CN105903353B

CN105903353B - Membrane filtration module and its film core pre-pressing structure

Info

Publication number: CN105903353B
Application number: CN201610393177.1A
Authority: CN
Inventors: 宋岱峰; 韩亮
Original assignee: Chengdu Environmental Protection Industry Group Co Ltd Foote
Current assignee: Chengdu Meifote Membrane Environmental Protection Technology Co.,Ltd.
Priority date: 2016-06-03
Filing date: 2016-06-03
Publication date: 2019-01-18
Anticipated expiration: 2036-06-03
Also published as: CN105903353A

Abstract

The invention discloses a kind of membrane filtration module and its film core pre-pressing structures, the membrane filtration module includes 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 is located on mandrel and is made of multiple membrane filter units, the film core being made of these membrane filter units is configured to axial compression state by film core pre-pressing structure and is placed 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 the first end cover component and second end cover component, the first end cover component and second end cover component are compressed inside the housing by sealing；The film core pre-pressing structure has the floating type hold-down mechanism moved in filtering towards the direction of axial compression film core.The membrane filtration module and its film core pre-pressing structure can preferably guarantee the axial compression state of film core.

Description

Membrane filtration module and its film core pre-pressing structure

Technical field

The present invention relates to the membrane filtration module in filtration, purification field more particularly to nanofiltrations or reverse osmosis in water treatment field Permeable membrane filter assemblies and its film core pre-pressing structure.

Background technique

Present applicant develops a kind of membrane filtration module for being mainly used for sewage nanofiltration or reverse osmosis treatment, 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 configured to axial compression state by film core pre-pressing structure and is placed in the first end cover group 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, makes film core in axial by the axial pre tightening force that the nut on mandrel applies Impaction state and be placed between first end cover component and second end cover component.

Applicant has found in the long-term use process to above-mentioned membrane filtration module, often the 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 carries out discovery when analysis comparison over time, and setting exists in film core pre-pressing structure In membrane filtration module, its pretightning force will be less than design pretightning force to nut on mandrel after a period of work, tighten nut again Afterwards, membrane filtration module can restore normal operating conditions.

Applicant has found after further testing, to the fastening frequency for the nut being arranged on mandrel need to control 1 time/ 200 hours or so, just it is avoided that the problem of causing membrane filtration module to leak because of pretightning force decrease, and it is raw in actual industrial In production, sewage treatment 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 test 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., lesser 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.

Summary of the invention

In view of the above technical problems, the present invention is intended to provide a kind of can preferably guarantee film of the film mandrel to impaction state Filter assemblies and its film core pre-pressing structure and parts peculiar.

Membrane filtration module of the 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 are filtered by multiple films Unit composition, the film core being made of these membrane filter units are configured to axial compression state by film core pre-pressing structure and are placed in 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 when filter towards the direction of axial compression film core.

The floating type hold-down mechanism can play the work for fastening of floating when film core is filtered to each membrane filter unit 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 guarantee 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 significance and environmental protection to entire filtration, purification industry on the basis of not increasing enterprise's excessive cost Meaning.

For the film core pre-pressing structure of above-mentioned membrane filtration module, the film core retainer plate is located on mandrel and is filtered by multiple films single Member composition, the film core being made of these membrane filter units are configured to axial compression state by film core pre-pressing structure and are placed in the 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 in filtering towards the direction of axial compression film core.

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 be set between second end cover component and film core and can be driven and court in filtering by material flow 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, film core is made to remain preferable axial compression state, and film filtered single Member plays compensating action along the micro compressive deformation of axial generation in filtering, avoids because film core is during the filtration process because of its film mistake The case where filtering unit and generate micro compressive deformation along axial, and the pretightning force of retention mechanism is caused to weaken；Described in another aspect Floating member can also share material flow to the pressure of film core, to can 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 are arranged, and floating member energy band moving mandrel is whole towards compressing film core Direction movement has better effect to the axial compression state for guaranteeing film core.

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.

Have due to being set up in membrane filtration module for making the equally distributed shunting disk of material flow, and shunting disk is existing Membrane filtration module in be to be fixedly connected with second end cover component, therefore in order to simplify structure, reduce the production 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 drive shunting disk to move using the driving force of material flow, 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 guaranteeing shunting disk relative to mandrel Radial equilibrium, and it is further ensured that the radial equilibrium for the film core being mounted 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.

The preferred structure of shunting disk when shunting disk is located on second end cover component, for above-mentioned membrane filtration module It is, including disk body that the side of the disk body is equipped with fluid inlet orifice, an axial end face for disk body is equipped with Fluid-exiting apertures, the fluid It connects to form the split channel of side influent stream body into hole and Fluid-exiting apertures.In use, material flow enters shunting through fluid inlet orifice It is arranged from Fluid-exiting apertures to film core behind channel.The split channel of side influent stream body, can use 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, axially extending formation outlet fluid of the Fluid-exiting apertures along 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 certain buffer function to material flow, 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 upper section output channel of inner diameter size and connects on described The lower section output channel of section output channel and fluid inlet channel.When the internal diameter of upper section output channel is less than lower section 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 upper section output channel is greater than the internal diameter of lower section output channel.In this way when fluid is from fluid When input channel enters upper section output channel through lower section output channel, the speed of fluid will reduce, and the relative pressure of fluid will It increased, advantageously ensure that film core filter efficiency with higher.

Preferably, the fluid inlet orifice is domed, and structure is simple, 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, thus be conducive to improve film core in membrane filter unit overall utilization rate and guarantee 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 of welded connecting, the fixation between shunting disk and mandrel can be made stronger, be more advantageous to shunting disk It is moved with moving mandrel towards the direction of axial compression film core under material flow driving, to preferably guarantee the axial compression of film core State.

Specifically, the shunting disk the centre bore axial direction at least one end 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 and mandrel of the stage portion Welding groove is formed in the small end and mandrel of the stage portion.The outside diameter of the stage portion is greater 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 is fully welded 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 support frame；Limit Portion, the limiting section include the first limit base that can cooperate with mandrel and be correspondingly arranged with first limit base and can with divide 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 support frame.The welding Tool structure is simple, can more accurately control the concentricity of shunting disk and mandrel, and guarantee 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 ends of support frame.

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 can be with the limit shaft of mandrel cooperation Set, the first mounting plate edge, which is axially arranged with, can carry out axially position to limit shaft sleeve and can make the mandrel cooperated with limit shaft sleeve The stepped hole of shunting disk is connected after passing through.In actual installation, it need to only guarantee the concentricity and ruler of the stepped hole and limiting slot Very little and limit shaft sleeve precision is the concentricity that can guarantee after shunting disk and mandrel installation.Pass through limit shaft sleeve and limiting slot Respectively to the constraint of mandrel and shunting disk, it can guarantee that shunting disk and the precision after mandrel welding are higher.

Preferably, the second mounting plate edge is axially arranged with corresponding with the stepped hole and is at least used as the operating space 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 rods 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, guarantee 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 using flexible connection and shunting disk being caused to generate centainly during compressing 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, It avoids causing retention mechanism there is a situation where loosening because of filtering, and since the pressure of material flow when filtering often is 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 move in floating member towards the direction of axial compression film core 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 and floating member and/or mandrel linkage are arranged.The piston element can play Sealing function.

Further, the piston element and mandrel or second end cover component keep sliding contact frictional fit.

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 connecting with the piston head, the piston head are equipped with the groove cooperated with the mandrel.Such structure is also It can be very easily to the positioning of mandrel.The groove and mandrel are preferably connected through a screw thread fixation.

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 being cooperatively connected respectively with the rod assembly and across the mandrel of first end cover component.It is logical It crosses and the first end cover component is set and second end cover component can be realized fixation to shell and film core, while passing through pull rod again More pull rods and screw threads for fastening structure in component, that is, can ensure that 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 using the retention mechanism that rod assembly is combined with screw threads for fastening structure Good fastness, but in actual use, since sewage treatment 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, at 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, greatly increases the space occupied needed for entire membrane filtration module, to 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 Structure, the end of mandrel axial direction one end connect the screw threads for fastening structure after passing through 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 separated 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 interior of shell, 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 Between the lateral wall of two end-cap assemblies compression can be sealed by wedge, sealing structure or other existing similar structures.

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 composition, 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 uses on the flow guiding disc ontology In the first centre bore cooperated 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 cooperating 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 cavity of the flow-guiding structure be connected respectively with the second centre bore of each diaphragm, the flow-guiding structure and each diaphragm and the second center 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 filtered in this film Do not include the second centre bore in component with make material flow by the cross-sectional area of the second flow-guiding channel of diaphragm, it is found by the applicant that Ratio between the number product and the area of a circle that is constituted with diaphragm outer diameter of the projected area and 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 are significantly improved, and are generated 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 guarantees film core in filter process In always under the premise of the axial compression state, filter area can be significantly increased, so that the filtering of membrane filtration module is imitated Rate is higher and filtering rejection 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 Using the drainage structure of hollow core shaft, can also be used applicant's application application No. is 201610226549.1, entitled " films The drainage structure using solid mandrel mentioned in the application for a patent for invention of filter assemblies ".

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 gap between adjacent lobe, the outside circle of the lobe is engaged with the mandrel, 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, which is arranged, not only can carry out radial positioning to film core by mandrel, but also can allow purification fluid that can smoothly pass over First centre bore, the lobe can be the plate profile structure with 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 material flow conveying 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, enters material flow delivery outlet along the channel and 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 Film filtering group is discharged by purification 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 It turns up, tilt to flow guiding disc two sides respectively at mouth and breach, slope surface is formed, in this way since membrane filter unit includes several along core The axial direction of axis is successively socketed in flow guiding disc and diaphragm on mandrel, 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 sealing 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 set into Enclosed construction is welded to connect with plug.Material flow generates in the cavity on diaphragm ontology after diaphragm is handled 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 Lumen after pass through the shaft end of mandrel opening discharge membrane filtration module.

Further, each diaphragm is RO film or NF film.

RO is the abbreviation of English Reverse Osmosis membrane, and Chinese means reverse osmosis.The flowing of general water Mode is that high concentration is flowed to 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 film 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 film to carry out high Molecular filtration.

NF film is nanofiltration 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.Nanofiltration 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 also can be set where second end cover component End；The material flow input port and material flow delivery outlet also can be set 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 end surface passes through the upper end face contact compression of first flange disk and the first sealing plate, first preload piece upper end to On across first flange disk and with nut cooperate, first preload piece upper end preferably use double nut to tighten top 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 and the lower end face contact of second flange disk compress, It is locked between second preload piece and second flange disk by screw.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 stepped shaft 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 the better pretightning force of film core offer, 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 embodiment with reference to embodiments is described in further detail above content of the 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.

Detailed description of the invention

Fig. 1 is the first structural representation of the membrane filtration module in the specific embodiment of the invention with film core pre-pressing structure Figure.

Fig. 2 is second of structural representation of the membrane filtration module in the specific embodiment of the invention with film core pre-pressing structure Figure.

Fig. 3 is the third structural representation of the membrane filtration module in the specific embodiment of the invention with film core pre-pressing structure Figure.

Fig. 4 is the 4th kind of structural representation of the membrane filtration module in the specific embodiment of the invention with film core pre-pressing structure Figure.

Fig. 5 is the 5th kind of structural representation of the membrane filtration module in the specific embodiment of the invention with film core pre-pressing structure 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 to 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 to 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 to 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 to FIG. 5.

Specific embodiment

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 are set on mandrel 200 and are made of multiple membrane filter units, are filtered by these films single The film core 300 of member composition is configured to axial compression state by film core pre-pressing structure and is placed in the first end cover component 410 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 in filtering towards the direction of axial compression film core 300.

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 be set between second end cover component 420 and film core 300 and can filter when by raw material flow Body driving 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 when filter by material flow and further compresses film core 300, film core 300 is made to remain preferable axial compression state, and Compensating action is played along axial generation micro compressive deformation in filtering to membrane filter unit, avoids filtering because of film core 300 The compressive deformation micro along axial generation because of its membrane filter unit in the process, and the feelings for causing the pretightning force of retention mechanism to weaken Condition；On the other hand the floating member can also share material flow to the pressure of film core 300, to can 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 It opens and 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 cooperating 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 cooperates, 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 The conducting of second centre bore 321；Sealing is respectively equipped 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 with the conducting of the second centre bore 321 of each diaphragm 320 respectively, 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 Not including the second centre bore 321 in membrane filtration module passes through the transversal of the second flow-guiding channel 322 of diaphragm 320 with material flow is made Area, it is found by the applicant that between the number product and the area of a circle that is constituted with 320 outer diameter of diaphragm of the projected area and diaphragm 320 Ratio between 250 to 320 when, compared to conventional membrane filtration module, the filter efficiency and filtering of the application membrane filtration module 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 during the filtration process, filter area can be significantly increased, So that the filter efficiency of membrane filtration module is higher and filtering rejection is 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, the preferred shape of the diaphragm 320 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 and extend protrusion to two sides, make 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.

It include that several axial directions along mandrel 200 are successively socketed in leading on mandrel 200 in the membrane filtration module of the present embodiment Flow table 310 and diaphragm 320, the number of 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 diaphragm is 0.2 to 0.4 meter.The upper diaphragm 323 and lower diaphragm 324 are RO film or NF film.

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 on first flange disk 411 around the periphery of mandrel 200 with purification fluid outlet 520, the first sealing plate 412 is equipped with It is connected to the purification fluid conveying flow path 521 and purifies the apocenosis passage 522 of 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 second channel that the input terminal of material flow input port 510 and material flow conveying 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 (specific structure here can refer to the structure in CN103657414A), also by material flow convey flow path 511 and First passage connection, after setting solid circular shafts for mandrel 200, 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 gap between adjacent lobe 315, the outside circle of the lobe 315 is engaged with the mandrel 200, 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 with 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, and the split channel deviates in 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, punishes flow table 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 with the stage portion to the formation axially position of mandrel 200, 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 and mandrel 200 of the stage portion.

For the welding tooling of above-mentioned shunting disk 610 and mandrel 200, including fixed part, the fixed part include support frame 710；Limiting section, the limiting section include can with mandrel 200 cooperate the first limit base 720 and with first limit base 720 the second limit bases 730 that is correspondingly arranged and can cooperate with shunting disk 610, first limit base 720 and the 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 support frame 710 Form the operating space being welded to connect for shunting disk 610 and mandrel 200.

First limit base 720 and the second limit base 730 are separately positioned on the axial ends of support frame 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 mandrel 200 cooperation Set 722, first mounting plate 721 can carry out axially position to limit shaft sleeve 722 and can make and limit shaft sleeve along being axially arranged with The mandrel 200 of 722 cooperations connects the stepped hole 723 of shunting disk 610 after passing through.

Second mounting plate 731 is corresponding with the stepped hole 723 and at least as the operating space along being axially arranged with A part through-hole 733.Support frame as described above 710 includes more and is connected between the first limit base 720 and the second limit base 730 Supporting rod.It can be used between the supporting rod and the first mounting plate 721 and the second mounting plate 731 and be threadedly coupled fastening. The concentricity of shunting disk 610 Yu mandrel 200 can more accurately be controlled using above-mentioned welding tooling, and guarantee welding operation Convenient, the structural stability after shunting disk 610 is welded with mandrel 200 is good, can effectively avoid causing to shunt using being flexibly connected 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 connecting 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 cooperatively 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.

Screw threads for fastening structure with the mandrel 200 cooperation includes the first preload piece 631 and nut, second flange disk 421 The screw threads for fastening structure of lower end includes the second preload piece 632 and nut；First preload piece, 631 lower end surface passes through first flange The upper end face contact of disk 411 and the first sealing plate 422 compresses, and first preload piece, 631 upper end is upward through first flange disk 411 and cooperate 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 end face contact of ring flange 421 compresses, and is locked between second preload piece 632 and second flange disk 421 by screw.With The screw threads for fastening structure that rod assembly 620 cooperates is nut.The second flange disk 421 and the second sealing plate 422 can pass through spiral shell Line fastening structure is fixed, which is screw.

First preload piece 631 is stepped shaft structure, which contacts with the first sealing plate 412, institute Stating the second preload piece 632 is disc structure.Wherein, the contact area of the second preload piece 632 and second flange disk 421 is greater than first The contact area of preload piece 631 and the first sealing plate 412, screw threads for fastening structure and the second method on such first sealing plate 412 The pressure that the screw threads for fastening structure of blue 421 lower end of disk generates, along concentrating, was conducive to provide film core 300 more preferably to mandrel 200 weeks Pretightning force, and due to the sealing structure 330 be set to each upper diaphragm 323 with it is corresponding annular diversion cavity 313 inner edge 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 conveying 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 and second centre bore 321 are constituted passes through purification 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 It is respectively equipped with sealing structure 330 between the inner edge 314 of shape diversion cavity 313, each lower diaphragm 324 and corresponding annular diversion cavity 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 The flowing of 321 direction of centre bore, 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 successively socketed in flow guiding disc 310 and diaphragm 320 on mandrel 200, 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 is: 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 ".That is: the described 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 lumen 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 set into enclosed construction or be 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 lumen 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: on the second sealing plate 422 that the shunting disk 610 is located at second end cover component 420, such structure is more conducive to protecting It demonstrate,proves shunting disk 610 and keeps radial equilibrium relative to mandrel 200, and be further ensured that the film core 300 being mounted on shunting disk 610 Radial equilibrium avoids film core 300 because of axis so that it is uniform to be more conducive to axially loaded under the action of material flow of film core 300 Lead to micro inclination and distortion to unbalance stress.And the split channel of side influent stream body, can use 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 an axial end face for disk body is set There are Fluid-exiting apertures 612, the fluid inlet orifice 611 and Fluid-exiting apertures 612 connect to form the split channel of side influent stream body.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.

Axially extending formation outlet fluid 614 of the Fluid-exiting apertures 612 along disk body, 611 edge of 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 certain buffer function to material flow, 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 upper section output channel of inner diameter size and the connection upper section output The lower section output channel in channel and fluid inlet channel 613.Wherein, it is logical to be greater than lower section output for the internal diameter of the upper section output channel The internal diameter in road.In this way when fluid enters upper section output channel through lower section output channel from fluid inlet channel 613, the speed of fluid Degree will reduce, and the relative pressure of fluid will increased, and advantageously ensure that the filter efficiency with higher of film core 300.

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 centre bore 615 and be arranged 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 and mandrel 200 can also be carried out using welding tooling as shown in Figure 9 and Figure 10 in embodiment 1 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 is: 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 After second flange disk 421 with screw threads for fastening structure be cooperatively connected, the screw threads for fastening structure be locking nut, the locking nut with The lower end 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 is: described the One end-cap assembly 410 and second end cover component 420 are pressed on inside shell 100 by sealing, 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 in 100 compress sealing.The membrane filtration module is no Tiebar structure, and this non pull rod type structure specifically refers to applicant's application, Publication No. CN104128094A, entitled " a kind of with end disengaging water separating filter film column " patent document in 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 cavity is formed between 100 inner wall of shell and film core 200.The inner wall and first end cover component 410 of the shell 100 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, flows to material flow conveying flow path 511 for material flow, 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, enters material flow delivery outlet 530 along the channel and 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 is: the floating type compacting machine Structure, which is additionally provided with, to be protected when shunting disk 610 is compressed axially direction along film core 300 with moving mandrel 200 and moves with the second sealing plate 422 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 connecting with the piston head 810, the piston head 810 are equipped with and the mandrel 200 are connected through a screw thread the groove 811 of cooperation.

The floating member may also include the elastic compensating between the piston element 800 and second flange disk 421 Element 900, the elastic compensation element 900 are waveform spring, and the waveform spring is sheathed on the piston rod 820.

The retention mechanism further includes the screw threads for fastening structure set on 421 lower end of second flange disk.The screw threads for fastening 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 The upper surface of two preload pieces 632 and the lower end face contact of second flange disk 421 compress, second preload piece 632 and the second method It is locked between blue disk 421 by screw.The second flange disk 421 and the second sealing plate 422 can be solid by 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 greater 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, along concentrating, was conducive to film core to mandrel 200 weeks 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: on the second sealing plate 422 that the shunting disk 610 is located at second end cover component 420, such structure is more conducive to protecting It demonstrate,proves shunting disk 610 and keeps radial equilibrium relative to mandrel 200, and be further ensured that the film core 300 being mounted on shunting disk 610 Radial equilibrium avoids film core 300 because of axis so that it is uniform to be more conducive to axially loaded under the action of material flow of film core 300 Lead to inclination and distortion to unbalance stress.And the split channel of side influent stream body can use material flow to fluid inlet orifice 611 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 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 centre bore 615 and be arranged in hole 612.

Shunting disk 610 and mandrel 200 can also be using welderings as shown in Figure 9 and Figure 10 in embodiment 1 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 is: the floating type compacting machine Structure, which is equipped with, to be kept when shunting disk 610 is compressed axially direction along film core 300 with moving mandrel 200 and moves with the second sealing plate 422 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 connecting 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 and the lower end face contact of second flange disk 421 compress, second preload piece 632 and second It is locked between ring flange 421 by screw.The second flange disk 421 and the second sealing plate 422 can pass through screw threads for fastening structure Fixed, which is screw.

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 is: floating member does not include elastic benefit 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 with screw threads for fastening structure be cooperatively connected, the screw threads for fastening structure be locking nut, the locking The lower end face contact of nut and second flange disk 421 compresses.

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 set on 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:

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 once find seal failure)；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 film filtering group The use reliability of part, and can guarantee that membrane filtration module has better strainability in a long time, while also corresponding The maintenance times reduced to membrane filtration module, there is important economic significance and environmental protection to anticipate enterprise and entire industry Justice.

Claims

1. 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) it is set on mandrel (200) and is made of multiple membrane filter units, the film core (300) being made of these membrane filter units Axial compression state, which is configured to, by film core pre-pressing structure is placed in the first end cover component (410) and second end cover component (420) between, the shell (100) setting film core (300) outside and be separately connected the first end cover component (410) and Second end cover component (420), the first end cover component (410) and second end cover component (420) are pressed on shell by sealing (100) internal；When filtering, material flow through the material flow input port (510) flow into after, through with second end cover component (420) it is opposite with first end cover component (410) backward to pass sequentially through each membrane filter unit for film core (300) axial end that is opposite and setting And the axial end motion of film core (300) set, filtered purification fluid are discharged from the purification fluid outlet (520), it is special Sign is: the film core pre-pressing structure has the floating type compression moved in filtering towards the direction of axial compression film core (300) Mechanism；The floating type hold-down mechanism include be set between second end cover component (420) and film core (300) and can filter when by Material flow driving and towards the direction of axial compression film core (300) move floating member.

2. membrane filtration module as described in claim 1, it is characterised in that: the floating type hold-down mechanism includes by film core (300) retention mechanism of the axial compression between first end cover component (410) and second end cover component (420), the float portion Part includes the shunting disk (610) being sheathed on mandrel (200).

3. membrane filtration module as claimed in claim 2, it is characterised in that: the floating member and mandrel (200) linkage are arranged.

4. membrane filtration module as described in claim 1, it is characterised in that: the film core (300) is set on mandrel (200) simultaneously It is made of multiple membrane filter units being axially sequentially stacked along mandrel (200)；The membrane filter unit includes number Zhang Yici socket Flow guiding disc (310) and diaphragm (320) on mandrel (200) are equipped with one between every two adjacent flow guiding discs (310) Diaphragm (320)；Each flow guiding disc (310) includes flow guiding disc ontology and is set on the flow guiding disc ontology for matching with mandrel (200) The first centre bore (311) closed, and deviate the first flow-guiding channel (312) of first centre bore (311), each flow guiding disc sheet Be additionally provided with the annular diversion cavity (313) for accommodating corresponding diaphragm (320) on the side of body, each annular diversion cavity (313) with it is corresponding First flow-guiding channel (312) conducting；Each diaphragm (320) includes diaphragm ontology and is used on the diaphragm ontology and mandrel (200) the second centre bore (321) cooperated, and deviate the second flow-guiding channel (322) of second centre bore (321)；Each film Piece ontology includes upper diaphragm (323), lower diaphragm (324) and the cavity between upper diaphragm (323) and lower diaphragm (324) (325), the cavity (325) and the second centre bore (321) are connected；Each upper diaphragm (323) and corresponding annular diversion cavity (313) Inner edge (314) between be respectively equipped with sealing structure (330), each lower diaphragm (324) and corresponding annular diversion cavity (313) Sealing structure (330) are respectively equipped between inner edge (314)；The mandrel (200) be equipped with respectively with each diaphragm (320) the The flow-guiding structure (201) of two centre bores (321) conducting, the cavitys (325) of the flow-guiding structure (201) and each diaphragm (320) with And second centre bore (321) constitute with purification fluid outlet (520) conducting purification fluid conveying flow path (521)；Each water conservancy diversion The first flow-guiding channel (312) of disk (310) and second flow-guiding channel (322) of each diaphragm (320) are sequentially communicated composition raw material flow Body conveys flow path (511)；The first end cover component (410) includes first flange disk (411) and the first sealing plate (412), institute Stating second end cover component (420) includes second flange disk (421) and the second sealing plate (422)；The film core (300) is held in Between first sealing plate (412) and the second sealing plate (422), the first sealing plate (412) is held in film core (300) and the Between one ring flange (411), the second sealing plate (422) is held between film core (300) and second flange disk (421), shell (100) be fixed between first flange disk (411) and second flange disk (421), the mandrel (200) at least with the first sealing plate (412) it is tightly connected；The original with material flow conveying flow path (511) conducting is additionally provided on the first flange disk (411) Expect fluid outlet (530), the material flow delivery outlet (530), material flow input port (510) and purification fluid outlet (520) periphery on first flange disk (411) around mandrel (200) is arranged, and the first sealing plate (412) is equipped with described in connection It purifies fluid conveying flow path (521) and purifies the apocenosis passage (522) of fluid outlet (520), be equipped in the shell (100) First passage that the output end of material flow delivery outlet (530) and material flow conveying flow path (511) is connected and by raw material The second channel that fluid input port (510) is connected with the input terminal of material flow conveying flow path (511).

5. the membrane filtration module as described in one of claim 2 to 3, it is characterised in that: the retention mechanism includes screw threads for fastening Structure, the end of mandrel (200) axial direction one end pass through first end cover component (410) and connect the screw threads for fastening structure, mandrel afterwards (200) the axial other end keeps being slidably and sealingly connected with second end cover component (420).

6. membrane filtration module as claimed in claim 5, it is characterised in that: the floating type hold-down mechanism, which is additionally provided with, to float When component is moved towards the direction of axial compression film core (300), sliding is kept to match with mandrel (200) or second end cover component (420) Close the piston element (800) of connection；It is slidably connected when the piston element (800) and second end cover component (420) are kept When, piston element (800) and floating member and/or mandrel (200) linkage are arranged.

7. for the film core pre-pressing structure of membrane filtration module described in one of claim 1 to 6, the film core (300) is set in core It is formed on axis (200) and by multiple membrane filter units, the pre- tight knot of film core is passed through by the film core (300) that these membrane filter units form Structure is configured to axial compression state and is placed between first end cover component (410) and second end cover component (420), described first End-cap assembly (410) and second end cover component (420) are by being arranged in film core (300), first end cover component (410) and second end The external shell (100) of cap assemblies (420) compresses sealing；When filtering, material flow pass through it is opposite with second end cover component (420) and Film core (300) axial end set passes sequentially through that each membrane filter unit is opposite with first end cover component (410) backward and the film core set (300) axial end motion, it is characterised in that: the film core pre-pressing structure has in filtering towards the side of axial compression film core (300) To the floating type hold-down mechanism of movement.

8. film core pre-pressing structure as claimed in claim 7, it is characterised in that: the floating type hold-down mechanism includes by film core (300) retention mechanism of the axial compression between first end cover component (410) and second end cover component (420), and it is set to the Between two end-cap assemblies (420) and film core (300) and can be driven in filtering by material flow and towards axial compression film core (300) Direction movement floating member, the floating member includes the shunting disk (610) that is sheathed on mandrel (200).

9. film core pre-pressing structure as claimed in claim 8, it is characterised in that: the floating member is set with mandrel (200) linkage It sets.

10. film core pre-pressing structure as claimed in claim 8 or 9, it is characterised in that: the retention mechanism includes screw threads for fastening knot Structure, the end of mandrel (200) axial direction one end pass through first end cover component (410) and connect the screw threads for fastening structure, mandrel afterwards (200) the axial other end keeps being slidably and sealingly connected with second end cover component (420).