CN105921022A - Processing process for filter membrane - Google Patents
Processing process for filter membrane Download PDFInfo
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- CN105921022A CN105921022A CN201610464464.7A CN201610464464A CN105921022A CN 105921022 A CN105921022 A CN 105921022A CN 201610464464 A CN201610464464 A CN 201610464464A CN 105921022 A CN105921022 A CN 105921022A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
- B01D63/062—Tubular membrane modules with membranes on a surface of a support tube
- B01D63/065—Tubular membrane modules with membranes on a surface of a support tube on the outer surface thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
- B01D63/061—Manufacturing thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0011—Casting solutions therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/024—Oxides
- B01D71/027—Silicium oxide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/30—Polyalkenyl halides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/30—Polyalkenyl halides
- B01D71/32—Polyalkenyl halides containing fluorine atoms
- B01D71/34—Polyvinylidene fluoride
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/44—Polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds, not provided for in a single one of groups B01D71/26-B01D71/42
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/52—Polyethers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
- B01D2325/025—Finger pores
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/30—Chemical resistance
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
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- Inorganic Chemistry (AREA)
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention relates to a processing process for a filter membrane, and belongs to the technical field of filter membrane processing. The processing process comprises the following steps: weighing raw materials of a PET braided tube, forming the raw materials after mixing the raw materials, and braiding the raw materials to obtain the PET braided tube; weighing raw materials of a membrane substrate coating, pouring a PVC material into a solvent, stirring for 1-2 hours at a temperature being 60-80 DEG C, pouring other raw materials of the membrane substrate coating, stirring the raw materials for 18-23 hours and then heating the raw materials to a temperature being 85-100 DEG C, and stirring the raw materials until a casting membrane solution is obtained; then, standing and de-foaming for 10-15 hours at a temperature being 30-50 DEG C; enabling the PET braided tube to penetrate into a spinning nozzle, spraying the casting membrane solution to the spinning nozzle at a constant speed by virtue of a metering pump, and coating the surface of the PET braided tube with the casting membrane solution of the membrane substrate coating; and finally, taking down membrane yarns, and enabling the membrane yarns to sequentially pass through a primary coagulating bath, a secondary coagulating bath and a tertiary cleaning tank, thereby preparing the filter membrane. According to the filter membrane, one layer of the inner supporting tube is additionally arranged in the membrane substrate coating, and the membrane substrate coating and raw materials of the inner supporting tube are reasonably combined, so that the mechanical property of the membrane is improved, the water flux and the retention rate of the membrane are increased, and the service life of the filter membrane is prolonged.
Description
Technical field
The present invention relates to the processing technique of a kind of filter membrane, belong to the technology of filter membrane processing
Field.
Background technology
Along with China's rapid development of economy, water resource increasingly becomes the system of economic development
About factor, therefore reduces sewage discharge, and the regeneration carrying out water has become a kind of inevitable
Trend.Traditional wastewater Regeneration Treatment technology also exists that effluent characteristics is the highest, it is big, steady to take up an area
The shortcomings such as qualitative difference, cannot meet new requirement, and new technique-water treatment by membrane should
Fortune and give birth to, this technique is applied to making profits again of water purification and sewage the most more and more
With.Membrane separation technique has that energy consumption is low, process is simple, separation efficiency is high, dirty without environment
The advantages such as dye, are to solve the energy in the present age, resource and the important new and high technology of environmental problem,
That other any chemical separation technologies are irreplaceable, its application have been directed to chemical industry,
The fields such as food, medicine, biochemistry, environmental protection, to saving the energy, improving efficiency, purification
Environment etc. are made that significant contribution, the most rising by being abroad referred to as 21st century
One of ten big new and high technologies.Wherein, ultrafiltration (UF) is that the film with pressure as motive force divides
From process, it be based on selectivity fence effect by granule and larger molecular organics matter from stream
Body is separated, to realize the process purified.Particles in solution particle diameter exists
The filtration that solute in 0.01 μm～1 μ m is retained by the perforated membrane with special pore size distribution
Operation.Ultrafilter membrane is for larger molecular organics, colloid, algae, antibacterial, virus, interior
The material such as toxin, granule has the removal efficiency of superelevation.Ultrafilter membrane generally use CA, CTA,
CN, PAN, PS, PES, PC, PET, PI, PE, PP, PVC, PVDF are (poly-
Vinylidene) etc. high molecular polymer.Wherein, Kynoar (PVDF) is one
Planting fluorocarbon thermoplastic plastics, its crystalline melt point is about 170 DEG C, and heat decomposition temperature is at 360 DEG C
Above, long-term temperature range-50-150 DEG C.Under 0.45MPa load pressure,
Its heat distortion temperature is 150 DEG C.Kynoar has good against weather and chemistry steady
Qualitative, to be irradiated 1 year by the ultraviolet that wavelength is 200-400nm, its performance is basically unchanged,
The at room temperature strong oxidizer such as acid and alkali, alkali and halogen corrosion.Owing to it has above-mentioned all
Many advantages, and the formation preferable thin film of pore performance can be cast, it is in special fibre separation film
A kind of new and effective separation film kind, can be widely applied to chemical industry, environmental protection, food, drink
The aspects such as material, biochemical pharmacy, health care and industry water purified treatment, but single poly-
Film strength and water flux that vinylidene is made are general.
Summary of the invention
Present invention aims to the deficiency of above-mentioned existence, it is provided that a kind of simple
The processing technique of filter membrane, prepared filter membrane has the performance such as high intensity, high flux.
For realizing the purpose of foregoing invention, the present invention adopts the following technical scheme that: a kind of mistake
The processing technique of filter membrane, described processing technique comprises the steps:
S1, weigh the raw material of PET braided tube: PET, glass fibre, nano silicon,
Modified alta-mud, Polyethylene Glycol, by double screw extruder extrusion molding after raw material is mixed,
And work out to obtain PET braided tube by basketry；
S2, weigh the raw material of film base material coating: Kynoar (PVDF), polychlorostyrene second
Alkene (PVC), polyvidone (PVP), Polyethylene Glycol, solvent, first fall PVC material
Entering in solvent, stir 1-2h at 60-80 DEG C, other being subsequently poured into film base material coating are former
Material, is warming up to 85-100 DEG C after stirring 18-23h, continues stirring at this temperature until obtaining
The casting solution of mix homogeneously, then 30-50 DEG C of standing and defoaming 10-15h in Debubbling tank；
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface；
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by the present invention by inner support tube and
It is coated in the film base material coating filter membrane dimerous on inner support tube surface.
The filter membrane of the present invention adds one layer of inner support tube in film base material coating, and (i.e. PET compiles
Knit pipe) in order to improve stretch capability and the ageing resistance of filter membrane, the film base material of outer layer is coated with
Layer, by its constituent of reasonable compatibility, improves the performance of filter membrane, especially improved
Corrosion-resistant, the hydrophilic of filter membrane and pliability, be coated in inner support tube surface and carry further
Exceed the service life of filter membrane so that it is the life-span can reach about 3 years.
In prior art, the standing and defoaming time of casting solution is the longest generally 48 hours
Above, but the raw material of inventive film substrate coating is by first stirring PVC at 60-80 DEG C
Mix, then be warming up to 85-100 DEG C again after pouring other raw material stirring into and be stirred, the most significantly
Degree improves the uniformity of casting solution, is also greatly shortened the standing and defoaming time, and then improves film
Water flux and rejection, and improve the mechanical performance of film.
The raw material of described PET braided tube includes following constituent and number thereof: PET:
50-70 part, glass fibre: 5-20 part, nano silicon: 5-20 part, bentone
Soil: 5-10 part, Polyethylene Glycol: 5-10 part.PET braided tube in filter membrane of the present invention with
PET is matrix, take full advantage of the high strength and modulus of PET and corrosion-resistant, solvent resistant,
High temperature resistant etc.；It is simultaneously introduced glass fibre, nano silicon, modified alta-mud etc. to strengthen
Agent, by the compounding mechanical property using the synergism produced to improve PET braided tube further
Can, especially improve the hot strength about 180% of PET braided tube, and then make PET weave
Pipe has higher intensity, modulus, also have preferable Corrosion Protection, resistance to elevated temperatures,
Solvent resistance, impact resistance performance, and then improve the service life of filter membrane.
In the processing technique of above-mentioned filter membrane, in step S1, double screw extruder is extruded into
Xing Shi mono-district temperature is 200-220 DEG C, and two district's temperature are 220-230 DEG C, and three district's temperature are
230-240 DEG C, four district's temperature are 240-260 DEG C.
The raw material of described film base material coating includes following constituent and mass percent thereof:
Kynoar (PVDF): 6-17%,
Polrvinyl chloride (PVC): 4-7%,
Polyvidone (PVP): 3-8%,
Polyethylene Glycol: 12-25%,
Surplus is solvent,
Wherein, Kynoar: the content of polrvinyl chloride is than being (1.5-2.5): 1.
The present invention uses Kynoar (PVDF) and polrvinyl chloride (PVC) part phase
The co-mixing system of volume system, is blended proportioning raising filter membrane film base material painting by controlling polymer
The performance of layer.The present invention is by constantly testing discovery, film base material coating material constituent shape
Along with the increase of polrvinyl chloride (PVC) solid content, the flux of filter membrane in the casting solution become
It is the trend of first increases and then decreases with average pore size, works as Kynoar: containing of polrvinyl chloride
Amount ratio is for (1.5-2.5): when 1, the flux of filter membrane is bigger.Especially work as polyvinylidene fluoride
Alkene: the content ratio of polrvinyl chloride is during for 2:1, and the flux of filter membrane reaches maximum.
It addition, polymer blend in the casting solution of film base material coating material constituent formation
Content is also the key factor affecting final filtration film properties.At filter membrane film base material of the present invention
In the raw material of coating, if Kynoar (PVDF) and polrvinyl chloride (PVC's) is total to
The mass percent of mixed polymer, more than 25%, can cause flux and the hole of final filtration film
Rate reduces, and its reason is: along with the increase of polymer blend content, big in unit volume
The increased number of molecule, macromolecule is assembled in a large number, not only increases the density in network hole, and
And add the winding between adjacent micella.In cast film process, high polymer quality divides
Number is conducive to the initial association of polymer, forms little and homogeneous gel phase, the network hole of film
And the average pore size in micella hole all declines, porosity is inevitable to be declined simultaneously.The decline of porosity
Macroscopically show as the decline of membrane flux.It addition, the casting film that polymer blend content is higher
The porous network wall that liquid is formed is thicker, add water by time resistance, make permeable speed
Slowing down, this is also the reason that water flux declines.When Kynoar (PVDF) with
When the mass percent of the polymer blend of polrvinyl chloride (PVC) is 10-20%, film base
The inside and outside epidermal area of material coating also exists the thinnest compacted zone, is to be distributed more inside compacted zone
Uniform little finger-like pore, film base material coating intermediate layer is big class finger-like hole and spongy hole
Structure, the micropore quantity on the outer surface of coating is relatively more and aperture ratio is relatively big, and this film is tied
Structure has higher water flux.Along with polymer blend mass fraction increases, when film base material is coated with
Layer polymer blend mass percent is more than 25%, and coating intermediate layer is also big hole, but
Coating appearance cortex becomes the finest and close, and compacted zone is the thickest, simultaneously micro-in spongiosis
Aperture, hole also diminishes, and the hole number of film outer surface is less, aperture is less, and therefore the water of film leads to
Measure relatively low.Therefore, the content of Kynoar and polrvinyl chloride is controlled by the present invention respectively
In the range of 6-17%, 4-7%.
It is additive that filter membrane of the present invention uses containing large hydrophilic molecular PVP, the dissolving of PVP
Property, water absorption good, can keep the most preferable adhesivity, and without polyvinyl alcohol, formaldehyde
Etc. harmful material, and along with the increase of PVP content, film in certain content range
Flux is gradually increased.
The intrinsic viscosity of the Kynoar described in film base material coating material is
1.65-2.0, weight average molecular weight is 40 ten thousand to 80 ten thousand dalton.
The average degree of polymerization of the polrvinyl chloride described in film base material coating is 1000-3000.
Solvent described in film base material coating material is dimethyl acetylamide, dimethyl formyl
Amine, N-Methyl pyrrolidone.Compared with dimethylformamide, use dimethyl acetylamide
The water flux of the filter membrane making solvent is bigger.Although N-Methyl pyrrolidone is the system of solvent
The water flux of the filter membrane of film liquid system gained is higher, but N-Methyl pyrrolidone price
Expensive.Therefore, comprehensive each factor, as preferably, described solvent is dimethyl acetylamide.
Described film base material coating material also includes accounting for film base material coating material gross mass 2-4%
Modified manometer silicon dioxide.Nano-meter SiO_22Particle surface is owing to having abundant silicone hydroxyl and relatively
Strong skin effect, fills it into the hardness of polymer in coating material, toughness, hydrophilic
Property.Containing Nano-meter SiO_22The filter membrane of particle is combined good during processing sewage with polymer
Good, the contact angle of film can be effectively reduced, and flux is the most stable, is greatly increased filter membrane
Anti-pollution ability.It addition, containing Polyethylene Glycol in the raw material of inventive film substrate coating,
Nano silicon dispersibility in the base can be improved so that it is be easier to be uniformly dispersed.
Further preferred, described modified manometer silicon dioxide changes by the following method
Property: selection gamma-aminopropyl-triethoxy-silane is coupling agent, is dissolved in ethanol water
It is made into the solution that mass concentration is 8-15%, first stirs 1-2h with glacial acetic acid regulation pH to 3,
Again with ammonia regulation pH value to 11 and stir and add SiO after 1-2h2It is warming up to 90 DEG C and carries out idol
Connection reaction treatment 1-2h, is then vacuum dried in 65 DEG C and i.e. obtains modified manometer silicon dioxide grain
Son.
Use gamma-aminopropyl-triethoxy-silane modified to Nano-meter SiO_22Modification, is effectively reduced
Nano-meter SiO_22The surface of particle can so that it is is difficult to reunite.With unmodified Nano-meter SiO_22
Compare, through ultrasonic disperse, modified Nano SiO2Do not reunite, can be the most dispersed；
Add and fill modified SiO2The toughness of the coating of particle has had and has significantly improved, minimum bend length and connecing
Feeler is all effectively reduced；Due to Nano-meter SiO_22The strongly hydrophilic of particle makes film base material coating table
Face (i.e. filter membrane surface) forms a hydrophilic layer, thus has restrained the formation of gel layer, prolongs
Grow the use time, improve anti-pollution ability.During use, flux is the most stable,
And Nano-meter SiO_22In use not falling off, the modified effect making coating is lasting and notable, and then
Improve the performance of filter membrane.
In the processing technique of above-mentioned filter membrane, after step S2 stirs at 85-100 DEG C,
Before the casting solution of mix homogeneously, also include that ultrasound wave disperses.Nanoparticle is in dispersive process
It is easy to again reunite, after using preliminary dispersed with stirring, then is disperseed by ultrasonic wave concussion
Nano silicon aggregate can be ground into little granule, thus increase nano-particle and other
The compatibility of composition.As preferably, ultrasonic dispersing time is 10-20min.
In the processing technique of above-mentioned filter membrane, the extrusion frequency of dosing pump described in step S3
Rate is 24-28Hz, and spinning-drawing machine winding frequency is 20-26Hz.
In the processing technique of above-mentioned filter membrane, first coagulating bath described in step S4
In containing the solvent of 40-60%, gel solidification 8-20s.Solvent by first coagulating bath
Concentration controls at 40-60%, is effectively improved acceleration molding and the solidification of filter membrane.?
If solvent strength is excessive in one coagulating bath, easily cause the difficulty of follow-up cleaning, if molten
Agent concentration is too low, the most not easy-formation.
In the processing technique of above-mentioned filter membrane, described second coagulating bath contains
The solvent of 5-20%, gel solidification 5-10s.Second coagulating bath can leach front road tank
Band comes the bigger solvent of concentration.
In the processing technique of above-mentioned filter membrane, described first coagulating bath and second coagulate
Gu the solvent in Yu is dimethyl acetylamide (DMAC).
In the processing technique of above-mentioned filter membrane, being clear water in the 3rd road rinse bath, purpose exists
In the solvent of front twice is cleaned.
The filter membrane that present invention processing obtains by inner support tube and is coated in inner support tube surface
Film base material coating two parts composition, the wall thickness 0.3-0.35mm of inner support tube, film base material be coated with
The thickness of layer is 0.08-0.1mm, and described inner support tube is PET braided tube.
In the present invention, film base material coating uniform is wrapped in inner support tube outer surface, with interior
The thickness propping up stay tube is compared, and film base material coating layer thickness is significantly smaller, only accounts for filter membrane wall thickness
About 25%.Whole film base material is thin porous spongy structure, thus decreases casting
The usage amount of film liquid, reduces the cost of film preparation.And when film base material coating is the thinnest, mistake
The self resistance of filter membrane is the least, thus filter membrane pure water flux is the biggest, but due to interior
The existence of stay tube, flux magnitude is also affected by inner support tube.When inner support tube external diameter increases
Time big, filter membrane pure water flux, average pore size all increase significantly, and porosity
Reduce, this is because under identical number of spindles and mesh number, inner support tube internal diameter is the least, interior
The cellosilk supporting tube-surface is the most closely knit, then in inner support tube, nodes is the most, makes filtration
The film effective filtration area when filtering reduces, thus causes the pure water flux of film to reduce,
Average pore size diminishes.And when inner support tube external diameter is constant, mesh number the least inner support tube table
Face nodes is the fewest, and resistance of membrane filtration reduces, and the pure water flux of film, average pore size all have
Being increased, porosity but decreases by contrast, therefore when inner support tube surface node
When number is the most, when inner support tube is more densely cross-linked, in filter membrane, preservable amount of liquid also will
Increase, thus porosity value is the highest.
Compared with prior art, present invention have the advantage that
1, filter membrane of the present invention by add in film base material coating one layer of inner support tube in order to
Improve stretch capability and the ageing resistance of filter membrane.
2, the film base material coating of outer layer passes through its constituent of reasonable compatibility, improves and filters
The performance of film, especially improves corrosion-resistant, hydrophilic and the pliability of filter membrane, coating
The service life of filter membrane is improved further so that it is the life-span can reach on inner support tube surface
About 3 years.
3, the PET braided tube in filter membrane is with PET as matrix, be simultaneously introduced glass fibre,
The reinforcing agent such as nano silicon, modified alta-mud, by the compounding collaborative work using and producing
By the mechanical property of raising PET braided tube further, especially improve drawing of PET braided tube
Stretch intensity about 180%, and then improve the service life of filter membrane.
4, the processing technique simple possible of filter membrane of the present invention, the raw material of film base material coating
By first PVC being stirred at 60-80 DEG C, then heat up again after pouring other raw material stirring into
It is stirred to 85-100 DEG C, not only increases substantially the uniformity of casting solution, the most significantly
Shorten the standing and defoaming time, and then improve water flux and the rejection of film, and improve film
Mechanical performance.
Accompanying drawing explanation
Fig. 1 is the structural representation of filter membrane of the present invention.
Fig. 2 is the top view of filter membrane of the present invention.
In figure, 1, inner support tube；2, film base material coating.
Detailed description of the invention
The specific embodiment that the following is the present invention combines accompanying drawing, to technical scheme
It is further described, but the present invention is not limited to these embodiments.
A kind of filter membrane as depicted in figs. 1 and 2, filter membrane is by inner support tube 1 and is coated in
Film base material coating 2 two parts composition on inner support tube surface, the wall thickness of inner support tube 1
0.3-0.35mm, the thickness of film base material coating 2 is 0.08-0.1mm.
Embodiment 1
A kind of filter membrane, filter membrane is by inner support tube and the film base being coated in inner support tube surface
Material coating two parts form, the wall thickness 0.32mm of inner support tube, the thickness of film base material coating
For 0.09mm, inner support tube is PET braided tube, and the raw material of described film base material coating includes
Following constituent and mass percent thereof: Kynoar (PVDF): 14%, poly-
Vinyl chloride (PVC): 6%, polyvidone (PVP): 5%, Polyethylene Glycol: 18%,
Modified manometer silicon dioxide: 3%, surplus is solvent dimethyl acetylamide；Described PET compiles
Knit the raw material of pipe and include following constituent and number thereof: PET:60 part, glass fibre:
12 parts, nano silicon: 12 parts, modified alta-mud: 8 parts, Polyethylene Glycol: 8 parts.
Described filter membrane is processed prepared as follows:
S1, weigh the raw material of above-mentioned PET braided tube, squeezed by twin screw after raw material is mixed
Go out machine extrusion molding, and work out to obtain PET braided tube by basketry；Double screw extruder
During extrusion molding, one district's temperature is 210 DEG C, and two district's temperature are 225 DEG C, and three district's temperature are
235 DEG C, four district's temperature are 250 DEG C, and the time of staying is 2 minutes.
S2, weigh the raw material of film base material coating, first PVC material is poured in solvent, at 70 DEG C
Lower stirring 1.5h, is subsequently poured into other raw materials of film base material coating, is warming up to after stirring 20h
90 DEG C, carry out ultrasound wave dispersion after continuing stirring at this temperature until being uniformly mixed
Casting solution, then 40 DEG C of standing and defoaming 12h in Debubbling tank.
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface, metering
Pump extrusion frequency is 26Hz, and spinning-drawing machine winding frequency is 23Hz.
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by filter membrane.
Embodiment 2
A kind of filter membrane, filter membrane is by inner support tube and the film base being coated in inner support tube surface
Material coating two parts form, the wall thickness 0.33mm of inner support tube, the thickness of film base material coating
For 0.085mm, inner support tube is PET braided tube, and the raw material of described film base material coating includes
Following constituent and mass percent thereof: Kynoar (PVDF): 10%, poly-
Vinyl chloride (PVC): 5%, polyvidone (PVP): 6%, Polyethylene Glycol: 18%,
Modified manometer silicon dioxide: 3%, surplus is solvent dimethylformamide；Described PET compiles
Knit the raw material of pipe and include following constituent and number thereof: PET:55 part, glass fibre:
15 parts, nano silicon: 18 parts, modified alta-mud: 6 parts, Polyethylene Glycol: 6 parts.
Described filter membrane is processed prepared as follows:
S1, weigh the raw material of above-mentioned PET braided tube, squeezed by twin screw after raw material is mixed
Go out machine extrusion molding, and work out to obtain PET braided tube by basketry；Double screw extruder
During extrusion molding, one district's temperature is 205 DEG C, and two district's temperature are 222 DEG C, and three district's temperature are
233 DEG C, four district's temperature are 245 DEG C, and the time of staying is 2 minutes.
S2, weigh the raw material of film base material coating, first PVC material is poured in solvent, at 65 DEG C
Lower stirring 2h, is subsequently poured into other raw materials of film base material coating, is warming up to after stirring 19h
88 DEG C, carry out ultrasound wave dispersion after continuing stirring at this temperature until being uniformly mixed
Casting solution, then 35 DEG C of standing and defoaming 12h in Debubbling tank.
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface, metering
Pump extrusion frequency is 25Hz, and spinning-drawing machine winding frequency is 22Hz.
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by filter membrane.
Embodiment 3
A kind of filter membrane, filter membrane is by inner support tube and the film base being coated in inner support tube surface
Material coating two parts form, and the wall thickness 0.4mm of inner support tube, the thickness of film base material coating is
0.095mm, inner support tube is PET braided tube, the raw material of described film base material coating include as
Lower constituent and mass percent thereof: Kynoar (PVDF): 13%, polychlorostyrene
Ethylene (PVC): 6%, polyvidone (PVP): 7%, Polyethylene Glycol: 22%, change
Property nano silicon: 2%, surplus is solvent N-methyl pyrilidone；Described PET compiles
Knit the raw material of pipe and include following constituent and number thereof: PET:65 part, glass fibre:
10 parts, nano silicon: 8 parts, modified alta-mud: 8 parts, Polyethylene Glycol: 8 parts.
Described filter membrane is processed prepared as follows:
S1, weigh the raw material of above-mentioned PET braided tube, squeezed by twin screw after raw material is mixed
Go out machine extrusion molding, and work out to obtain PET braided tube by basketry；Double screw extruder
During extrusion molding, one district's temperature is 215 DEG C, and two district's temperature are 228 DEG C, and three district's temperature are
238 DEG C, four district's temperature are 255 DEG C, and the time of staying is 2 minutes.
S2, weigh the raw material of film base material coating, first PVC material is poured in solvent, at 75 DEG C
Lower stirring 1h, is subsequently poured into other raw materials of film base material coating, is warming up to after stirring 22h
95 DEG C, carry out ultrasound wave dispersion after continuing stirring at this temperature until being uniformly mixed
Casting solution, then 45 DEG C of standing and defoaming 12h in Debubbling tank.
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface, metering
Pump extrusion frequency is 27Hz, and spinning-drawing machine winding frequency is 25Hz.
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by filter membrane.
Embodiment 4
A kind of filter membrane, filter membrane is by inner support tube and the film base being coated in inner support tube surface
Material coating 2 two parts form, the wall thickness 0.3mm of inner support tube 1, the thickness of film base material coating
For 0.08mm, inner support tube is PET braided tube, and the raw material of described film base material coating includes
Following constituent and mass percent thereof: Kynoar (PVDF): 17%, poly-
Vinyl chloride (PVC): 7%, polyvidone (PVP): 3%, Polyethylene Glycol: 12%,
Surplus is solvent N-methyl pyrilidone；The raw material of described PET braided tube includes forming as follows
Composition and number thereof: PET:50 part, glass fibre: 20 parts, nano silicon: 5
Part, modified alta-mud: 10 parts, Polyethylene Glycol: 10 parts.
Described filter membrane is processed prepared as follows:
S1, weigh the raw material of above-mentioned PET braided tube, squeezed by twin screw after raw material is mixed
Go out machine extrusion molding, and work out to obtain PET braided tube by basketry；Double screw extruder
During extrusion molding, one district's temperature is 220 DEG C, and two district's temperature are 230 DEG C, and three district's temperature are
240 DEG C, four district's temperature are 260 DEG C, and the time of staying is 2 minutes.
S2, weigh the raw material of film base material coating, first PVC material is poured in solvent, at 80 DEG C
Lower stirring 1h, is subsequently poured into other raw materials of film base material coating, is warming up to after stirring 18h
100 DEG C, continue stirring at this temperature until the casting solution that is uniformly mixed, then exist
50 DEG C of standing and defoaming 10h in Debubbling tank.
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface, metering
Pump extrusion frequency is 28Hz, and spinning-drawing machine winding frequency is 26Hz.
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by filter membrane.
Embodiment 5
A kind of filter membrane, filter membrane is by inner support tube and the film base being coated in inner support tube surface
Material coating 2 two parts form, the wall thickness 0.35mm of inner support tube 1, the thickness of film base material coating 2
Degree is 0.1mm, and inner support tube is PET braided tube, and the raw material of described film base material coating includes
Following constituent and mass percent thereof: Kynoar (PVDF): 6%, polychlorostyrene
Ethylene (PVC): 4%, polyvidone (PVP): 8%, Polyethylene Glycol: 25%, remaining
Amount is solvent dimethyl acetylamide；The raw material of described PET braided tube includes following constituent
And number: PET:70 part, glass fibre: 20 parts, nano silicon: 5 parts,
Modified alta-mud: 5 parts, Polyethylene Glycol: 5 parts.
Described filter membrane is processed prepared as follows:
S1, weigh the raw material of above-mentioned PET braided tube, squeezed by twin screw after raw material is mixed
Go out machine extrusion molding, and work out to obtain PET braided tube by basketry；Double screw extruder
During extrusion molding, one district's temperature is 200 DEG C, and two district's temperature are 220 DEG C, and three district's temperature are
230 DEG C, four district's temperature are 240 DEG C, and the time of staying is 2 minutes.
S2, weigh the raw material of film base material coating, first PVC material is poured in solvent, at 60 DEG C
Lower stirring 2h, is subsequently poured into other raw materials of film base material coating, is warming up to after stirring 23h
85 DEG C, continue stirring at this temperature until the casting solution that is uniformly mixed, then de-
30 DEG C of standing and defoaming 15h in bubble tank.
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step S2
The casting solution that middle standing obtains is beaten to spinning head by dosing pump constant speed, at take-up winding
Under constant speed traction, the casting solution of film base material coating is made to be coated in PET braided tube surface, metering
Pump extrusion frequency is 24Hz, and spinning-drawing machine winding frequency is 20Hz.
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by filter membrane.
In above-described embodiment 1-5, the characteristic of Kynoar in film base material coating material
Viscosity is 1.65-2.0, and weight average molecular weight is 40 ten thousand to 80 ten thousand dalton；Polrvinyl chloride
Average degree of polymerization be 1000-3000；Modified manometer silicon dioxide enters by the following method
Row modification: selection gamma-aminopropyl-triethoxy-silane is coupling agent, is dissolved in ethanol water
Solution is made into the solution that mass concentration is 8-15%, first regulates pH to 3 with glacial acetic acid
Stirring 1-2h, then with ammonia regulation pH value to 11 and stir and add SiO after 1-2h2
It is warming up to 90 DEG C and carries out coupling reaction process 1-2h, be then vacuum dried in 65 DEG C and get final product
Modified manometer silicon dioxide particle.The step S4 first coagulating bath of processing technique contains
There are the solvent dimethyl acetylamide of 40-60%, gel solidification 8-20s, second coagulating bath
In containing the solvent dimethyl acetylamide of 5-20%, gel solidification 5-10s, the 3rd road is clear
It washing trough is clear water.
Comparative example 1
PVC filter membrane common in prior art.
Comparative example 2
Kynoar filter membrane common in prior art.
Filter membrane in embodiment 1-5 and comparative example 1-2 is tested.
It is former water with municipal tap water, inflow temperature≤45 DEG C, maximum pressure of intaking
≤ 0.5Mpa, Inlet and outlet water pressure reduction ＜ 0.2Mpa, tap water influent turbidity is 1.8NTU, warp
Results of property after hyperfiltration membrane assembly of the present invention filters is as shown in table 1.BSA rejection
" University Of Ningbo's material science and Chemical Engineering institute " sample detection report according to test,
With the hyperfiltration membrane assembly of BSA Protein Detection 8-10 ten thousand molecular weight of 6.7 ten thousand molecular weight,
Results of property is as shown in table 1.
Table 1: test result
In sum, filter membrane of the present invention is by adding one layer of inner support in film base material coating
Pipe, and reasonable compatibility film base material coating and the raw material of inner support tube, by simple possible
Processing technique, improve that the stretch capability of filter membrane, ageing resistance be corrosion-resistant, hydrophilic and
Pliability, and then improve water flux and the rejection of film, and significantly improve making of filter membrane
Use the life-span.
Specific embodiment described herein is only to present invention spirit theory for example
Bright.Those skilled in the art can be to described specific embodiment
Make various amendment or supplement or use similar mode to substitute, but without departing from the present invention
Spirit or surmount scope defined in appended claims.
Claims (10)
1. the processing technique of a filter membrane, it is characterised in that described processing technique bag
Include following steps:
S1, weigh the raw material of PET braided tube: PET, glass fibre, nanometer titanium dioxide
Silicon, modified alta-mud, Polyethylene Glycol, squeezed by double screw extruder after being mixed by raw material
Go out molding, and work out to obtain PET braided tube by basketry；
S2, weigh the raw material of film base material coating: Kynoar, polrvinyl chloride, poly-dimension
Ketone, Polyethylene Glycol, solvent, first pour into polrvinyl chloride in solvent, at 60-80 DEG C
Stirring 1-2h, is subsequently poured into other raw materials of film base material coating, heats up after stirring 18-23h
To 85-100 DEG C, continue stirring at this temperature until the casting solution that is uniformly mixed,
Then 30-50 DEG C of standing and defoaming 10-15h in Debubbling tank；
S3, by step S1 prepare PET braided tube penetrate in spinning head, by step
S2 stands the casting solution obtained and beats to spinning head by dosing pump constant speed, at spinning winding
Under the constant speed traction of machine, the casting solution of film base material coating is made to be coated in PET braided tube surface；
S4, film silk is taken off from take-up winding, successively solidify through first under room temperature
Bath, second coagulating bath, the 3rd road rinse bath, can be prepared by by inner support tube and coating
Film base material coating filter membrane dimerous on inner support tube surface.
The processing technique of filter membrane the most according to claim 1, it is characterised in that
The raw material of described PET braided tube includes PET, glass fibre, nano silicon, changes
Property bentonite, Polyethylene Glycol.
The processing technique of filter membrane the most according to claim 2, it is characterised in that
The raw material of described PET braided tube specifically includes the composition of following parts by weight:
PET:50-70 part,
Glass fibre: 5-20 part,
Nano silicon: 5-20 part,
Modified alta-mud: 5-10 part,
Polyethylene Glycol: 5-10 part.
The processing technique of filter membrane the most according to claim 1, it is characterised in that
In step S1, during double screw extruder extrusion molding, one district's temperature is 200-220 DEG C, 2nd district
Temperature is 220-230 DEG C, and three district's temperature are 230-240 DEG C, and four district's temperature are 240-260 DEG C.
The processing technique of filter membrane the most according to claim 1, it is characterised in that
The raw material of described film base material coating specifically includes the constituent of following mass percent:
Kynoar (PVDF): 6-17%,
Polrvinyl chloride (PVC): 4-7%,
Polyvidone (PVP): 3-8%,
Polyethylene Glycol: 12-25%,
Surplus is solvent,
Wherein, Kynoar: the content of polrvinyl chloride is than being (1.5-2.5): 1.
The processing technique of filter membrane the most according to claim 5, it is characterised in that
The raw material of described film base material coating also includes the modification accounting for raw material gross mass 2-4% of coating
Nano silicon.
The processing technique of filter membrane the most according to claim 1, it is characterised in that
After step S2 stirs at 85-100 DEG C, also include before the casting solution being uniformly mixed
Ultrasound wave disperses, and ultrasonic dispersing time is 10-20min.
The processing technique of filter membrane the most according to claim 1, it is characterised in that
The extrusion frequency of dosing pump described in step S3 is 24-28Hz, and spinning-drawing machine winding frequency is
20-26Hz。
The processing technique of filter membrane the most according to claim 1, it is characterised in that
First coagulating bath described in step S4 contains the solvent of 40-60%, gel solidification
8-20s, contains the solvent of 5-20%, gel solidification 5-10s in described second coagulating bath.
The processing technique of filter membrane the most according to claim 9, it is characterised in that
Solvent in described first coagulating bath and second coagulating bath is dimethyl acetylamide.
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| CN106731901A (en) * | 2017-01-19 | 2017-05-31 | 西安建筑科技大学 | Polyester fiber weaves the preparation method of tube enhancement type composite hollow fibre forward osmosis membrane |
| CN108771983A (en) * | 2018-07-04 | 2018-11-09 | 青岛大学 | A kind of multilayer through-hole high penetration polymer micro-filter membrane and preparation method thereof |
| CN114733353A (en) * | 2022-04-14 | 2022-07-12 | 山东产研久膜科技开发有限公司 | Particle size grading device and particle size grading process for superfine powder suspension |
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| CN108771983A (en) * | 2018-07-04 | 2018-11-09 | 青岛大学 | A kind of multilayer through-hole high penetration polymer micro-filter membrane and preparation method thereof |
| CN114733353A (en) * | 2022-04-14 | 2022-07-12 | 山东产研久膜科技开发有限公司 | Particle size grading device and particle size grading process for superfine powder suspension |
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