fastening respective outer side edges after second flange disk 421, the screw threads for fastening structure be locking nut, the locking nut with
The lower face contact of second flange disk 421 compresses.
Embodiment 5:
As shown in figure 4, embodiment 5 is roughly the same with the membrane filtration module structure of embodiment 1, but difference lies in:Described
One end-cap assembly 410 and second end cover component 420 are pressed on by sealing inside shell 100, i.e., described 410 He of first end cover component
Second end cover component 420 is by the way that the shell outside film core 300, first end cover component 410 and second end cover component 420 is arranged
100 compress sealing.The membrane filtration module is no Tiebar structure, and this non pull rod type structure specifically refers to applicant's application,
In Publication No. CN104128094A, entitled " a kind of with end disengaging water separating filter film column " patent document shell 100 with
The connection structure of first end cover component 410 and second end cover component 420.The shell 100 have with first end cover component 410 and
The adaptable inner cavity of second end cover component 420, first end cover component 410 and second end cover component 420 are clamped in shell 100
Portion, and it is formed with cavity between 100 inner wall of shell and film core 200.The inner wall of the shell 100 and first end cover component 410
It can be sealed by wedge, sealing structure or other existing similar structures between the lateral wall of second end cover component 420
It compresses.
The retention mechanism of its film core pre-pressing structure includes screw threads for fastening structure, and the end of the axial one end of mandrel 200 is worn
The screw threads for fastening structure is connected after crossing the first sealing plate 412, the axial other end of mandrel 200 and the second sealing plate 422 are kept
It is slidably and sealingly connected with.Sealing element is equipped between the mandrel 200 and the second sealing plate 422, the sealing element is preferably close
Seal.Its floating type hold-down mechanism does not include piston element 800, and the floating member does not include elastic compensation element 900.
421 lower end of second flange disk can be not provided with second preload piece 632, second flange disk 421 and second close
Sealing plate 422 is fixed by screw threads for fastening structure, which is screw.
After material flow is inputted from material flow input port 510, the cavity between shell 100 and film core 200 can be used as institute
Second channel is stated, flowing to material flow for material flow conveys flow path 511, and material flow is in the material flow trandfer fluid 511
In transmission process, material flow can enter in the annular diversion cavity 313, after the split channel of shunting disk in flow guiding disc 310
It is flowed between diaphragm 320, diaphragm 320 is allowed to carry out abundant filtration treatment to material flow.Wherein, material flow is by shunting
During disk 610, it can drive shunting disk that the mandrel being welded as a whole therewith is driven to move upwards, to further compress film
Core avoids the first preload piece 631 and nut being set on the first sealing plate 412 from loosening.Material flow after treatment
(or being dope) enters first passage, and enter material flow delivery outlet 530 along the channel flows out membrane filtration module later.
Embodiment 6:
Embodiment 6 is roughly the same with the membrane filtration module structure of embodiment 5, and further limits the axis of the mandrel 200
Sliding contact frictional fit is kept to the other end and the second sealing plate 422.
Embodiment 7:
Embodiment 7 is roughly the same with the membrane filtration module structure of embodiment 5, but difference lies in:The floating type compacting machine
Structure, which is additionally provided with, to be protected with the second sealing plate 422 when shunting disk 610 is compressed axially direction along film core 300 with moving mandrel 200 and moves
The piston element 800 of sliding connection is held, the piston element 800 includes keeping the company of being slidably matched with the second sealing plate 422
The piston head 810 connect, and the piston rod 820 that is connect with the piston head 810, the piston head 810 is equipped with and the mandrel
200 are connected through a screw thread the groove 811 of cooperation.
The floating member further includes the elastic compensating member being set between the piston element 800 and second flange disk 421
Part 900, the elastic compensation element 900 are waveform spring, and the waveform spring is sheathed on the piston rod 820.
The retention mechanism may also include the screw threads for fastening structure set on 421 lower end of second flange disk.The screw thread is tight
Fixing structure includes the second preload piece 632 and nut;Second preload piece 632 is integrally provided in the lower section of second flange disk 421,
The upper surface of second preload piece 632 contacts compression, second preload piece 632 and second with the lower face of second flange disk 421
Pass through screw lock between ring flange 421.421 and second sealing plate 422 of the second flange disk can pass through screw threads for fastening structure
Fixed, which is screw.
Second preload piece 632 is disc structure.Wherein, the contact surface of the second preload piece 632 and second flange disk 421
Product is more than the contact area of the first preload piece 631 and the first sealing plate 412, the screw threads for fastening knot on such first sealing plate 412
The pressure that the screw threads for fastening structure of structure and 421 lower end of second flange disk generates is concentrated to 200 weeks edges of mandrel, is conducive to film core
300 provide better pretightning force, and since the sealing structure 330 is set to each upper diaphragm 323 and corresponding annular diversion cavity
Between 313 inner edge 314, therefore such structure can also make upper diaphragm 323, lower diaphragm 324 and corresponding annular diversion cavity 313
Inner edge 314 between sealing performance it is more preferable.
It is similar to Example 1 to the setting of piston element 800 and elastic compensation element 900 in the present embodiment.
Embodiment 8:
As shown in Fig. 5, Fig. 7 and Fig. 8, embodiment 8 is roughly the same with the membrane filtration module structure of embodiment 5, but distinguishes
In:The shunting disk 610 is located on the second sealing plate 422 of second end cover component 420, and such structure is more conducive to guarantor
It demonstrate,proves shunting disk 610 and keeps radial equilibrium, and the film core 300 that is further ensured that on shunting disk 610 relative to mandrel 200
Radial equilibrium, it is uniform to be more conducive to axially loaded under the action of material flow of film core 300, avoid film core 300 because of axis
Lead to inclination and distortion to unbalance stress.And side can utilize material flow to fluid inlet orifice 611 into the split channel of fluid
The active force of the disk body wall of top pushes disk body band moving mandrel 200 axially movable, and further compresses film core 300.
The shunting disk 610 includes disk body, and the side of the disk body is equipped with fluid inlet orifice 611, and the axial end face of disk body is set
Have a Fluid-exiting apertures 612, the fluid inlet orifice 611 and Fluid-exiting apertures 612 connect to be formed side into fluid split channel.It uses
When, material flow is after fluid inlet orifice 611 enters split channel from 612 row of Fluid-exiting apertures to film core.The fluid inlet orifice 611 is in
Arch.Fluid inlet orifice 611 and Fluid-exiting apertures 612 are uniformly distributed along the circumferential direction of disk body.
The Fluid-exiting apertures 612 are along the axially extending formation outlet fluid 614 of disk body, 611 edge of the fluid inlet orifice
Disk body extends radially to formation fluid inlet channel 613, the fluid inlet channel 613 at the outlet fluid 614
It connects to form the L-shaped split channel in cross section with outlet fluid 614.Such structure fabrication is convenient, and transversal
The L-shaped split channel in face can also play material flow certain cushioning effect, to be conducive to subtract to a certain extent
Pressure of the small material flow to film core 300.
The fluid inlet channel 613 axially penetrates through the disk body axial end opposite with Fluid-exiting apertures 612, i.e., goes out with fluid
The edge part setting notch 616 for the disk body end face that hole 612 is opposite and sets, using between the notch 616 and the second sealing plate 422
Gap can be used as the fluid inlet channel 613.
The outlet fluid 614 includes the different epimere output channel of inner diameter size and the connection epimere output
The hypomere output channel in channel and fluid inlet channel 613.Wherein, it is logical to be more than hypomere output for the internal diameter of the epimere output channel
The internal diameter in road.In this way when fluid enters epimere output channel from fluid inlet channel 613 through hypomere output channel, the speed of fluid
Degree will reduce, and the relative pressure of fluid will increased, and advantageously ensure that film core 300 has higher filter efficiency.
The shunting disk 610 is equipped with the centre bore 615 for being socketed with mandrel 200, and the fluid inlet orifice 611 and fluid go out
Deviate the setting of the centre bore 615 in hole 612.
Shunting disk 610 can also use weldering as shown in Figure 9 and Figure 10 in embodiment 1 with mandrel 200 in the present embodiment
Tooling is connect to be welded.
Embodiment 9:
Embodiment 9 is roughly the same with the membrane filtration module structure of embodiment 8, but difference lies in:The floating type compacting machine
Structure, which is equipped with, to be kept with the second sealing plate 422 when shunting disk 610 is compressed axially direction along film core 300 with moving mandrel 200 and moves
The piston element 800 of sliding connection, the piston element 800 include keeping being slidably connected with the second sealing plate 422
Piston head 810, and the piston rod 820 that is connect with the piston head 810, the piston head 810 is equipped with and the mandrel 200
It is connected through a screw thread the groove 811 of cooperation.
Elastic compensation element 900, the elastic compensating member are equipped between the piston element 800 and second flange disk 421
Part 900 is waveform spring, and the waveform spring is sheathed on the piston rod 820.
The retention mechanism may also include the screw threads for fastening structure set on 421 lower end of second flange disk.The screw thread is tight
Fixing structure includes the second preload piece 632 and nut;Second preload piece 632 is integrally provided in the lower section of second flange disk 421,
The upper surface of second preload piece 632 contacts compression, second preload piece 632 and second with the lower face of second flange disk 421
Pass through screw lock between ring flange 421.421 and second sealing plate 422 of the second flange disk can pass through screw threads for fastening structure
Fixed, which is screw.
Second preload piece 632 is disc structure.Wherein, the contact surface of the second preload piece 632 and second flange disk 421
Product is more than the contact area of the first preload piece 631 and the first sealing plate 412, the screw threads for fastening knot on such first sealing plate 412
The pressure that the screw threads for fastening structure of structure and 421 lower end of second flange disk generates is concentrated to 200 weeks edges of mandrel, is conducive to film core
300 provide better pretightning force, and since the sealing structure 330 is set to each upper diaphragm 323 and corresponding annular diversion cavity
Between 313 inner edge 314, therefore such structure can also make upper diaphragm 323, lower diaphragm 324 and corresponding annular diversion cavity 313
Inner edge 314 between sealing performance it is more preferable.
Membrane filtration module in the present embodiment in a non-operative state, the upper surface of piston head 810 in piston element 800
Not higher than the upper surface of the second sealing plate 422.
It can be similar to Example 1 to the setting of piston element 800 and elastic compensation element 900 in the present embodiment.
Embodiment 10:
Embodiment 10 is roughly the same with the structure of the membrane filtration module of embodiment 9, and the shunting disk 610 is located at second end
On second sealing plate 422 of cap assemblies 420, but difference lies in:Floating member does not include that elasticity is mended in the film core pre-pressing structure
Repay element 900.The piston head 810 of the piston element 800 is slidably and sealingly connected with the holding of mandrel 200.Also, in the present embodiment
It is not provided with the second preload piece 632, the second sealing plate of second end cover component 420 is passed through using the piston rod 810 of piston element 800
422 and second flange disk 421 after connect with screw threads for fastening respective outer side edges, the screw threads for fastening structure be locking nut, the locking
Nut contacts compression with the lower face of second flange disk 421.
It can be similar to Example 3 to the setting of piston element 800 in the present embodiment.
In the following, beneficial effects of the present invention are described in detail by contrast test.
(1) maintenance period is tested
Traditional membrane filtration module and the membrane filtration module of Examples 1 to 10 are in different time points to being set to first end cover component
The results are shown in Table 1 for the maintenance of screw threads for fastening structure on 410.
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Table 1:
It is learnt by contrast test:During membrane filtration module continues use, membrane filtration module in Examples 1 to 10
For traditional membrane filtration module, just needed to be serviced after membrane filtration module was using 1000 hours, maintenance period
Substantially extend;Membrane filtration module is effectively avoided in filter process by the way that floating type hold-down mechanism is arranged in Examples 1 to 10
The case where 300 axial compression state of film core is affected, greatly improve membrane filtration module entirety fastening reliability and easily
Production and maintenance cost can be greatly reduced in maintainability.
(2) sealing performance is tested
The membrane filtration module of traditional membrane filtration module and Examples 1 to 10, integral sealing situation in different time points is such as
Shown in table 2.
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Table 2:
It is learnt by contrast test:During membrane filtration module continues use, traditional membrane filtration module is using 200
Just occur the problem of seal failure when hour, and the membrane filtration module of Examples 1 to 10 is using 1000 hours, just occurs close
The problem of envelope fails once in a while (such as:In retest three times, only seal failure is once found);In different time points, real
The overall sealing performance for applying 1~10 membrane filtration module of example is superior to traditional membrane filtration module, can greatly improve membrane filtration group
The use reliability of part, and can ensure that membrane filtration module has better strainability in a long time, and meanwhile it is also corresponding
The maintenance times reduced to membrane filtration module, there is important economic implications and environmental protection to anticipate enterprise and entire industry
Justice.